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Concentration Reduction Effort,Technical Bases & Operational Analysis.
	ML17221A597
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Site:	Saint Lucie
Issue date:	01/22/1988
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880i 290202 880i22 PDR ADOCK 05000335 P ~PDR ATTACHMENT 4 CONCENTRATION REDUCTION EFFORT CEN-353 (F)

TECHNICAL BASES AND OPERATIONAL ANALYSIS ST. LUCIE POWER PLANT UNIT 1 PREPARED FOR FLORIDA POWER 6 LIGHT COMPANY t /

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Table of Contents Section Title Pa e 1~0 Introduction Purpose and Scope 1.2 Report Organization 1-2 1.3 Past vs. Present Methodology for 1"3 Setting BAMT Concentration 2.0 Technical Bases for Reducing BANT 2" 1 Concentration 2.1 Boric Acid Solubility 2-1 2.2 Method of Analysis and Assumptions 2"1 2.2.1 RCS Boron Concentration vs. Temperature 2"1 2.2.2 Impact of Various Cooldown Rates 2-4 2.2.3 Applicability to Future Reload Cycles 2"6 2.2.4 Boron Mixing in the RCS and in the 2"6 Pressurizer 2' Borated Water Sources - Shutdown 2-7 (Modes 5 and 6) 2.3.1 Boration Requirements for Modes 2-7 5 and 6 2.3.2 Assumptions Used in the Nodes 2"7 5 and 6 Analysis 2.3.3 Nodes 5 and 6 Analysis Results 2-8 2.3.4 Refueling Water Tank Boration 2-12 Requirements - Modes 5 and 6

Table of Contents cont.

Section Title Pa e 2.4 Borated Water Source - Operating 2-16 (Nodes 1, 2, 3, and 4) 2.4.1 Boration Requirements for Modes 2-16 1,2,3, and4 2.4.2 Assumptions Used in the Nodes 2-16 1, 2, 3, and 4 Analysis 2.4.3 Modes 1, 2, 3, and 4 Analysis 2-17 Results 2.4.4 Simplification Used Following 2"21 Shutdown Cooling Initiation 2.4.5 Refueling Water Tank Boration 2"22 Requirements - Modes 1, 2, 3 and 4 2.5 Boration Systems - Bases 2-24 2.6 Response to Typical Review guestions 2-25 3.0 Operational Analysis 3-1 3.1 Introduction to the Operational 3"1 Analysis 3.2 Response to Emergency Situations 3-1 3.3 Feed-and-Bleed Operations 3-2 3.4 Blended Makeup Operations 3-4

Table of Contents cont.

Section Title Pa e to Refueling Mode 6 3-5 3.5 Shutdown 3.6 Shutdown to Cold Shutdown Mode 5 3-8 3.7 Long Term Cooling and Containment 3-10 Sump pH 4.0 References 4-1 Appendix 1 Oerivation of the Reactor Coolant System Feed-and-Bleed Equation Appendix 2 A Proof that Final System Concentration is Independent of System Volume Appendix 3 Methodology for Calculating Dissolved Boric Acid per Gallo'n of Water Appendix 4 Methodology for Calculating the Conversion Factor Between Weight Percent Boric Acid and ppm Boron Appendix 5 Bounding Physics Oata Inputs

Boric Acid Concentration Reduction Effort Technical Bases and Operational Analysis CEN - 353 (F) 1.0 INTROOUCTION

1. 1 PURPOSE AND SCOPE This report defines the methodology and outlines the technical bases which allows a reduction in the boric acid makeup tank (BANT) concentration to the point where heat tracing of the boric acid makeup system is no longer required in order to prevent boric acid precipitation. The basic methodology or procedure used to set the minimum SANT concentration and level for Modes 1, 2, 3, and 4 is derived from the safe shutdown requirements of NUREG 0800 Branch Technical Position RSB 5-1, "Design Requirements for the Residual Heat Removal System", (BTP 5-1). The St. Lucie Unit 1 plant has been classified as a Class 3 plant. Two independent boration sour ces are provided to compensate for reactivity changes and all expected transients throughout core life. These boration sources are the boric acid makeup tanks (BAMT) and the refueling water tank (RWT). This report reexamines the design basis used to establish BANT boron concentration and volume requirments.

In addition the minimum RWT volume requirements for RCS boration are recalculated. Specifically, sufficient dissolved boric acid is maintained in these tanks in order to provide the required shutdown margin of Technical Specification 3.1.1. 1 for a cooldown from hot standby to cold shutdown conditions. In addition, the minimum BANT concentration and level for Nodes 5 and 6 are based upon the ability to maintain the required shutdown margin in Technical Specification 3.1.1.2 following xenon decay and cooldown from 200 degrees to 135 degrees.

1-1

The work detailed in this report was performed specifically for the St.

Lucie Unit 1 plant. The calculation performed herein and the values obtained should be applicable to future cycles. (See Section 2.2.3 below). The physics parameters used in this analysis were conservatively selected to bound core physics parameters for the remainder of plant life. Future cycle core physics parameters will be compared to the data in Appendix 5 to ensure that this calculation is bounding. The curve in Figure 3.1-1 of Technical Specification 3.1.2.8 and the values in 3.1.2.7 may change slightly; however, there should not be a need to heat trace the majority of the boric acid system for the remainder of plant life.

'. 2 REPORT ORGANIZATION This report has been organized into three general sections:

Introduction, Technical Bases, and Operational Analysis. The Technical Bases Section 2.0, outlines the methodology which allows a significant reduction in boric acid makeup tank concentration and presents the results of the detailed calculations performed in support of the Technical Specifications. Separate calculations were performed for Specification 3. 1.2.7 (Borated Mater Source - Shutdown), Specification 3.1.2.8 (Borated Mater Source - Operating), and Specification B3/4. 1.2 (Boration Systems Bases). For completeness'the volume requirements of the refueling water tank have been recalculated to demonstrate that the boration requirements for reactivity control in Modes 1, 2, 3 and 4 are much less than the emergency core cooling requirements. Also included in Section 2.0 are the technical responses to typical questions asked by the NRC during review of 'similar submittals by other nuclear facilities. The Operational Analysis Section, Section 3.0, outlines the impact on normal operations of a reduced boric acid makeup tank concentration. The types of operations evaluated in Section 3.0 include feed-and-bleed, blended makeup, shutdown to refueling, and shutdown to cold shutdown. All tables and figures are contained at the end of each section for easy reference.

1-2

1.3 PAST vs. PRESENT HETHOOOLOGY OF SETTING BAHT CONCENTRATION Prior to the development of the new methodology for setting BAHT concentration and level described in this report, the level and concentration specified in the plant Technical Specifications for Modes I, 2, 3, and 4 were based upon the ab1lity to perform a cooldown to cold shutdown in the absence of letdown. (Safe Shutdown requirements of NUREG-0800 BTP 5-1 event). The RCS was borated to the boron concentration required to provide a shutdown margin of 3.6X delta k/k at 200 degrees prior to coamencing plant cooldown. In the limit1ng situation where letdown was not available, this boration was accomplished by charging to the RCS while simultaneously fill1ng the pressur1zer.

Since boron concentration typically had to be increased by 800 ppm or more prior to comaencing cooldown, highly concentrated bor1c ac1d solut1ons were required due to the limited space that was available in the pressurizer.

Relat1vely recent advances have made it poss1ble to develop new methodologies for setting BAHT concentration and levels. The methodology for setting concentration and level of Hodes 1, 2, 3, and 4 described in this report differs from previous methodologies in that boration of the reactor coolant system is performed concurrently with plant cooldown, i.e., concentrated boric acid is added concurrently w1th cooldown as part of normal inventory makeup due to coolant contraction. By knowing the exact boron concentration required to maintain proper shutdown margin at each temperature during a plant cooldown, BAHT concentration can be decoupled from pressur1zer volume. As a result, the concentrat1on of boric acid required to be ma1ntained 1n the boric acid makeup tanks in order to perform a cooldown without letdown to cold shutdown conditions can be lowered to a range of 2.5 to 3.5 wt'A, where heat trac1ng of the boric acid system is no longer requ1red, i.e., the amb1ent temperatures that normally ex1st in the plant's auxil1ary building are sufficient to prevent boric acid precipitation.

1-3

Similarly, a new methodology was developed for setting the minimum concentration and level of the boration source required to be operational in Modes 5 and 6. Since letdown is available in Mode 5 and 6 cooldown scenarios, a feed and bleed can be conducted to increase RCS boron concentration. Additionally boration can be conducted concurrently with cooldown as part of normal system makeup. By insuring that the boron concentration is maintained greater than that required for proper shutdown margin at each temperature, the boric acid makeup tank concentration for Modes 5 and 6 can be lowered to 2.5 weight percent.

1-4

0 2.0 TECHNICAL BASES FOR REDUCING BAHT CONCENTRATION 2.1 BORIC ACID SOLUBILITY Figure 2-1 is a plot show1ng the solubility of boric ac1d in water for temperatures ranging from 32 to 160 degrees. (Data for Figure 2-1 was obtained from Reference 4.1 and is reprinted in Table 2-1.) Note that the solubility of boric acid at 32 degrees is 2.52 weight percent and at 50 degrees is 3.49 weight percent. At or below a concentration of 3.5 J

weight percent boric acid, the ambient temperature that normally exists in the auxiliary bu1lding will be sufficient to prevent precipitation with1n the boric acid makeup system.

2.2 METHOD OF ANALYSIS AND ASSUMPTIONS 2.2. I RCS Boron Concentr ation v . Tem erature 2.2. 1. 1

~ ~ ~ Operating Hodes. I, 2, 3 and 4 As stated 1n Sect1on 1.3 above, the methodology developed to allow a signif1cant reduct1on 1n the boric acid concentrat1on requ1red to be maintained in the BAHTs in Hodes 1, 2, 3, and 4 differs from the previous methodology in that boration of the reactor coolant system is performed concurrently with cooldown in order to insure proper shutdown margin, 1.e., concentrated boron 1s added as part of normal system makeup during the cooldown process. To employ a methodology allowing boration concurrent with cooldown, the exact boron concentration required to be present in the reactor coolant system must be known at any temperature during the cooldown process. In addition, in order to 1nsure applicability for an ent1re cycle, a cooldown scenario must be developed wh1ch is conservative 1n that it places the greatest burden on an operator's ability to control reactivity, i.e., this scenario must define the boration requirements for the most limiting t1me in core cycle. Such a limiting scenario is as follows:

2-1

1. Conservative core physics parameters were used to determine the required boron concentration and the required Boric Acid Makeup Tank volumes to be added during plant cooldown. End-of-cycle initial boron concentration is assumed to be zero. End-of-cycle moderator cooldown effects are used to maximize the reactivity change during the plant cooldown. Beginning-of-cycle boron reactivity worths (which are smallest at the beginning of cycle) are used to maximize the amount of boron that must be added to provide the required reactivity change. These assumptions assure that the required boron concentration and the Boric Acid Makeup Tank minimum volume requirements conservatively bound all plant cooldowns during core life.

2. The most reactive rod is stuck in the full out position.

3. Prior to time zero, the plant is operating at 10'ower with 10(C equilibrium xenon. Zero RCS leakage.

4. At time zero, the plant is shutdown and held at hot zero power conditions for 25.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months . (The xenon peak after shutdown will have decayed back to the 10(5 power equilibrium xenon level. Further xenon decay will add positive reactivity to the core during the plant cooldown.) No credit was taken for the negative reactivity effects of the xenon concentration peak following the reactor shutdown.

5. At 25.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months , offsite power is lost and the plant goes into natural circulation. All non-safety grade plant equipment and components are lost. During the natural circulation the RCS average temperature rises 25'F due to decay heat'in the core. The initial temperature at the start of the cooldown is 557'F.

6. Approximately 0.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months later, at 26 hours3.009259e-4 days 0.00722 hours 4.298942e-5 weeks 9.893e-6 months , the operators commence a cooldown to cold shutdown.

2-2

The scenario outlined above was used to generate the boration requirements for Modes 1, 2, 3, and 4 (Specification 3. 1.2.8). It produces a situation where positive reactivity will be added to the reactor coolant system simultaneously from two sources at the time that a plant cooldown from hot shutdown is commenced. These two reactivity sources result from a temperature effect due to an overall negative isothermal temperature coefficient of reactivity, and a poison effect as the xenon-135 level in the core starts to decay below 1ts equil1brium value at 100K power. Th1s scenario, therefore, represents the greatest challenge to an operators ability to borate the reactor coolant system and mainta1n the required Technical Specification shutdown marg1n while cooling the plant from hot standby to cold shutdown conditions.

2.2. 1.2 Operating Modes 5 and 6 The methodology developed for Modes 5 and 6 differs from the method used in previous refueling cycles to determine bor ation requirements. In this new methodology boration of the reactor coolant system is performed concurrently with cooldown. Concentrated boric acid is added as part of normal system makeup dur1ng the cooldown process. To employ a methodology allowing boration concurrent with cooldown, the exact boron concentration required to be present in the reactor coolant system must be known at any temperature during the cooldown process. The follow1ng scenario was developed to 1dent1fy the most 11miting cooldown transient for Modes 5 and 6.

l. End-of-cycle conditions w1th the in1t1al RCS boron concentrat1on necessary to provide shutdown margins of 2.0X delta k/k at 200 degrees and xenon free core. EOC moderator cooldown effects are used to maxim1ze the react1v1ty change during the'lant cooldown.

BOC boron worths are used since they are the smallest over core 11fe, therefore, requiring the greatest overall 1ncrease in boron concentration in order to maintain proper shutdown margin.

2-3

2. Most reactive rod is stuck in the full out position.

3. Zero RCS leakage.

4. RCS feed-and-bleed can be used to increase boron concentration.

5, RCS makeup is supplied either from the RWT alone or a combination of makeup from the BANT and RWT.

6. The most limiting scenario for boration in Node 5 requires that a 2%

gk/k shutdown be maintained during the cooldown from 2004F to 1354F.

The boration requirements for Mode 6 only address maintaining a previously established shutdown margin. If the required shutdown margin for Node 6 is not maintained, Technical Specification 3.9.1 requires that the RCS be borated at 40 gallons per minute from source of wate~ > 1720 ppm boron. Technical Specification,3. 1.2.7 provides three alternative sources to meet this requirement, either

,BAMT or the RWT..

The scenario outlined above was used to determine the boration requirements for Nodes 5 and 6 (Specification 3.1.2.7). It produces a situation where positive reactivity will be added to the reactor coolant system due to the overall negative isothermal temperature coefficient of reactivity. Since the core is already assumed to be xenon free there is no contribution to core reactivity due to xenon decay.

2.2.2 Im act of Various Cooldown Rates As discussed in the previous Section, a conservative cooldown scenario was selected for use in determining RCS boron. concentration levels.

These concentration results were then used to define the minimum 2-4

Technical Spec1fication boric acid makeup tank 1nventory requirements.

In the scenario for Modes 1, 2, 3, and 4, positive reactivity was added simultaneously from two sources at the time that the plant cooldown from hot standby was commenced. The component resulting from an overall negative isothermal temperature coeffic1ent of react1vity 1s independent of time, but it is directly dependent upon the amount that the system has been cooled. In contrast, the component that results from the decay of xenon-135 below its equilibr1um value at 10% power 1s 1ndependent of temperature, but directly dependent upon time. As a result, a slow cooldown rate will require more boron to be added to the reactor coolant system than a fast cooldown rate for a given temperature decrease since more positive react1vity must be accounted for due to xenon decay. This effect is illustrated in Figure.2-2 and is appl1cable to the Modes 1, 2, 3, and 4 analysis. Note that the bases for Techn1cal Specificat1on 3.1.2.7 require a cooldown following xenon decay. As a result, borat1on requirements are independent of cooldown rate for the Modes 5 and 6 analysi s.

For the purpose of sett1ng the miniamm Technical Specification boric acid makeup tank inventory requirements in Modes 1, 2, 3, and 4, reactor coolant system boron concentration data was used that was based upon an overall cooldown rate of 12.5 degree per hour. This slow cooldown rate was chosen in order to be cons1stent with the time frames spec1fied 1n Section 6.2 of Reference 4.3 (natural circulation cooldown in CE NSSS) for reactor vessel upper head cooldown. Specif1cally, 23.07 hours8.101852e-5 days 0.00194 hours 1.157407e-5 weeks 2.6635e-6 months was required in order to take the plant from hot standby conditions to cold shutdown as shown in Table 2-2. For addit1onal conservatism, 5.73 hours8.449074e-4 days 0.0203 hours 1.207011e-4 weeks 2.77765e-5 months was added to this number to arrive at a f1nal total of 28.8 hours9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months . An overall cooldown rate, therefore, of 12.5 degrees per hour was required to cool the plant from an average coolant temperature of 557 degrees to an average coolant temperature of 200 degrees 1n 28.8 hours9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months . Th1s cooldown scenario will conservatively bound cooldowns that occur sooner and/or at a higher cooldown rate. The above scenario bounds the 2-5

reactivity affects of a BTP 5-1 cooldown. It is assumed in the BTP 5-1 scenario that the RHR will be capable of bringing the RCS to cold shutdown conditions within 36 hours4.166667e-4 days 0.01 hours 5.952381e-5 weeks 1.3698e-5 months . With respect to Xenon reactivity affects the scenario used in this report bounds the 36 hour4.166667e-4 days 0.01 hours 5.952381e-5 weeks 1.3698e-5 months cooldown time frame of BTP 5-1 (26 hours3.009259e-4 days 0.00722 hours 4.298942e-5 weeks 9.893e-6 months to let Xenon return to 100% equilibrium level and 28 hours3.240741e-4 days 0.00778 hours 4.62963e-5 weeks 1.0654e-5 months for a slow cooldown).

2.2.3 A licabilit to Future Reload C cles To ensure that the current analys1s would be valid for future cycles, data from St. Lucie 1 Cycle 6 was conservatively bounded. The physics data used in this analys1s should bound future fuel cycles of similar reload cores. Appendix 5 contains bounding physics assumptions that were used to produce the required boron concentration values. As long as these inputs are more conservat1ve than the reload cycle physics parameters, the values produced 1n this analys1s will bound the boron concentration values for the future. reload cycles.

2.2.4 Boron Mixin in the RCS and in the Pressurizer Throughout the plant cooldowns performed in Section 2.3 and Section 2.4 below, a constant pressurizer level was always assumed, 1.e., plant operators charged to the RCS only as necessary to makeup for coolant contraction. The dr1ving force 1s small, in th1s s1tuat1on, for the mixing of fluid between the reactor coolant system and the pressurizer.

As a conservatism, however, complete and instantaneous mixing was assumed between all makeup fluid added to the reactor coolant system through the loop. charging nozzles and the pressurizer. Further, various pressure reduct1ons were performed during the plant cooldown process as 1ndicated in Section 2.4. These pressure reductions are necessary since the shutdown cooling system is a low pressure system and is normally aligned at or below an RCS pressure of 268 psia. Typically, such 2-6

depressurizations are performed using the auxiliary pressurizer spray system under conditions where the reactor coolant pumps are not running.

As an added conservatism in the Modes 1, 2, 3, and 4 analysis, any boron added to the pressurizer via the spray system was assumed to stay in the pressurizer and not be ava1lable for mixing with the flu1d in the remainder of the RCS.

2.3 BORATED WATER SOURCES SHUTDOWN (HODES 5 AND 6) 2.3.1 Boration Re uirements for Hodes 5 and 6 As stated in the plant Technical Specificat1ons, the boration capacity required below a reactor coolant system average temperature of 200 degrees is based upon providing a shutdown margin of 2.(5 delta k/k following xenon decay and a plant cooldown from 200 degrees to 135 degrees. From this basis the required RCS boron concentrations were determined using conservative core physics data. The results of these calculations are contained 1n Table 2-3. The results contained in Table 2-3 are plotted as the required shutdown curve in Figure 2-3. Note that a total boron concentration increase of 69.2 ppm for St. Lucie 1 was required for the cooldown.

2.3.2 Assum tions Used in the Hodes 5 and 6 Anal sis A complete list of assumptions and initial cond1t1ons used 1n calculating the minimum boric acid makeup tank inventory requirements for Modes 5 and 6 is contained 1n Table 2-4. In the process of taking the plant from hot standby to cold shutdown, the shutdown cooling system (SDCS) will normally be aligned when the RCS temperature and pressure have been lowered to approximately 325 degrees and 268 ps1a for St. Lucie l. As shown in the next Sect1on, the total system volume, i.e., RCS volume plus PZR volume plus SDCS volume, 1s required to be known for the Modes 5 and 6 analysis. The exact volumes of the reactor coolant system and the 2-7

pressurizer are known. The exact volume of the shutdown cooling system, however, is not known. (Best estimate calculations for this volume have yielded values from approximately 2500 ft to approximately 3000 ft ).

3 3 For the purpose of the analysis in the following Section, the volume of the shutdown cooling system will be chosen conservatively large, equal to the RCS volume, so as to yield conservative results with respect to minimum boric acid makeup tank inventory requirements.

The exact system volume used in the Modes 5 and 6 calculation is as fol 1ows:

2 x (RCS volume) + (PZR volume at l5 power),

or 2(9601 ft ) + (460 ft ) 19 662 ft 2.3.3 Modes 5 and 6 Anal sis Results As stated in Section 2.3.1, the boration capacity required below a reactor coolant system average temperature of 200 degrees is based upon providing shutdown margins of 2.0X delta k/k for St. Lucie 1 following xenon decay and a plant cooldown from 200 degrees to 135 degrees. The operating scenario that will be employed for the purpose of determining reactor coolant system boron concentration and ensuring that proper shutdown margin will be maintained is as follows:

2-8

A. The systems are initially at 200 degrees and 268 psia. Initial concentration in the reactor coolant system, pressurizer, and in the shutdown cooling system is 702.2 ppm boron. (See Table 2-4 for a complete list of assumptions).

B. Perform a plant cooldown from an average temperature of 200 degrees to an average temperature of 135 degrees using makeup water from the BANT (2.5 weight %%d boric acid solution at 70 degrees). Charge only as necessary to makeup for coolant contraction.

From Equation 2.0 of Appendix 3 and the conversion factor that is derived in Appendix 4, the initial boric acid mass in the system can be calculated as follows:

702.2 m f 19 202 ft + 460 ft mb ba

= 1748.34 m wt. % L 0.01662 ft ibm

- (702.2 ppm)/(1748.34 ppm/wt.

0.01874 ft ibm 100 %)

or ba

= 4758.0 ibm boric acid Knowing the initial mass of boron in the system, the exact concentration and makeup requirements can be calculated for each 10 degrees of a cooldown from 200 degrees to 135 degrees. These values are contained in Table 2-6.

Fquations used to obtain the values shown in Table 2-6 are as follows:

2-9

Shrinkage Mass 19,202 (1/vf 1/vi)

Water Vol. (Shrinkage Mass) / (8.329 ibm/gallon) (1)

Boric Acid Added (Water Vol.) x (0.19172 ibm/gallon) (2)

Total Boric Acid (Initial Boric Acid) + (Boric Acid Added)

Total System Mass (Total Initial Mass) + (Shrinkage Mass) +

(Boric Acid Added)

Final Conc. Total Boric Acid 100 1748.34 (

(Total System Hass)

Note that the initial total system mass of, 1,184,651.2 ibm in Table 2-6 was obtained as follows:

(Initial Boric Acid) + (Initial System Water Hass) +

(Pressurizer Water Mass)

= 4758.0 ibm + (19,202 ft / 0.01662 ft /ibm) +

(460 ft / 0.01874 ft /ibm)

= 1,184,651.2 lb@

(1) ,Water density at 70 degrees.

(2) See Appendix 3 for values of dissolved boric acid in water.

(3) See Appendix 4 for the conversion factor between wt. X and ppm.

2-10

The boration results from the system cooldown from 200 to 135 degrees are plotted as the actual concentration curve in Figure 2-3. As can be seen from this figure,a shutdown margin of greater than the required 2.0% delta k/k was maintained throughout the evaluation. A minimum concentration of 2.5 weight 5 boric acid was therefore specified in the plant Technical Specification 3.1.2.7. The minimum'volume that should be specified in the Technical Specification is 3650 gallons. This volume was determined as follows:

Makeup volume (4) 3114 8

~ gallons Arbitrary amount 500.0 gallons for conservatism Total 3614.8 gallons Round up to nearest 3650 gallons 50 gallons (4) Total of values in Mater Vol. column of Table 2-6.

2-11

2.3.4 Refueling Mater Tank Boration Requirements - MODES 5 5 6 The RWT will not provide enough boric acid to compensate for the reactivity inserted during the cooldown if charging is restricted to makeup for coolant contraction only. A system feed-and-bleed must be performed to raise the RCS concentration before the cooldow'n is commenced. The initial feed-and-bleed ensures that the actual RCS boron concentration is maintained above the required boron concentration for a 2.0gdelta k/k shutdown margin while the plant is cooled from 200 degrees to 135 degrees.

For St. Lucie 1, in order to calculate the initial increase in boron concentration during the 8270 gallon system feed-and-bleed, Equation 9.0 of Appendix 1 will be used with values as follows:

C = 702.2 ppm = 1720 ppm 0 Cin T = 19 202 ft 0.01662 ft ibm + 460 ft / 0.01874 ft ibm 40 gallons 0.343 ibm min gallon T = 3535.6 min.

(5) Specific volume of compressed water at 200'F and 268 psia (6) Specific volume of saturated water at 268 psia (7) Density of water at 50 F 2-12

e If one charging pump at 40 gpm (as assumed in calculating the value of T above) is used to conduct the system feed-and-bleeds, 206.75 minutes are required (8270 gal/40 gpm = 206.75 min). Concentrations vs time for the feed-and-bleeds from equation 9.0 of Appendix 0 are therefore:

Time Conc 0 702.2 30 710.9 60 719.3 90 727.8 120 736.2 150 744.5 180 752.7 206.75 760.0 The feed-and-bleed portion of the cooldown process is indicated on Figure 2-4 as the vertical line. As shown, concentrations were increased from 702.2 ppm to 760.0 ppm following the 8270 gallon feed-and-bleed.

From Equation 2.0 of Appendix 3 and the conversion factor derived in Appendix 4, the mass of boric acid in the system corresponding to concentrations of 760.0 ppm can be calculated as follows:

2-13

CM M

ba 100- C 760.0 m 1748.34 wt.X 19 202f) 0.016628 lbm+460f) 0.01874f) ibm 100 - (760.0ppm)/(1748.34ppm/wt.X)

= 5151.4 ibm bor1c ac1d Knowing the masses of boric ac1d in the system following the feed-and-bleeds, the exact concentrations and makeup requirements can be calculated for each 10 degrees of cooldowns from 200'F to 135'F. These values are contained 1n Table 2-7. The cooldown assumes a constant pressurizer volume of 460 ft and 3

a constant pressure of 268 psia. In add1tion, complete m1x1ng between the RCS and the PZR is assumed as discussed in Section 2.2.4 above. Equations used to obtain the values contained 1n Table 2-7 are as follows:

Shr1nkage mass 19,202 (1/vf 1/vi)

Water Vol. = (Shr1nkage mass) / (8.343 ibm/gallon)

Boric acid added (water vol.) (0.08289 ibm/gallon)

Total boric ac1d init1al bor1c ac1d + boric ac1d added Total System mass = Total initial mass + shrinkage mass + boric acid added Final concentration ~ Total Boric Acid 100 1748.34 Total System Mass 2-14

The results of the initial system feed-and-bleed plus the plant cooldown are plotted as Curve 2 in Figure 2-4. Note that throughout the evaluation, a shutdown margin greater than 2.0% delta k/k was maintained as required.

The initial total system mass in Table 2-7 was obtained as follows:

Initial boric acid mass + initial system water mass + initial PZR water mass =

5151.4 ibm + (19,202 ft )-/ (0.01662 ft /ibm) + (460 ft ) / (0.01874 ft /ibm)

= 1,185,052.8 ibm ~

RMT concentrations of 1720 ppm will therefore be specified in Technical Specification 3.1.2.7 since the proper shutdown margin could be maintained.

The minimum volume will be specified as follows for the RWT cooldown:

Feed-and-Bleed Volume 8,270.0 gallons Makeup Volume 3,108.8 gallons Total 11,378.8 Round up to nearest 11,900 gallons 50 + 500 gallons With 60,000 gallons of the RWT unusable, the actual required volumes in the RMT at 1720 ppm is 71,900 gallons for St. Lucie 1.

2-15

2.4 BORATED WATER SOURCES OPERATING (HOOES 1, 2, 3, and 4) 2.4.1 Boration Re uirements for Hodes 1 2 3 and 4 For this analysis a shutdown marg1n of 3.6X delta k/k 1s provided at all temperatures above a reactor coolant system average temperature of 200 degrees. For temperatures at or below 200 degrees, a shutdown margin of 2.0% delta k/k is provided after xenon decay and cooldown to 200 degrees.

From this basis, the required RCS'boron concentrations were determined us1ng conservative core phys1cs parameters and the limit1ng cooldown scenar1o outlined 1n Sect1on 2.2. 1 above. The results are plotted as the shutdown curve in Figure 2-5.

2.4.2 Assum tions Used in the Hodes 1 2 3 and 4 Anal sis A complete list of assumpt1ons and 1nitial condit1ons used 1n calculating the minimum bor1c ac1d makeup tank inventory requ1rements for Hodes j., 2, 3, and 4 are contaiaed 1n Table 2-5. Note that complete and instantaneous mixing between the reactor coolant system and the pressurizer was assumed as stated 1n Sect1on 2.2.4 for all fluid added to the reactor coolant system via the loop charging nozzles. The mechanism used to implement th1s assumption in the analysis was to include the pressurizer water mass as part of the total system mass for the purpose of calculat1ng boron concentration. Spec1fically, boron concentration in terms of weight fraction is defined as follows:

(boron conc.) mass of boron in s stem (total system mass) where, if complete mix1ng 1s assumed between the RCS and the pressurizer, the total system mass 1s the sum of the boron mass in the system, the reactor coolant system water mass, and the pressurizer water mass.

2-16

Therefore, the initial total system mass of 467,651.2 ibm in Table 2-8 through Table 2-32 for St. Lucie 1 was calculated as follows:

Initial boron mass + Initial RCS water mass + Initial PZR water mass,.

or 9 601 ft 600 ft 0.021567 ft /lbm (8) 0.02669 ft /ibm(9) 2.4.3 Modes 1 2 3 and 4 Anal sis Results As stated in Section 2.4. 1, the boration capacity required below a reactor coolant system average temperature of 200 degrees is based upon providing a 2.0% delta k/k shutdown margin after. xenon decay and a plant cooldown to 200 degrees from expected operating conditions. In addition for this analysis a shutdown margin of 3.6% delta k/k is provided at all temperatures above a reactor coolant system average temperature of 200 degrees. In order to perform a plant cooldown from hot standby conditions to cold shutdown and maintain the above shutdown margin at each temperature above 200 degrees, the following operating scenario will be employed:

A. Assuming the initial conditions outlined in Table 2-5, perform a plant cooldown starting from an initial RCS average temperature of 557 degrees to a final average system temperature of 200 degrees.

B. Charge to the RCS only as necessary to makeup for coolant contraction. Charge from the BAMT initially until BAMT is drained, then switch to the RWT for the remainder of the cooldown.

(8) Specific volume of compressed water at 557 degrees arid 2200 psia.

(9) Specific volume of saturated water at 2200 psia.

2-17

The exact reactor coolant system boron concentrations versus temperature for, plant cooldowns and depressurizations from 557 degrees and 2200 psia to 200 degrees and 268 psia with a boric acid makeup tank concentration of 3.50 weight percent and a refueling water tank concentration of 1720 ppm boron is contained in Table 2-8. These results are plotted as the actual concentration curve in Figure 2-5. (The exact temperature at which contraction makeup was switched from the BAMTs to the refueling water tank was determined via an iterative process. In this process, the smallest boric acid makeup tank volume necessary to maintain the required shutdown margin was calculated for the given set of tank concentrations).

Note that at each temperature during the cooldown process, RCS boron concentration is greater than that required for the shutdown margin of 3.6% delta k/k. Also note in Figure 2-5 that the shutdown margin drops from 3.6% delta k/k to 2.0% delta k/k at an average coolant temperature of 200 degrees. Following xenon decay the final concentration required to be present in the system at the most limiting time in core cycle are 702.2 ppm boron. Using the scenario outlined on the previous page, the final system concentration will always be at least 80:0 ppm greater than this amount. A detailed parametric analysis was performed for the modes 1, 2, 3, and 4 Technical Specification (Specification 3.1.2.8). In this study, BANT concentration was varied from 3.5 weight percent boric acid to 2.5 weight percent boric acid and RMT concentration was varied from 1720 ppm boron to 2300 ppm boron. The results are contained in 2-18

Table 2-9 through Table 2-32. Equations used to obtain the values in these tables as well as Table 2-8 are as follows:

Shrinkage Hass = 9601 (1/vf - 1/vi)

BAHT Vol. (Shrinkage Hass) / (8.3290 ibm/gallon) (10)

RWT Vol. (Shrinkage Hass ) / (8.343 ibm/gallon)

Boric Acid Added (BAHT Vol.) x (mass of boric acid/gallon) or (RWT Vol.) x (mass of boric acid/gallon)(

Total Boric Acid (Initial Boric Acid) + (Boric Acid Added)

Total System Hass (RCS water mass) + (PZR water mass) (13)'

(Total boric acid)

Final Conc. Total Boric Acid 100 1748.34 (Total System Hass)

(10) Oensity of water at assumed tank temperature 70'F.

(11) Oensity of water at assumed tank temperature 50'F.

(12) See Appendix 3 for values of dissolved boric acid in water.

(13) PZR water mass ~ (600 ft3

) / (specific volume at indicated Psat).

(14) See Appendix 4 for the conversion factor between wt. 5 and ppm.

2-19

Note that the value of the total system mass at any temperature and pressure in Table 2-8 through Table 2-32 can be obtained as follows:

RCS water mass + PZR water mass + total boric acid mass =

total system mass.

As an example, the value of the total system mass at 200 degrees and 268 psia in Table 2-8 was obtained as follows:

9 601 ft-3 600 ft-3 + 2921.4 ibm 0.01662 ft /ibm 0.01874 ft /ibm(")

= 612,616.0 ibm.

In a similar manner as in the results of Table 2-8, the concentration results of Table 2-9 through Table 2-32 were compared to the required concentrations at each temperature for a plant cooldown from 557 degrees to 200 degrees which are contained in Table 2-33. In each case, the actual system boron concentrations were greater than that necessary for the required shutdown margin as indicated in Figure 2-5. To set the minimum Technical Specification boric acid makeup tank volume corresponding to the various BAHT and RWT concentrations, the (15) Specific volume of compressed water at 200 degrees and 268 psia.

(16) Specific volume of saturated water as 268 psia.

2-20

makeup tank volumes from Table 2-8 through Table 2-32 were compiled into Table 2-34. The volume requirements were rounded up to the nearest 50 gallons. Oepressurizing from 2200 psia to 1200 psia is accomplished by providing auxiliary spray from the BAMTs to depressurize the plant to 1200 psia which is below the HPSI pump shutoff head. 1000 gallons has been added to the rounded values determined above in order to provide water for auxiliary spray to provide depressurization from BAMT and Figure 2-6 is produced.

In a similar manner, Figure 3.1-1 of the St. Lucie 1 Technical Specifications is produced with 1000 gallons added. This figure replaces the original Technical Specification Figure 3.1-1.

2.4.4 Sim lification Used Followin Shutdown Coolin Initiation In the cooldown and depressurization process assumed in Table 2-8 through Table 2-32, the plant operators must physically align the shutdown cooling systems at a RCS temperature and pressure of approximately 325 degrees and 268 psia. Following this alignment, the volume and mass of the system that the operator must contend with during any subsequent cooldown will obviously increase by the volume and mass associated with the shutdown cooling system. Further, the total boron mass in the system that the operator is now dealing with will also have increased by the amount of boron in the SOCS prior to alignment. In Table 2-8 through 2-32, as a simplification, no attempt was made to factor into the equations the higher total volume and total boron mass that would result when the shutdown cooling system is placed i'n service. The use of these simplifications in the Modes 1, 2, 3, and 4 calculations can be justified as follows:

2-21

At the time that the shutdown cooling system is aligned, makeup is being supplied from the refueling water tank. Therefore, additional makeup that would be required during the cooldown from 300 degrees to 200 degrees due to a larger system volume will not affect the total BAMT volume requirements. This assumption would affect the minimum volume requirement of the RWT in Modes 1, 2, 3, and 4. Since the RWT requirements for emergency core cooling are much greater than the requirements for this'cooldown scenario, this simplification does not impact RWT sizing requirements.

2. In a cooldown process where an operator is charging only as necessary to makeup for coolant contraction, the change in boron concentration within the system is independent of the total system volume, i.e., the final system boron concentration is not a function of total system volume. (A proof of this statement is contained in Appendix 2).

3. As stated in Table 2-5 boron concentration in the SOCS is assumed to be equal to reactor coolant system concentration at the time of shutdown cooling initiation. This assumption is in fact a conservatism since the concentration in that system in most situations will be closer to refueling water tank concentration at the time of initiation.

2.4.5 Refuelin Water Tank Boration Re uirements - Modes 1 2 3"and 4 The refueling water storage tank provides an independent source of borated water than can be used to compensate for core reactivity changes and expected transients throughout core life.. It should be noted that in Nodes 1,2,3 and 4 the minimum RWT water volume is 401,800 gallons as required by emergency core cooling considerations. The purpose of this section of the report is to demonstrate that the RWT minimum inventory requirement in Nodes 1, 2, 3 and 4 to compensate for these reactivity changes during a shutdown are much less than the emergency core cooling requirements.

2-22

This calculation derives the minimum quantity of RWT water necessary to bring the plant from hot standby to cold shutdown while maintaining the plant at a 3.6X delta k/k shutdown margin. All RCS makeup is supplied by the'WT with a boron concentration 1720 ppm. This cooldown is performed as described below.

A. Perform a RCS feed-and-bleed to raise RCS boron concentration from 0 ppm to 579 ppm boron. This is a three hour feed-and-bleed using three charging pumps.

B. Perform a plant cooldown from an initial RCS temperature of 557 degrees and 2200 psia to 325 degrees and 268 psia. Charge only as necessary to makeup for coolant contraction.

C. Align the shutdown cooling system (SOCS) to the RCS at 325 degrees.

Assume that the SOCS volume is 9601 ft . Assume that the concentration of the SOCS is equal to that of the RCS at time SOCS initiation.

O. Continue cooldown from 325 degrees and 268 psia to a final RCS condition of 200 degrees and 268 psia. Charge only as necessary to makeup for coolant contraction.

Table 2-36 contains the results of the calculated volumes in Steps A through O. The RWT boration requirements for Nodes 1, 2, 3 and 4 has been rounded up to 45,000 gallons. Figure 2-9 shows the RCS boron concentration as the plant cooldown progresses. As expected the boration requirements imposed on RWT sizing are much smaller than the minimum volume requirements placed on the RWT by emergency core cooling requirements (401,800 gallons).

2-23

2.5 BORATION SYSTEHS - BASES The BASES section of the technical spec1fications was developed to demonstrate the boration system capabil1ty to maintain adequate shutdown margin from all operating cond1t1ons. Section 3/4.1.2 of the plant Techn1cal Spec1fications will be changed to state the following:

"The boration capability of either system is suffic1ent to provide a SHUTOOWN HARGIN from all operat1ng cond1t1ons of 2.(5 delta k/k after xenon decay and cooldown to 200'F. The max1mum borat1on capab1lity requirement occurs at EOL from full power equ1libr1um xenon condit1ons.

This requirement can be met for a range of boric ac1d concentrations in the BAHT and RWT. Th1s range is bounded by 7317.1 gallons of 3.5 weight X bor1c ac1d from the BAHT and 14,000 gallons of 1720 ppm borated water from the RWT to 12,271.2 gallons of 2.5 weight A boric acid from the BAHT and 9,000 gallons of 1720 ppm borated water from the RWT.

The 14,000 gallon RWT volume for St. Lucie 1 1n Section 3/4.1.2 of the plant Technical Specificat1ons was obtained by assum1ng RCS makeup was prov1ded from the BAHT and the RWT. Total RCS makeup due to the coolant contraction dur1ng cooldown is calculated as descr1bed 1n A, B and C below. Th1s yielded a contraction volume of 20,965.2 gallons. From this volume the min1mum BAHT volume for the RWT at 1720 ppm boron from Table 2-34, 7317.1 gallons was subtracted yield1ng 13,648 gallons, wh1ch was rounded up to 14,000 gallons. As a result of the addition of 3.5 weight

% boric ac1d from the BAHT, a feed-and-bleed 1s not requ1red to ma1ntain the shutdown margin of 2.0X delta k/k. Table 2-35 shows how this RWT volume was calculated.

A. Perform plant cooldowns from 557 degrees and 2200 psia to 325 degrees and 268 psia using the RWT- at 1720 ppm boron and 50 degrees.

Charge only as necessary to makeup for coolant contraction. (See Table 2-5 for complete list of assumptions and 1nitial conditions).

2-24

B. At 325 degrees and 268 psia align shutdown cooling system. Assume that the volume of the shutdown cooling system is 9,601 ft as discussed in Section 2.3.2 above. Assume that the concentration of the shutdown cooling system is equal to that of the reactor coolant system at the time of shutdown cooling initiation.

C. Continue system cooldown from 325 degrees and 268 psia to 200 degrees and 268 psia using the RMT. Charge only as necessary to makeup for coolant contraction.

A plant cooldown using water from the RMT alone is discussed in Section 2.4.5 of this report. This cooldown scenario provides the minimum RMT water volume requirement for plant cooldown considerations of 45,000 gallons. This number is contained in Technical Specification Bases 3/4.1.2.

2.6 RESPONSE TO REVIEM QUESTIONS This Section of the report details the responses to the typical questions asked during the review of the Technical Specifications.

Question 1: Mhat are the uncertainties and conservatisms associated with the two curves shown in Figure 2-5 of this report?

2-25

Response to guestion 1:

The lower curve in Figure 2-5 of this report represents an upper bound on the minimum concentrations required to be present in the reactor coolant system for a required shutdown margin at the indicated temperatures. In the computer analyses that were performed to generate these curves, appropriate analytical and measurement uncertainties as well as appropriate conservatisms were included to ensure that an upper bounding curve was obtained. The major uncertainties and conservatisms that were factored into the required shutdown curve of Figure 2-5 was as follows:

1. Initial scram is assumed to take place from the hot full power PDIL (power dependent insertion limit) to all rods in, with the worst case rod stuck in the full out position.

2-26

2. A bias and uncertainty of -1(5 was applied to the scram worth for the Unit 1 data.

3. A conservative correct1on was appl1ed to the St. Lucie Unit 1 moderator cooldown data to adjust the cooldown curve to the Technical Specification MTC of -2.8 x 10 +'F.

4. A combined bias.and uncertainty of 1% was appl1ed to the corrected moderator data.

5. A b1as of 15% and an uncertainty of 15% was applied to the Ooppler data.

6. The assumption that the cooldown beg1ns at 26 hours3.009259e-4 days 0.00722 hours 4.298942e-5 weeks 9.893e-6 months is conservat1ve 1n relat1on to the bu1ldup and decay of Xenon.

Since appropr1ate analyt1cal and measurement uncertainties as well as appropriate conservatisms associated with the analys1s were factored into the lower curve 1n Figure 2-5, it is not necessary to factor any additional uncertainties or conservatisms directly 1nto the upper curve shown in that f1gure. Although no additional uncerta1nt1es were included in the upper curve, the cooldown scenar1o followed by the operator was specifically chosen to be conservative such that the actual concentration curve in Figure 2-5 in effect represents a lower bound on the boron concentration that can be achieved by an operator given a certain boric ac1d makeup tank (BAHT) level and boron content. Specifically, conservat1sms in the cooldown scenario were 1nsured 1n two ways. First, the cooldown was conducted assuming a constant pressurizer level, i.e.,

plant operators charged to the reactor coolant system only as necessary to makeup for coolant contraction. As a result,.boron 'concentration in the reactor coolant system can be increased above the upper curve in Figure 2-5 by over-charging during the cooldown process, i.e., charge in excess of the makeup required for coolant contraction by allowing 2-27

pressurizer level to increase. Second, the BAHT volumes obtained in Table 2-8 through Table 2-32 of this report were rounded up to the nearest 50 gallons and 1000 gallons were added 1n order to give the final results that appear in Figure 2-6. Boron concentration in the reactor coolant system, therefore, can be increased further since more inventory 1s available in the BAHTs than that used to generate the actual concentration curve in Figure 2-5.

guestion 2: What are the implicat1ons of a reduction in boric acid makeup tank concentrations with respect to plant emergency procedures and Combust1on Engineering's Emergency Procedure Guidelines7 Response to guestion 2:

As stated in Sect1on 3.2 of th1s report cred1t 1s not taken for boron addition to the reactor coolant system from the bor ic acid makeup tanks for the purpose of reactiv1ty Control in the accidents analyzed 1n Chapter 15 of the plant's Final Safety Analys1s Report. The response of an operator, therefore, to such events as steam line break, overcooling, boron dilution, etc., w1ll not be affected by a reduct1on 1n BAHT concentrat1on. In particular, the act1on statements associated with Techn1cal Specif1cat1on 3.1.1.2 require that boration be commenced at greater than 40 gallons per minute using a solution of at least 1720 ppm boron in the event that shutdown margin 1s lost. Such statements are conservatively based upon the refueling water tank concentration and are therefore 1ndependent of the amount of boron in the BAHTs.

S1milar to the Techn1cal Specif1cat1on act1on steps 1n the event of a loss of shutdown margin, the operator guidance in Combust1on Engineering's Emergency Procedure Guidelines (EPGs), CEN-152, Rev. 2, are also 1ndependent of spec1fic boron concentrations within the boric acid makeup tanks. Specif1cally, the acceptance crfter1a developed for the 2-28

reactivity control section of the Functional Recovery Guidelines of CEN-152 are based upon a boron addition rate from the chemical and volume control system (CVCS) of 40 gallons per minute without reference to a particular boration concentration. Chapter 15 Safety Analysis assume that any makeup from the CVCS be supplied at concentrations of at least 1720 ppm boron (the minimum RWT concentration). The reduction in boron concentration within the boric acid makeup tanks therefore has no impact on, and does not change, the guidance contained in the EPGs.

(}uestion 3: Under natural circulation conditions, show that boron mixing in the reactor coolant system is rapid enough to ensure that proper shutdown margin is maintained during a safe shutdown. What is the effect of various cooldown rates on the mixing process'f an operator charges only as necessary to makeup for coolant contraction; what is the impact of pressurizer level instrument errors on boron concentration?

Response to guestion 3:

As discussed in Section 1.1 of this report the basic methodology or procedure used to set the minimum boric acid makeup tank (BAMT) level and concentration for Nodes 1, 2, 3, and 4 is derived from the safe shutdown requirements of Branch Technical Position (RSB) 5-1. Specifically, sufficient dissolved boric acid is maintained in these tanks in order to provide the required shutdown margin of Technical Specification 3. 1.1. 1 for a cooldown from hot standby to cold shutdown conditions. Further, the methodology outlined in Section 2.0 of the report for Modes 1, 2, 3, and 4 was developed by incorporating appropriate conservatisms to insure that the shutdown margin of 3.6% delta k/k would indeed be satisfied at each temperature during the cooldown process.

These conservatisms include a cooldown scenario that maximized the boration requirements due to xenon decay. In Section 2.0 the cooldown was not commenced until twenty-six hours after the reactor trip. This 2-29

time interval allowed the post tr1p xenon to peak and decay back to the pre-trip steady state value. Select1ng the low cooldown rate of 12.5 degrees per hour maxim1zed the xenon contribution to the boration requirement by allowing more xenon decay dur1ng the cooldown than would have occurred if a more rap1d cooldown had been conducted.

Boron mixing effects were evaluated for natural circulation cooldown condit1ons specified in the safe shutdown requirements of Reference 4.4.

Just pr1or to event init1ation, the plant 1s operat1ng at 100% of rated thermal power. Previous operating history is such as to develop the maximum core decay heat load. At t1me zero, event init1ation occurs and offs1te power 1s lost. The reactor coolant pumps deenergize caus1ng a reactor trip, and the plant goes into natural c1rculation. All non-safety grade equipment 1s lost, 1ncluding letdown, and one d1esel generator fa1ls to start. The plant is held at these conditions in hot standby for four hours, at wh1ch t1me a cooldown to cold shutdown 1s commenced. (Sect1on 5.4 of CEN-201(S), Supplement No. 1, contains a computer simulation of the safe shutdown scenar1o of Reference 4.3 and shows these events).

The exact boration requirements that give a 3.6X shutdown margin for these scenarios are shown in Figure 2-7. (These curves were obta1ned using conservat1ve core phys1cs parameters. Note that the above shutdown curves 1n these figures are based upon a 100 degree per hour cooldown rate. A cooldown rate of 100 degrees per hour was selected for the following reasons: First, a fast cooldown rate is more limiting than a slow cooldown w1th respect to boron m1x1ng since the slope of the required boration curve is greater. The effect of the assumed m1xing time (less than th1rty minutes) would be more adverse then than a cooldown at a slower cooldown rate (see Figure 2-7). Second, a 100 degrees per hour cooldown rate is the maximum allowable. For an added conservatism the actual RCS boron concentratiorr was derived by using BAHT concentrations of 2.5 weight percent. (BAHT concentrations of 2.5 weight 2-30

X was selected since these are the lowest values that will be allowed by Technical Spec1f1cation 3.1.2.8 and since 1t yields the slowest 1ncreases in reactor coolant system concentrat1ons during the cooldown process).

The actual concentrat1on curves were obtained using the methodology outlined in Section 2.4 of this report and includes the following assumptions and conservatisms:

1. No boron add1tion is credited pr1or to commencing plant cooldown.

(Note that one charging pump will operate 1mmediately following plant tr1p in response to pressur1zer level shrink as 1nd1cated in Section 5.4 of CEN-201(S), Supplement No. 1. Credit for boron addition, however, during this period will not be taken).

2. Pressurizer volume at the start of plant cooldown equals 460 ft3 .

3. Charging will be secured at the start of the plant cooldown and wi)l remain secured unt11 pressurizer level has decreased by 10%. (In the methodology outlined 1n th1s report operators were assumed to charge as necessary to maintain a constant pressur1zer level. Note that the error associated with pressurizer level is 'typically + 2 percent, therefore allowing a 10 percent decrease in level before init1at1ng charging is conservative).

4. Following the init1al 10K decrease 1n pressurizer level, charging w1ll be in1tiated and maintained as necessary to keep pressur1zer levels constant for the remainder of the plant cooldown.

5. Complete and instantaneous mixing with all flu1d added via the charg1ng nozzles with the contents of the RCS and the pressur1zer is assumed. (Note that this assumpt1on 1n relat1on to a delay 1n boron mix1ng will be d1scussed below).

2-31

The concentration curves that were obtained using these assumptions are shown in Figure 2-7. In order to account for the effects of a delay in the boron mixing process under natural circulation conditions, the actual concentration curve in Figure 2-7 will be shifted to the right by 0.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months . (Note that 30 minutes is consistent with the boron mixing time that was determined in CEN-259 and, in addition, is conservative since CEN-259 also indicates that significant mixing of added boron does occur prior to 30 minutes). These shifts are shown in the expanded graphs shown 1n Figure 2-8. As can be seen, the concentrations within the reactor coolant system for the 0.5 houi sh1ft curves in F1gure 2-8 above the requ1red shutdown curve at each temperature dur1ng the cooldown.

2-32

Table 2-1 Boric Acid Solubility in Water Temperature (Oegrees F) Wt. 'X H 80 32.0 2.52 41.0 2.98 50.0 3.49 59.0 4.08 68.0 4.72 77.0 5.46 86.0 6.23 95.0 7.12 104.0 8.08 113.0 9.12 122.0 10.27 131.0 11.55 140.0 12.97 149. 0 14.42 158.0 15.75 167.0 17.91 176.0 19.10 (1) Solubility from Technical Oata Sheet IC-ll, US Borax 8 Chemical Corporation, 3-83-J.W.

2-33

Table 2-2 Time Frames for Determining an Overall RCS Cooldown Rate Initial Hot Standby hold 4.0 hours0 days 0 hours 0 weeks 0 months period (+)

Plant cooldown from 557 to 2.32 hours3.703704e-4 days 0.00889 hours 5.291005e-5 weeks 1.2176e-5 months 325 degrees (8)

Hold period for cooling the 15.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months reactor vessel upper head Plant cooldown from 325 1.25 hour2.893519e-4 days 0.00694 hours 4.133598e-5 weeks 9.5125e-6 months s to 200 degrees (0)

Additional conservatism 5.73 hours8.449074e-4 days 0.0203 hours 1.207011e-4 weeks 2.77765e-5 months Total 28.8 hours9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months

(*) Per the requirements of Branch Technical Position (RSB) 5-1.

(0) Assume an average cooldown rate of 100 degrees per hour.

2-34

Table 2-3 Required Boron Concentration for a Cooldown from 200 Degrees to 135 Degrees Concentration Temperature'Degrees F) (ppm boron) 200 702.2 190 712.8 180 723.5 170 734.1 160 744.8 150 755.4 140 766.1 135 771. 4 (9) Based upon a 2.Nf delta k/k shutdown margin after xenon decay.

2-35

Table 2-4 Initial Conditions and Assumptions Used in the Hodes 5 and 6 Calculation

a. Reactor coolant system volume = 9,601 ft3 .

b. Reactor coolant system pressure 268 psia.

c. Pressurizer volume 460 ft .

d. Pressurizer is saturated.

e. Zero reactor coolant system leakage.

f. Boration source concentration 2.25 weight X boron.

g. Boration source temperature 70 degrees.

h. Initial reactor coolant system concentration 702.2 ppm

i. Initial pressurizer concentration 702.2 ppm boron.

Complete and instantaneous mixing between the pressurizer and the reactor coolant system. (Refer to discussion on Section 2.2.4 above).

Constant pressurizer level maintained during the plant cooldown, i.e.,

charge only as necessary to makeup for coolant contraction.

Total system volume (RCS + SDCS + PZR) 19,662 ft . (See discussion in Section 2.3.2).

2-36

Table 2-5 Initial Conditions and Assumptions Used in the Hodes I, 2, 3, and 4 Calculation

a. Reactor coolant system volume = 9,601 ft3

b. Initial reactor coolant system pressure = 2200 psia.

c. Pressurizer volume = 600 ft3 (4'evel).

d. Pressurizer is saturated.

e. Reactor coolant system depressur1zat1on performed as shown in Table 2-8 through Table 2-32.

f. Zero reactor coolant system Technical Spec1fication leakage.

g. Init1al reactor coolant system concentrat1on 0 ppm.

h. Initial pressurizer concentrat1on 0 ppm boron.

Complete and instantaneous mixing between the pressur1zer and the reactor coolant system. (Refer to discussion on Section 2.2.4 above).

Constant pressurizer level ma1ntained during the plant cooldown, 1.e.,

charge only as necessary to makeup for coolant contract1on.

k. Boron concentrat1on 1n the SOCS is equal to the boron concentration in the reactor coolant system at the t1me of shutdown cool1ng 1nit1at1on.

l. Letdown 1s not ava1lable.

m. RAT temperature 50 degrees.

n. BAHT temperature 70 degrees.

2-37

TABLE 2-6 PLANT COOLMW fROH 200 F TO 135 f; RAH'I AT 2.5 eN RORIC ACID IAVO.SVS. TON PZR PRESS SPECIFIC VOLIRIE 'SNRINKACE RAHT VOL 8 RNT VOL Q 8/A ADOEO TOTAL 8/A TOTAL SYS. HASS f INAL CONC. I I (F) (pa(a) (cU f t./Iba) HASS(lba) 70 F (gal) 50 f (gal) (lba) (Iba) (lba) (ppe boron) I I

Ti 200 Tf 200 268 Vi 1.00000 Vf 1.00000 0.0 0.0 0.0 0.0 4,758.0 1, 184,659.5

""I 702.2 I

I 200 190 268 0.01662 0.01656 4,186.1 502.6 0.0 107.3 4,865.4 1~ 188,952.9 715.4 I 190 180 268 0.01656 0.01650 4,216.5 506.2 0.0 108.1 4,973.5 1 ~ 193,277.5 728.7 I 180 170 268 0.01550 0.01644 4,247.3 509.9 0.0 108.9 5,082.4 1, 197,633.7 741.9 I 170 160 268 0.01644 O.OI &38 4,278.4 513.7 0.0 109.7 5,192.1 1,202,021.8 755.2 I 160 150 268 0.01638 0.01633 3,589.4 430.9 0.0 92.0 5,284.1 1,205,703.2 766.2 I 150 140 268 0.01633 0.01628 . 3,611 4 433.6 0.0 92.6 5,376.7 1,209,407.2 777.3 I 140 'I35 268 0.01628 0.01626 1,814.0 217.8 0.0 Cd.5 5,423.2 1,211,267.7 782.8 I I

I TOTAL RANT VOLTE 3114.8 gal iona I

I I I I I

I I

TABLE 2-7 PLANT CODLD04I fRON 200 f TO 'l35 f; RMI AT I720 ppa RDRON

)AVG.STS. TENP. PZR PRESS SPECIFIC VOLINIE SHRINKAGE RANT VDL 8 RQT VOL 8 6/h ADDED TOTAL 6/A TOTAL SYS. NASS f INAL CONC.)

I (F) (pa i a) (cu. f t./Ilaa) NASS(ita) 70 f (Ral) 50 F (gaI) (Ibi) (IIaa) (lba) (ppa boron) )

Ti Tf Vi Vt

-"--"""I I I 200 200 268 1.00000 1.00000 0.0 0.0 0.0 0.0 5,151.4 . I ~ 185,052.8 760.0 f I 200 190 268 0.01662 0.01656 4,166.1 0.0 501.7 41.6 5,193.0 1,169,260.5 763.4 )

I 190 150 265 0.01656 0.01650 4,216.5 0.0 505.4 41.9 5,234.9 1,193,538.9 766.d )

I 150 170 268 0.01650 O.OI644 4,247.3 0.0 509.1 42.2 5,277.1 I, 197, 82d.4 770.2 (

I 170 160 265 0.01644 0.016M 4,275.4 0.0 512.5 42.5 5,319.6 1,202,149.3 773.7 (

I 160 150 265 0.01638 0.01633 3,589.4 0.0 430.2 35.7 5,355.2 l,205,774.3 776.5 I I 150 140 265 0.01633 0.01628 3,611.4 0.0 432.9 35.9 5,391.1 1,209,421.6 779.3 )

I 140 135 26b 0.01628 0.01626 1,814.0 0.0 217.4 lb.0 5,409.2 1,211,253.6 760.8 )

I I

)TOTAL ROT VOL(HIE 3109.6 gal Iona I I

I I

TABLE 2-8 I

I- PLANl COOLDDQI FRDH 557 F TO 200 Fl BAHT AT 3.5 utX BORIC ACID; RUT AT 1720 ppa BORON I

IAVO.SYS. TEHP PLR PRESS SPECIFIC VOLLRLE SNRINKACE BAHT VOL Q RLTT VOL Q 8/A ADDED TOTAL 8/A TOTAL STS. HASS FINAL CONC.I (f) (paia) (cu.ft./Lbs) HASS(Lba) 70 f (gaL) 50 f (gal) (Lba) (LIaa) (Llaa) (ppta boron) I Ti Tf Vi Vf I I I I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I I 557 510 2200 0.02157 0.02032 27,319.3 3,2M.O 0.0 990.9 990.9 495,961.3 3C9.3 I I 510 490 2200 0.02032 0.01990 9,912.2 1,197.3 0.0 361.7 1,352.5 50&,295;2 4&7.1 I I 490 480 2200 0.01990 0.01910 4,898.1 588.1 0.0 117.7 ~

1,530.2 511,310.9 523.2 I I 480 470 2200 0.01970 0.01951 4,746.2 5&9.$ 0.0 112. \ 1,102.3 51&,289.3 51&.S I I 470 460 2200 0.01951 0.01933 4,582.5 550.2 0.0 166.2 1,868.5 521,038.0 &27.0 I I 460 450 2200 0.01933 0.01916 4,406.9 529.1 0.0 159.8 2,028.4 525,604.8 674.7 I I 450 438 2200 0.01916 0.01897 5,018.9 602.6 0.0 182.0 2,2I0.4 530,805.7 lbs.1 I I 43S C30 2200 0.01897 0.01885 3,222.0 0.0 386.2 32.0 2,242.4 534,059.& 73C.1 I 430 420 2200 O.OISS5 0.01670 4,085.& 0.0 469.7 40.6 2,283.0 538,185.8 741.7 I I C20 410 2200 0.01870 O.OISS5 4,151.7 0.0 C97.6 41.2 2,324.3 542,378.7 7C9.2 I I 410 400 2200 0. 01855 0.01842 3,652.8 0.0 437.8 36.3 2,360.6 5CS,O&l.d 155.d I I 400 390 2200 0.01842 0.0182$ 3,991.9 0.0 C78.5 39.7 2,C00.2 550,099.C 762.8 I I 390 380 2200 O.OIS28 O.OI81S 3,470.6 0.0 416.0 34.5 2,434.7 553,604.5 768.9 I I 380 370 2200 0.0181& 0.01804 3,516.8 0.0 421.5 34.9 2,4e9.e 557,156.2 715.0 I I 370 360 2200 O.oldOC 0.01192 3,5&3.9 0.0 427.2 35.4 2,505.1 560,755.5 781.0 I

.I 360 350 2200 0.01792 0.01781 3,309.1 0.0 396.6 32.9 2,537.9 5&4,097.4 78&.6 I I 350 340 2200 0.01781 0.01770 3,350.2 0.0 401.6 33.3 2,571.2 567,C$ 0.9 792.2 I I 340 330 2200 0.01710 0. 01759 3,392.1 0.0 40&.6 33.7 2,604.9 570,90S.l 791.1 I I 330 325 2200 0.01159 0.01754 1,555.9 0.0 166.5 15.5 2,620.4 572,476.1 800.3 I

. I 325 310 2M 0.0115C 0.01754 0.0 0.0 0.0 0.0 2,620.4 5S2,014.9 787.1 I

'lrlv IA '8 AA A Ar'W I 6 r ~ '%I 't r '7 4 rc ~ v4 abc rr ~ ~

I

~~ A

~ ~ rv v v ~~

~

~ rv v Av rtv v rr ~ v~ gyve Jvry ~Ivv ~ rv I 300 260 26$ 0.0114C 0.01701 11,932.7 0.0 1,430.3 118.6 2,710.1 597,235.9 810.9 I I 2&0 235 268 0.01701 0.01667 &,668.0 0.0 '99.2 6S.2 2,83&.4 &03,970.2 821.1 I 235 210 26$ O.OIMl 0.01669 6,137.9 0.0 735.7 61.0 2,891.3 610, 1&9. I S30.2 I I 210 200 2&d 0.01669 0.D ie&2 2,422.9 0.0 290.4 2C.1 2,921.4 612,616. 0 S33.7 I I I IlOTAL BAHT VDLLRLE 7317.1 gaL Iona I I I

TABLE 2-9 I I I PLANT COOLDOAI FROH 557 F TO 200 F; RAHT AT 3.25 stX RORIC ACID; RUT AT 1720 ppa ROROH l I I

)AVG.STS. TEHP. P?R PRESS SPECI flC VOLLNE SHRIICAGE QAHT VDL 0 RN VOL 6 8/A ADDED 'TOTAL 5/A TOTAI. STS. HASS FIHAL COHC. )

I (F) (peia) (cu.ft./Iba) HASS(iba) 70 f (gal) 50 f (gal) (lba) (lba) ( Iba) (ppa boron) )

Ti Tf Vi Vf I I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I 557 - 510 2200 0.02157 0.02032 27,319.3 3,260.0 0.0 9I7.7 917.7 495,8M.2 323.6 I 510 490 2200 0.02032 0.01990 9,972.2 I,197.3 0.0 335.0 1,252.7 506, 195.3 432.7 I 490 CM 2200 0.01990 0.01970 4,895.'I Mb. 1 0.0 164.5 1,C17.2 511,258.0 C64.7 )

450 470 2200 0.01970 0.01951 4,746.2 569.5 0.0 159.4 1,576.7 Sle. 163.6 534.0 )

C70 460 2200 0.01951 0.01933 4,562.5 550.2 0.0 153.9 1,730.6 520,900.0 580.9 )

CM 450 2200 0.01933 0.01916 4,406.9 529.1 0.0 148.0 1,678.7 525,455.0 625.1 450 440 2200 0.01916 0.01900 C,2I9.8 506.6 0.0 Nl.b 2,020.4 529,8I6.5 666.7 )

440 430 2200 0.01900 0.01655 452.8 0.0 135.1 2,155.5 533,972.7 705.8 )

4,021.1',065.6 C30 420 2200 O.0IMS 0.01570 490.S 0.0 137.2 2,292.7 535,195.5 744.5 I 420 410 2200 0.01870 0.01555 4,151.7 0.0 497.6 41.2 2,334.0 SC2,365.4 752.3 f 410 400 2200 0.01855 0.01842 3,652.5 0.0 437.5 36.3 2,370.3 546,077.5 755.9 )

400 390 2200 0.01542 0.01828 3,99I.9 0.0 478.5 39.7 2,409.9 550, 109.1 765.9 I 390 380 2200 0.01828 0.01516 3,470.6 0.0 416.0 34.5 2,444.4 553,614.2 772.0 )

380 370 2200 0.01816 0.01MC 3,51d.b 0.0 42I.S 3C.9 2,479.3 557,165.9 77S.O i 370 360 2200 0.01604 0.01792 3,563.9 0.0 C27.2 35.C 2,51C.S 560,765.2 784.0 )

360 350 2200 O.0I792 0.01781 3,309.1 0.0 396.6 32.9 2,547.d 564,107.1 789.6 I 350 340 2200 0.01751 0.01770 3,350.2 0.0 40l.d 33.3 2,580.9 567,C90.6 795.1 )

340 330 2200 a.a177a 0.01759 3,392.1 0.0 406.6 33.7 2,6N.6 570,916.C 600.7 )

330 325 2200 0.01759 0.0175C 1,555.9 0.0 156.5 IS.S 2,630.1 572,457.8 603.2 (

325 310 265 O.OI75C O.0 I75C 0.0 0.0 0.0 0.0 2,d30.1 552,024.d 790.0 )

310 300 26S 0.0175C 0.0174C 3,136.6 0.0 376.2 31.2 2,661.3 585,194.C 795.1 )

300 260 26S O.0I7CC 0.01707 11,932.7 0.0 1,430.3 118.d 2,779.8 597,2C5.6 513.7 I 260 235 268 0.01707 0.01657 6.665.0 0.0 799.2 66.2 2,646.1 603,979.9 S23.8 )

235 210 268 O.0I6S7 0.01669 6, 137.9 0.0 735.7 61.0 2,907.0 610,178.6 833.0 I 210 200 268 0.01669 0.01662 2,C22.9 O.a 290.4 24.1 2,931.1 612,625.7 836.5 )

I

[TOTAL RAHT VOLm S194.5 gallons I I I

TABLE 2-l0

(

PLANT COOLDONI FROH 557 F TO 200 F; RAHT AT 3.0 at% RORIC ACID) RM'I AT '1720 ppa BORON I

.I (AVG.STS. TEIN'~ P?R PRESS SPECIFIC VOLlNE SNRIID(AGE RANT VOL 0 RNT VOL 0 5/A ADDED TOTAL 5/A TOTAL SYS. HASS FINAL CONC I I (F) (pa(a) (cu.f t./Iba) HASS(lba) 70 F (gal) 50 F (gal) (Iba) (Iba) ( Ibs) (ppe boron) (

Tl Tf Vi Vf I

I I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I I 557 510 2200 0.02157 0.02032 27,319.3 3,280.0 0.0 544.9 644.9 495,515.4 297.9 I I 510 ,C90 2200 0.02032 0.01990 9,972.2 '1,197.3 0.0 305.4 I, 153.4 506,096.0 395A I I 490 C80 2200 0.01990 0.01970 4,698.1 565. I 0.0 151.5 '1,304.5 511, 145.6 4C6.3 I I C60 C70 2200 0.01970 0.01951 4,746.2 569.5 0.0 1C6.5 I,CS I.e 516,035.6 491.5 (

I 470 C60 2200 0.01951 0.01933 4,562.5 550.2 0.0 141.7 '1,593.4 520,762.8 534.9 I I 460 450 2200 0.01933 0.01916 C,C06.9 529.1 0.0 136.3 1,729.7 525,306.0 57S.7 (

I 450 440 2200 0.01916 0.01900 4,219.5 506.d 0.0 130.$ 1,660.2 529,656.3 6'14.0 I I 440 430 2200 0.01900 0.01885 4,021.1 452.8 0.0 124A 1,964.5 S33,601.7 650.0 I I 430 420 2200 O.OIMS O.OI570 C,055.6 490.$ 0.0 126.4 2, 110.9 S38,013.7 656.0 I I 420 410 2200 0.01870 O.OI555 4,151.7 495.5 0.0 128A 2,239.3 SC2,293.7 721.9 (

I 410 398 2200 0.01555 0.01539 4,446.3 533.5 0.0 137.5 2,376.8 546,577.6 7S9.9 I

, I 398 390 2200 0.0'1539 0.01825 3,195.4 0.0 363.4 31.5 2,405.6 550,107.7 les.s (

I 390 380 2200 0.01825 0.01516 3,470.6 0.0 cle.o 3C.S 2,CC3.1 553,612.5 771.5 I I 380 370 2200 O.OI816 0.0180C 3,5 I6.5 0.0 C21.5 34.9 2,C78.0 557,16C.S 777.6 I I 370 360 2200 0.01804 0.01792 3,563.9 0.0 427.2 35.4 2,513.4 560,763.5 783.6 (

I 360 350 2200 0.01792 0.01751 3,309.1 0.0 396.d 32.9 2,546.3 564, 105.5 789.2 I

'350 3CO 2200 0.01/81 0.01/70 3,350.2 0.0 C01.6 33.3 2,579.6 567,489.3 I 794.7 I I 3CO 330 2200 0.01770 D.0 1759 3,392.1 0.0 '06.6 33.7 2,613.3 570,915.1 600.3 I I 330 325 2200 0.01759 0.0175C 1,555.9 0.0 Ibe.s 0.0 2,613.3 572,471.0 798.1 I I 325 3lu 268 0.0175C 0.01754 0.0 0.0 0.0 0.0 2,613.3 582+007.5 785.0 I I 310 300 268 0.01754 0.01744 3,138.6 0.0 3le.2 31.2 2,64C.S 565 ~ 177.6 790.1 I I 300 260 2M 0.01744 0.01707 11,932.7 0.0 1,430.3 . 11b.d 2,763.0 597,225.5 808.9 I I 260 235 265 0.01707 O.0IMl e,eM.O 0.0 799.2 66.2 2,629.3 603,963.'I 619.0 I I 235 210 2M 0. 01687 0.01669 6,137.9 0.0 735.7 61.0 2,890.2 610,162.0 826.2 I I 210 700 268 0.01669 0.01662 2,C22.9 0.0 290.4 24.1 2,914.3 612,M8.9 531.7 I I I I TOTAL BAHT VOLUHE 9226.7 gallons I

I I

TABLE 2-11 I

PLANt COOLDQAI FROH 557 F TO 200 Ft RAHT AT 2.75 sstX RORIC ACIDI RVT At '1720 ppsa SDRQI I I

IAVr..STS. TEHP. PZR PRESS SPECIFIC VOLWE SHRINKAGE SAHt VOL 0 RVT VDL 8 8/A ADDED TOTAL 8/A TOtAL SYS. HASS FINAL CHIC. I I (paia) (cu.ft./Iba) HASS(lba) 70 F (gal) 50 F (gal) (Iba) (Iba) (lba) (ppsa boron) I I Ti Tf VI VF I I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,65 I.2 0.0 I 557 510 2200 0.02157 0.02032 27,319.3 3,250.0 0.0 772.5 772.5 C95,743.0 272.4 I 510 490 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 282.0 1,054.5 505,997.1 364.4 I C90 450 2200 0.01990 0.01970 4,895.1 555.1 0.0 13S.5 1,193.0 511,033.7 COS.I 4SO 4'/0 2200 O.OI970 0.01951 4, /Ce.z 569.5 0.0 134.2 1,327.2 5 I5,914.1 449.8 I 470 C&0 2200 0.01951 0.01933 4,582.5 550.2 0.0 129.6 1,456.5 szo.eze.z 459.2 I ceh ccn os ho n nsosa n nsosc c cDc 0 5~.1 hn ~ 'M CCS C C CC wa

~ C'0 a+ e+o 0 C'll ssV C I 450 440 2200 0.01916 0.01900 4,219.8 506.6 0.0 119.3 '1,700.7 529,496.5 561.6 I 440 430 2200 0.01900 0.01585 4,021.1 C82.S 0.0 113.7 1,514.4 533,631.6 594.5 I 430 420 2200 0.01585 O.OI870 4,055.6 C90.5 0.0 115.5 1,930.0 537,532.7 627.C I 420 410 2200 0.01570 0.01855 4, 151.7 495.5 0.0 117.4 2,047.4 5C2,101.5 6&0.3 I C10 400 2200 0.01S55 0.018C2 3,652.8 435.6 0.0 103.3 2,150.6 545,657.9 685.5 I COO 390 2200 O.OISC2 0.01828 3,991.9 479.3 0.0 112.9 2,263.5 5C9,962.7 719.6 I 390 380 2200 O.OISZS 0.01516 3,470.6 416.7 0.0 95.1 2,361.7 553,531.4 745.9 I 380 370 2200 D.OISI& 0.0150C 3,516.5 422.2 0.0 99.4 2,461.1 557,1C7.6 772.3 I 370 360 2200 O.0I504 0.01792 3,563.9 0.0 427.2 35 4 2,49&.5 560,746.9 77$ .4 I 360 350 2200 O.OI792 O.OI751 3,309.1 0.0 396.6 32.9 2,529.4 56C,085.9 764.0 I 350 3CO 2200 0.0 lrbl 0.01770 3,350.2 0.0 401.6 33.3 2,562.7 Sdr,472.4 759.5 I 3CO 330 2200 0.01770 0.01759 3,392.1 0.0 CO&.6 33.7 2,596.4 570,695.2 795.1 I 330 325 2200 0.01759 0.01754 1,555.9 0.0 166.5 15.5 2,611.5 572,I69.6 797.7 I 325 310 268 0.01754 0.0175C 0.0 0.0 0.0 0.0 2,611.$ 562,006.3 7SC.6 I 310 300 268 0.01754 0.01744 3,138.d 0.0 376.2 31.2 2,6C3.0 585, Ire.z 789.7 I 300 260 265 0.01744 0.01707 11,932.7 0.0 1,430.3 118.6 z,rel.e 597,227.4 SOS.C I 260 235 26$ 0.01707 0.01657 d,668.0 0.0 799.2 66.2 2,827.5 603,961. 7 Slb.d I 235 210 26b 0.01657 0.01669 6,137.9 0.0 735.7 d1.0 Z,bbb.b 610, 160.5 Szr.b I I 210 200 26S 0.01669 0.01662 2,422.9 0.0 290.4 24.1 2,9I2.9 612,607.5 53I.3 I I I I TOTAL BAH'I VOLUHE 10449.7 gal long I I I

TABLE 2-12 I

PLAN'I COOLDONN FRDH 557 f To 200 fI BAHT AT 2.50 stX BQIIC ACID; RNT AT 1720 PPa BORON I

I (AVC.STS. TEIN' PZR PRESS SPECI F IC VDLIRIE SHRIINAGE BAHT VOL 0 RUT VOL Q B/A ADDED TOTAI. 8/A TOTAI. STS. NASS FINAI. CONC. )

I (F) (paia) (ou.ft./Iba) MASS(lba) 70 F (gal) 50 f (gal) (lba) (lba) (lba) (ppa boron) )

Ti Tf Vi Vf I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,d51.2 0.0 )

557 510 2200 0.02157 0.02032 27,319.3 3,280.0 0.0 700.5 700.5 495,671.0 247.1 I 510 490 2200 0.02032 O.OI990 9,972.2 1,197.3 0.0 255.7 956.2 505,89S.S 330.4 I 490 Cbo 2200 0.01990 0.01970 4,89$ .1 5M. I 0.0 125.6 '1,081.8 510,922.5 370.2 I 4M C70 2200 0.01970 0.01951 C,746.2 569.$ 0.0 121.7 1,203.5 515,790.4 407.9 )

Cro Ceo 2200 0.01951 0.01933 4,582.5 550.2 0.0 117.5 1,321.0 520,490.4 443.7 I Cdo 450 2200 0.01933 0.01916 4,C06.9 529.1 0.0 113.0 1,434.0 525,010. 3 477.5 I 450 440 2200 O.0I916 0.01900 4,219.8 506.6 0.0 10$ .2 1,542.1 529,33$ .3 509.4 )

440 430 2200 0.01900 O.OIM5 4,021.1 C82.d 0.0 103.1 1,645.3 533,C62.5 539.2 (

430 420 2200 O.OIM5 0.01870 C,085.6 C90.5 0.0 10C.S 1,750.0 537,652.8 569.1 420 410 2200 0.01870 0.01855 4,151.7 498.5 0.0 106.5 1,856.5 541,910.9 59$ .9 I 410 400 2200 0.01855 0.01842 3,652.8 C38.6 0.0 93.7 1,950.1 scs,esr.c 624.$ I 400 390 2200 0.01842 O.OIS2$ 3,991.9 479.3 0.0 102 4 2,052.5 549,751.6 es2.r ~

390 380 2200 0.0182$ 0.oldie 3,470.6 416.7 0.0 $ 9.0 2,141.5 553,311.2 ere.r ~

380 370 2200 0.01816 0.01804 3,516.$ 422.2 0.0 90.2 2,231.d 556,91$ .2 700.6 )

370 360 2200 0.01804 0.01792 3,563.9 C27.9 0.0 91.4 2,323.0 560,573.C 724.5 I 360 350 2200 0.01792 0.01781 3,309.1 397.3 0.0 84.$ 2,407.9 563,967.C 746.5 I 350 340 2200 0.01781 O.OI770 3,350.2 402.2 0.0 $ 5.9 2,493.8 567,403.5 76$ .4 340 330 2200 0. 01770 0.01759 3,392.1 407.3 0.0 87.0 2,580.7 570,M2.6 790.4 )

330 325 2200 0.01759 0.01754 1,555.9 186.8 0.0 39.9 2,620.6 572,C78.4 800.3 (

325 310 26$ 0.0175C 0.01754 0.0 0.0 0.0 0.0 2,620.6 582,015. 1 787.2 I 310 300 26$ 0.0175C 0.0174C 3,13$ .6 0.0 376.2 31.2 2,651.$ 5S5, 184.9 792.3 )

300 260 268 0.017CC 0.01707 11,932.7 0.0 I,C30.3 118.6 2,770.4 597,236.2 811.0 I 260 235 26S 0.01707 O.0ldbr 6,6M.D 0.0 799.2 66.2 2,$ 3d.6 603,970.5 821.1 )

235 210 2M 0.01687 0.01669 6, 137.9 0.0 735.7 el.o 2,897.6 610, 169. 3 8$ 0.3 I 210 200 268 0.01669 0.01662 2,422.9 0.0 290.4 24.1 2,92'I.r 612,616.2 833.$ )

I I

)TOTAL RANT VDLIjNE 12271.2 gallons I

I I

TABLE 2-13 PLANT COOLDOQI TRON 557 F TO 200 F; RANT AT 3.5 vtX BORIC ACID; RVT AT 1850 ~ BORON I

I I

IAVG.STS. TENP. PZR PRESS SPECIFIC VOLWE SHRINKAGE BAHT VOL 0 RNT VOL 0 8/A ADDED TOTAL B/A 'TOTAL STS. NASS FINAL CONC.I

( (f) (pe I a) (cu. t t./I laa) NASS( Ibs) 70 F (gal) 50 F (gal) (Iba) (lba) ( lba) (ppaa boron) I Ti TF Vi Vt 557

- ".-"""""""-".-"".I I I 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 C67,651. 2 0.0 I I 557 510 2200 0.02 I 51 0.02032 27,319.3 3,280.0 0.0 990.9 990.9 495,961.3 349.3 I I 510 490 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 361.7 1,352.5 506,295. 2 467.1 I 490 4M 2200 0.01990 0.01970 4,898.1 5M.1 0.0 177.7 1,530.2 511,370.9 523.2 I I CSO C70 2200 O.0I970 0.01951 4,746.2 569.$ 0.0 172.1 1,702.3 516,289.3 576.5 I I C70 C60 2200 0.01951 0.01933 4,582.5 550.2 0.0 166.2 1,868.5 521,03$ .0 621.0 I I C60 450 2200 0.01933 O.0I916 4,406.9 529.1 0.0 159.$ 2,02$ .4 525,604.8 674.7 I 4 0 n nsnec n nennc a os@ a nn '106.9 I %53 R 2,135.3 S?8 AS&.n rnA? I I CC3 430 2200 0.01905 O.OIMS 5,294.5 0.0 d34.6 56.6 2, 191.9 534,009.1 717.6 I I 430 420 2200 0.0'IM5 O.0 I&70 4,0&s.d 0.0 4$ 9.7 43.7 2,235.6 53$ ,13$ .4 72d.3 I I 420 4 IO 2200 0.01870 0.01855 4,151.7 0.0- 497.6 C4.4 2,2&0.0 SC2,334.C 735.0 I I 410 COO 2200 0.01855 0.018C2 3,652.$ 0.0 437.8 39.1 2,3I9.0 SC6,026.3 742.5 I I 400 390 2200 0.0 I &42 0.0182$ 3,991.9 0.0 478.5 C2.7 2,361.7 550,060.9 750.7 I I 390 3&0 2200 O.OIS2$ 0.01816 3,470.6 0.0 416.0 37.1 2,398.9 553,568.6 757.6 I I 380 370 2200 0.0 I 8 I 6 0.0'IS04 3,516.8 0.0 421.5 37.6 2,436.5 557,123.0 764.6 I I 370 360 2200 0.01804 O.0I792 3,563.9 0.0 427.2 38.1 2,C74.6 560,725.0 711.6 I I 360 350 2200 0.0 I 792 0.01781 3,309.1 0.0 396.6 35.4 2,510.0 56C,069.5 778.0 I I 350 3CO 2200 0.01781 0.01770 3,350.2 0.0 401.6 35.8 2,545.8 Ser.CSS.S 784.4 I I 3CO 330 2200 0.0 I770 O.0 I 159 3,392.1 0.0 C06.6 36.3 2,5&2.1 570,M3.9 790.8 I I 330 325 2200 0.01759 O.OI75C 1,555.9 0.0 M6.5 16.d 2,59$ .1 572,C56.5 793.1 I I 325 310 268 0.0175C 0.01754 0.0 0.0 0.0 0.0 2,59$ .7 5$ 1,993.2 780.7 I I 310 300 2680.0175C 0.01744 3,138.6 0.0 376.2 33.d 2,632.3 5$ 5,165.4 786.5 I I 300 260 26S 0.011CC O.0I707 11,932.7 0.0 '1,430.3 127.6 2,759.9 591,225.7 807.9 I I 260 235 2680.01707 0.01681 6,668.0 0.0 799.2 71.3 2,831.2 603,965.1 8'I9.6 I I 235 210 268 0.016S7 0.01669 6,137.9 0.0 735.7 65.6 2,896.9 610, I68.6 830.1 I 2'I 0 200 268 0.01669 0. 01662 2,422.9 0.0 '290.4 25.9 2,922.8 I 612,617.C 83C.I I I

I ITOTAL RANT VOL(WE 706$ .3 gallons I

I I

TABLE 2-14 I

PLNIT COOLD(AAI FRDH 557 F TO 200 F; BAHT AT 3.25 utX BORIC ACID; RVT AT 1550 ppa BOROH I

IAVO.SVS. TEN. P2R PRESS SPECIFIC VDLllK SHRINKAGE BAHT VOL 8 RVT VOL 8 8/A ADDED TOTAL B/A TO'IAL SYS. HASS FIHAL COHC I I (F) (peia) (cu.f t./Iba) HASS(lba) 70 f (gal) 50 f (gal) (lba) (lba) ( lba) (ppa boron) I I Ti Tj Vl Vt I -"". "."" -"-- "II 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,d51.2 0.0 I 557 510 2200 0.02157 0.02032 27,319.3 3,250.0 0.0 917.7 917.7 495,6M.2 323.6 I 510 490 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 335 0 1 252 7 506, 195.3 432.7 I 490 460 2200 0.01990 0.01970 4,895.1 SM.1 0.0 164-5 ',417.2 511,255.0 48C.7 I 460 470 2200 0.01970 0.01951 4,746.2 569.5 0.0 159.4 1,57e.7 516, 163.6 534.0 I 470 C&0 2200 O.0I951 0.01933 4,562.5 550.2 0.0 I53.9 1,730.d 520,900.0 550.9 I C60 450 2200 0.01933 0.01916 4,C06.9 529.1 0.0 IC5.0 1,575.7 525,C55.0 625.1 450 440 2200 O.OI916 O.OI900 4,219.8 506.6 0.0 ICT.5 2,020.4 529,5'I6.5 &&6.7 I 440 C27 2200 0.01900 O.OIMI 5,239.9 629.1 0.0 176.0 2,196.4 535,232.5 717.5 I 427 420 2200 O.OIMT 0.01570 2,666.8 0.0 343.d 30.7 2,227.1 538,129.9 723.& I 420 410 2200 O.0I570 0.01555 4,'151.7 0.0 C97.6 44.4 2,271.5 SC2,325.9 732.3 I 410 400 2200 0.01555 0.01542 3,652.5 0.0 437.8 39.1 2,310.6 54&,OI7.8 739.8 I COO 2200 0.015C2 0.0'I 825 3,991.9 0.0 475.5 42.7 2,353.2 550,052.C 745.0 I 390 360 2200 0.0'I62d 0.01516 3,470.6 0.0 416.0 37.1 2,390.4 553,560.1 7S5.0 I 380 370 2200 0.015I& 0.01504 3,516.8 0.0 421.5 37.6 2,425.0 557,114.5 762.0 I 370 360 2200 O.OISOC 0.01792 3,563.9 0.0 427.2 35.1 2,466.1 560,7ld.S 765.9 I 360 350 2200 0.01792 0.01751 3,309.1 0.0 396.d 35.4 2,50'I.S 5&C,O&1.0 775.4 I 350 340 2200 O.OI751 0.01770 3,350.2 0.0 401 6 35.5 2,537.3 567,447.0 751.5 I 3CO 330 2200 O.OI770 0.01759 3,392.1 0.0 406.6 36.3 2,573.6 570,875.4 7M.2 I 330 325 2200 0.01759 0.01754 1,555.9 0.0 166.5 16.6 2,590.2 572,445.0 791.1 I 325 310 2&S 0.0175C 0.017SC 0.0 0.0 0.0 0.0 2,590.2 Sdl,984.7 778.1 I 310 300 266 0.0175C 0.017CC 3,'138.6 0.0 376.2 33.d 2,623.5 555,156.9 753.9 I 300 260 268 0.01744 0.01707 11 932.7 0.0 1,430.3 '127.6 2,751.4 597,217.2 605.5 2&0 235 268 0.01707 0.01657 6,665.0 0.0 '99.2 71.3 2,622.7 603,95&.d dl7.1 I 235 210 26S O.OI687 0.01669 6,137.9 0.0 735.7 es.e 2,555.4 610, 160. I 527.& I 210 200 26S 0.01669 0.0'l662 2,C22.9 0.0 290.4 25.9 2,914.3 d12,&DS.9 531.7 I I

IIOTAL BAHT VOIINE 7659.3 gallons I

I I

I PLANT COOLONQI FROI 557 F To 200 F; RANT AT 3.0 sttX RORIC ACIOT RNT At 1850 ppa QORON I

t (AVG.STS. TEHP. P2R PRESS SPECIFIC VOLIQIE SNRIICAGE RANT VOL Q Rill VOL 8 8/A AOOEO TOTAL 8/A TOTAL SYS. IIASS FINAL CINIC ~ )

(F) (paia) (cu. f t./Ilaa) NASS(IIaa) 70 F (gal) 50 F (gal) (lha) (Iiaa) (IIaa) (ppw boron) )

I Ti Tf Vi VF I

I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 cel,es1.2 0.0 I 557 510 2200 0.021$ l 0.02032 27,319.3 3,280.0 0.0 OC4.9 8CC.9 495,815.4 297.9 )

510 490 2200 0.02032 0.01990 9,972.2 1, 197.3 0.0 308.4 1,153.4 SO&,096.0 398.4 f 490 480 2200 0.01990 O.O197O 4,898.1 5M.1 0.0 151.5 ~

1,30C.8 511,145.6 4C&.3 )

Cbo Clo 2200 0.01970 0.01951 4,746.2 569.8 0.0 I C&.b 1,451.6 516,038.6 491.8 I 470 Cdo 2200 0.01951 O.OI933 4,$ 82.S 550.2 G.o 141.7 1,593.4 520,l62.8 534.9 I 460 4>0 2200 0.01933 O.OI916 4,406.9 529.1 0.0 136.3 1,729.7 525,306.0 5'/5.7 )

450 440 2200 O.0I916 0.01900 4,219.8 506.6 0.0 130.5 1,860.2 529,656.3 etc.o )

440 430 2200 O.OI900 O.OIMS 4,021.1 C82.8 0.0 124.4 1,984.5 533,801.7 650.0 I 430 420 2200 O.0I885 O.olblo 4,085.6 490.S 0.0 126.4 2, 110.9 538,013.7 Mb.o )

420 COS 2200 0.01870 0.018C9 5,971.6 717.0 0.0 18C.l 2,295.6 SCC, 170.0 737.5 (

COS 400 2200 0.01849 0.01842 I,832.8 0.0 219.7 19.6 2,315.2 546,022.C 741.3 I Coo 390 2200 0.01842 0.01828 3,991.9 0.0 478.5 42.7 2,357.9 550,05/.0 7C9.4 I 390 380 2200 0.01828 0.01816 3,470.6 0.0 416.0 37.1 2,395.0 553,564.8 756.4 )

$ 70 22UU U.0 INTO U UIOLVo S,S IO.O U U CCI.S $ /.6 2,4$ 2.6 55/,119.1 763.4 I 370 360 2200 0.0180C O.OI792 3,563.9 0.0 427.2 38.1 2,470.7 560,721.1 770.4 I 350 2200 0.01792 0.01781 3,309.1 0.0 396.6 35 A 2,506.1 564,065.6 776.8 I 350 340 2200 0.0178I O.OI770 3,3$ 0.2 0.0 401.&. 35.8 2,541.9 567,C51.7 783.2 )

340 330 2200 0.0 lllo 0.01759 3,392.1 0.0 406.6 36.3 2,578.2 570,880.0 789.6 I 330 325 2200 0.01759 0.01754 1,555.9 0.0 186.5 16.d 2,594.9 572,452.6 792.5 (

325 310 268 0.0175C O.oll54 0.0 0.0 0.0 0.0 2,594.9 581,989.4 ll9.5 )

310 300 268 0.0175C O.0 1744 3;138.d 0.0 376.2 33.6 2,628 A 585,161.6 785.3 i 300 260 268 O.OI744 0.01707 1'1,932.7 0.0 1,430.3 127.6 2,7S&.1 597,221.9 806.8 /

2M 235 2M 0.01707 O.OIM7 d,bbb.o 0.0 799.2 71.3 2,827.4 603,961.2 818.5 I 235 210 2M 0.01687 0.01669 6,137.9 0.0 735.7 d5.6 2,893.0 d10, 16C.7 829.0 )

210 200 268 O.0I669 0.0 I&62 2,422.9 0.0 290.4 25.9 2,918.9 612,613.5 833.0 I I

(TOTAL RANT VOLUNE 8911.4 gal Iona I

TABLE 2-16 I

PLANl COOLDONI FRDH 557 F 10 200 F; RAH1 Al 2.15 utX RORIC ACID; RMF AI 1550 ppa SORON I I

I li 'f

)AVG.S'FS.

(F) 557 108'.

557 P?R PRESS (pal ~ )

2200 SPECIFIC VOLWE,SNRIINAGE 8AHF VOL 0 (cu.ft./Iba)

Vi 1.00000 Vf 1.00000 HASS(IIaa) 0.0 70 F (gal) 0.0 RM1 .VOL 50 F 8

(gal) 0.0 8/A ADDED 10lAL 8/A

( IIaa) 0.0

( IIaa) 0.0 IDEAL SVS. HASS

( Ilaa) 467,651.2 FINAL CONC. )

(ppa boron) 0.0 f I

)

I I 557 510 2200 0.02157 0.02032 27,319.3 3,250.0 0.0 772.5 772.S 495,143.0 272.4 )

I I

I 510 490 CSO C90 460 410 2200 2200 2200 0.02032 0.01990 0.01970 0.01990 0.01970 0.01951 9,972.2 4,595.1 4,746.2 1,197.3 SM. I 569.5 0.0 0.0 0.0 252.0 13$ .5 13C.2

', 1,054.5 I93.0 1,327.2 505,991.1 5>>.033.7 515,9IC.1 364.4 )

405.1 449.8 I

=

I 470 460 2200 0.0195'I 0.01933 4,552.5 550.2 0.0 129.6 1,456.8 520,626.2 459.2 I I 460 450 2200 0.01933 0.01916 4,C06.9 529.1 0.0 124.6 1,551.4 525,157.S 526.5 I I CSO 4CO 2200 0.01916 0.01900 4,219.5 50b.d O.U 119.3 1,700.7 529,496.S 561.6 (

I 440 430 2200 O.0I900 '.01565 4,021.1 CS2.5 0.0 1'I3.7 1,814.4 533,631.6 594.5 I 430 420 2200 0.01855 0.01570 4,055.d 490.5 0.0 >>5.5 1,930.0 537,832.7 627.4 I I 420 CIO 2200 0.01870 0.01555 4,151.7 495.5 0.0 >>7.4 2,0C7.4 SC2, 10 I.S 660.3 )

I 410 400 2200 0.01555 0.015C2 3,652.5 438.d 0.0 103.3 2, 150.6 SC5,557.9 bm.b )

I 400 390 2200 O.OISC2 0.0152S 3,991.9 479.3 0.0 >>2.9 2,263.5 549,962.7 7I9.6 I I 390 375 2200 O.OIS28 0.01510 5,223.2 627.1 0.0 ICl.l 2,4>>.2 555,333.5 1S9.1 )

I 315 310 2200 0.01810 0.01604 1,76C.2 0.0 21'I.S 15.9 2,430.1 ssl, >>6.6 762.6 (

I 370 360 2200 O.OIM4 0.0'll92 3,563.9 0.0 CD.2 3S. I 2,468.2 560,715.6 769.6 )

I 360 350 2200 0.01792 0.01751 3,309.1 0.0 396.6 35.4 2,503.6 564,063.1 716.0 )

I 350 340 2200 0.01751 0.01710 3,350.2 0.0 401.6 35.5 2,539.4 567,449.1 152.4 )

I 3CO 330 2200 0.01770 0.01159 3,392.1 0.0 406.6 36.3 2,51S.7 570,877.5 75S.S )

I 330 325 2200 O.0I759 0.01154 1,555.9 0.0 166.5 16.6 2,592.3 572,450.1 791.7 (

I 325 310 26S 0.01754 0.0115C 0.0 0.0 0.0 0.0 2,592.3 SS1,986.S 715.5 I I 310 300 26S 0.0175C 0.01744 3,138.d 0.0 376.2 33.6 2,625.9 555,159.0 764.6 )

I 300 260 268 0.01744 O.OI107 >>,932.7 0.0 1,430.3 127.6 2,753.5 597,219.4 $ 06. I I 260 235 26S 0.01707 0.01661 6,665.0 0.0 '99.2 71.3 2,82C.9 603,95S.7 517.7 I I 235 210 265 O.OI687 0.01669 6,137.9 0.0 735.7 65.6 2,590.5 610, 162. 2 825.2 I I 210 200 26S 0. 01669 0.01662 2,422.9 0.0 290.4 25.9 2,91d.4 612,6>>.0 832.3 )

I I

[ IOIAL SAHI VOI.UHE 10237.9 gallons I

I I

TABLE 2-17 I

PLART COOLOQAI FROI 557 F 'TO 200 F; RA)IT Al 2.50 std BORIC ACID; RVT AT 1850 pps BORON I

I (AVG.STS. T~. PZR PRESS SPECIFIC VOLIBIE SRRIINAGE BAIIT VOL 0 RVl VOL Q g/A ADOEO TOTAL B/A loTAL SYS. IIASS FIINL COSC I I (pal ~ ) (cu.f t./Ibe) IIASS(lbs) 70 F (gal) 50 F (gal) (Ibs) (lbe) ( Iba) (pps boron) )

Ti Tf Vi Vf 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 )

557 510 2200 0.02157 0.02032 27,319.3 3,280.0 0.0 700.5 700.5 495,671.0 2C7.1 I 510 490 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 255.7 956.2 505,895.8 330.4 )

490 480 2200 0.01990 0.01970 C,895.1 588.'I 0.0 125.6 ~ 1,0SI.S 510,922.5 370.2 )

Cbo 470 2200 0.01970 0.01951 C,746.2 569.8 0.0 121.7 1,203.5 515,790.4 407.9 I 470 460 2200 0.01951 0.01933 C,M2.5 550.2 0.0 117.5 1,321.0 520,C90.4 443.7 )

) Cbo 450 2200 0.01933 0.019 I& 4,406.9 529.1 0.0 113.0 1,C3C.O 525,010.3 477.5 I I 450 CCO 2200 0.01916 0.01900 4,219.5 506.6 0.0 108.2 1,542. 1 529,338.3 509.4 )

4CO 430 2200 0.01900 0.01555 4,021 ~ 1 C$ 2.8 0.0 103.1 1,645.3 533,C&2.5 539.2 )

430 420 2200 0.01555 0.01570 4,085.d 490.5 0.0 104.8 1,750.0 537,652.5 569.1 I 420 4 IO 2200 O.0I$ 70 O.OISSS 4, 151.7 C98.5 0.0 106.5 1,856.5 5C1,910.9 59$ .9 I 410 Coo 2200 0.01855 0.018C2 3,652.5 438.6 0.0 93.7 1,950.1 545,657.4 62C.S )

Coo 390 2200 O.OIS42 0.01828 3,991.9 479.3 0.0 102.4 2,052.5 5C9,751.6 652.7 I 390 360 2200 O.0I$ 25 0.01516 3,470.6 416.7 0.0 89.0 2,141.5 553,311.2 676.7 )

380 370 2200 o.olsle 0.0150C 3,516.8 422.2 - 0.0 90.2 2,231.6 556,91$ .2 7oo.e ~

370 360 2200 0.01504 0.01792 3,563.9 427.9 0.0 91.4 2,323.0 560,573.4 724.5 )

360 350 2200 0.01792 0.01781 3,309.1 397.3 0.0 S4.$ 2,C07.9 5&3,967.4 746.5 I 350 340 2200 0.01781 0.01770 3,350.2 402.2 0.0 85.9 2,C93.8 567,403.5 7&5.4 3CO 330 2200 0.01770 O.ol7 59 3,392.1 407.3 0.0 87.0 2,5$ 0.7 570,8S2.6 790.4 )

330 325 2200 0.01759 0.01754 1,555.9 0.0 186.5 16.6 2,597.4 572,455.1 793.3 )

325 310 26S 0.01754 0.01754 0.0 0.0 0.0 0.0 2,597.C 5$ 1,991.9 780.3 )

310 300 265 0.01754 O.UI /44 S, Iab.e 0.0 376.2 33.d 2,630.9 5S5,16C.T 786.1 300 260 26S 0.0174C 0.01707 11,932.7 0.0 1,C30.3 127.6 2,758.d 597,224.4 807.6 )

260 235 26S 0.01707 0.01687 6,66$ .0 0.0 799.2 71.3 2,829.9 603,963.7 519.2 I 235 210 268 0.016S7 0.01669 6, 137.9 0.0 735.7 &s.d 2,$ 95.5 610,167.2 829.7 ]

210 200 268 0.01669 O.0I662 2,422.9 0.0 290.4 25.9 2,921.4 612,616.0 S33.7 )

I (IOTAL BAIIT VOLUHE 12084.4 gallons I

I I

TABLE 2-18 J

J

~ PLANT COOLMQI FROI 557 F 10 200 F; SANT AT 3.5 utX RORIC ACID; RUT AT 2000 ppa RORON J

JAVG.SYS. TEIN'. P?R PRESS SPECIFIC VOLIRIE SNRINKAGE RANT VOL 8 RMT VOL 8 8/A ADDED 10TAL 8/A TOTAL STS. NASS FINAL CONC. J J (F) (poja) (cu.fc./Iba) NASS(lba) 70 F (gal) 50 F (gal) (Iba) (Iba) (lha) (ppa boron) J Ti Tf Vi Vf J ----"" J J

J 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 J J 557 510 2200 0.02157 0.02032 27,3'I9.3 3,280.0 0.0 990.9 990.9 C95,961.3 3C9.3 J 5'IO C90 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 361.7 J 1,352.5 506,295.2 467.1 J 490 480 2200 0.01990 0.01970 4,898.1 SM.1 0.0 ill.l 1,530.2 511,370.9 523.2 J

J J

480 C70 2200 0.01970 0.01951 4,746.2 569.8 0.0 172.1 1,702.3 516,289.3 576.5 J J C70 C60 2200 0.01951 0.01933 4,582.5 550.2 0.0 166.2 1,668.5 521,038.0 627.0 J J

C60 CSO 2200 0.01933 0.01916 4,406.9 529.1 0.0 159.8 2,028.4 525,60C.8 674.7 J 450 CCO 2200 0.01916 0.01900 4,219.8 0.0 505.8 48.8 2,077.2 529,873.3 J 665.4 J J 440 430 2200 0.01900 O.OIMS 4,021.1 0.0 482.0 46.5 2,123.7 533,940.9 695.4 J J

430 C20 2200 O.OIM5 0.01870 4,065.d 0.0 489.7 47.3 2, 171.0 538,073.8 705.C J 420 410 2200 0.01870 0.01855 4,151.7 0.0 497.6 48.0 2,219.'I 542,273.5 J 715.4 J 410 COO 2200 0.01855 0.01842 3,652.8 0.0 437.8 42.3 2,2d1.3 545,968.6 J 724.1 J 400 390 2200 0.016C2 O.0I828 3,991.9 0.0 478.5 46.2 2,307.5 550,006.7 J 733.5 J J

390 360 2200 O.0I828 0.018I6 3,470.6 0.0 416.0 40.2 2,3Cl. 7 553,517.4 741.5 J 380 370 2200 0.018'I6 O.OIMC 3,516.8 0.0 421.5 40.7 2,3M.4 557,074.9 J

7C9.6 J 370 360 2200 0.01804 0.01792 3,563.9 0.0 427.2 41 ~ 2 2,429.d 560,660.0 J 757.6 J

.J 360 350 2200 0.01792 0.01761 3,309.1 0.0 396.6 38.3 2,'467.9 56C,027.4 765.0 J

'50 340 2200 0.01781 0.01770 3,350.2 0.0 401.6 38.8 2,506.7 567,4ld.C 772.4 J

J 3CO 330 2200 0.01770 0.01759 3,392.1 0.0 C06.6 39.3 2,5C5.9 570,8Cl.l J

779.7 J 330 325 2200 0.01759 0.0175C 1,555.9 0.0 186.5 18.0 2,563.9 572,421.7 J

783.1 J

~

J 325 310 266 0.0175C 0.01754 0.0 0.0 0.0 0.0 2,563.9 581,958.4 770.3 J 310 300 268 0.01754 0.01744 3,138.6 0.0 376.2 36.3 2,600.2 585,133.4 J

776.9 J 300 260 266 0.01744 0.01707 11,932.7 0.0 1,430.3 138.1 2,738.3 597,204.1 J

801.7 J J

260 235 268 0.01707 0.0168l 6,668.0 0.0 799.2 77.2 2,815,5 603,9C9.3 815.0 J 235 2IO 268 0.01687 0.0'1669 6,137.9 0.0 735.7 71.0 2,M6.5 610, 158.2 J

827.1 J 2 IO 200 268 0.01669 0.01662 2,422.9 0.0 290.4 28.0 2,914.5 612,609.1 J

831.8 J J

J JTOTAL RAHT VOLLNE 6714.5 gallons J

J J

TABLE 2-19 I

PLANT CDOLDOQI fRQI 557 f IO 200 f; SNIT AT 3.25 utX R(NIC ACID; Rill AT 2000 pfss QORDN I I

)AVQ.STS ~ TEIN'. PZR PRESS SPECIFIC VOLOK SNRINKACE RABAT V(N. 0 RNT VDL Q 5/A ADDED TOTAL 8/A TOTAL STS. HASS FINAL CONC-)

I (F) (ps la) (cu. I t./Ibs) MASS(lbs) 70 F (gsi) 50 f (gat) (lbs) (lbs) ( lba) (pps boron) )

I Tl Tf Vl Vf I I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 )

557 510 2200 0.02157 0.02032 27,319.3 3,280.0 0.0 917.7 917.7 C95,665.2 323.6 I 510 490 2200 0.02032 0.01990 9,972.$ '1,197.3 0.0 335.0 1,252.7 506, 195.3 432.7 )

490 460 2200 0.01990 0.01970 4,595.1 565.1 0.0 164.5 1,417.2 511,2M.O 484.7 (

C60 470 2200 0.01970 0.01951 4,746.2 569.5 0.0 159.4 1,576.7 5ld,163.6 53C.O )

C70 460 2200 0.01951 0.01933 4,552.5 550.2 0.0 153.9 1,730.6 520,900.0 560.9 )

460 CSO 2200 0.01933 0.01916 4,C06.9 529.1 0.0 148.0 1,676.7 525,455.0 625.1 )

450 440 2200 0.01916 0.01900 4,219.5 506.6 0.0 IC1.8 2,020.4 529,816.5 666.7 )

440 432 2200 0.01900 O.0IM5 3,211.8, 355.6 0.0 107.9 2,128.3 533,136.2 697.9 I 432 420 2200 O.OIM6 0.01570 4,694.9 0.0 566.7 Se.d 2,18C.9 538,057.7 709.9 )

420 410 2200 0.01670 O.0I555 4,151.7 0.0 497.6 C5.0 2,233.0 542,267.4 719.9 )

410 400 2200 O.0I555 O.OI$ 42 3,652.5 0.0 437.$ 42.3 2,275.2 SC5,982.5 728.6 )

400 390 2200 0.018C2 0.01528 3,991.9 0.0 478.5 46.2 2,321A 550,020.6 737.9 )

390 380 2200 0.01828 0.01516 3,470.6 0.0 416.0 40.2 2,361.6 553,531.4 745.9 I 360 370 2200 0.015I& 0.01804 3,516.5 0.0 421.5 40.7 2,402.3 557,088.8 753.9 (

370 360 2200 O.OIM4 0.01792 3,563.9 0.0 427.2 4'1.2 2,4C3.5 560,693.9 761.9 I 360 350 2200 0.01792 0.01781 3,309. I 0.0 396.& 38.3 2,451.6 56C,OC1.3 769.3 I

'350 340 2200 0.01761 0.01770 3,350.2 0.0 40'I.d 36.8 2,520.6 567,430.3 lie.e t 3CO 330 2200 0.01770 0.01759 3,392.1 0.0 C06.6 39.3 2,559.5 570,661.7 784.0 )

330 325 2200 0.01759 0.01754 1,555.9 0.0 186.5 lb.0 2,57l.b Sl2,435.6 787.3 I 325 310 268 0.01754 O.0I754 0.0 0.0 0.0 0.0 2,5ll.b 551,972.3 774.4 I 310 300 265 0.0llSC 0.0174C 3,13b.d 0.0 376.2 36.3 2,614.2 585, 147.3 761.1 I 300 260 2M O.0 I74C 0.01707 II,932.7 0.0 . 1,430.3 138.1 2,752.2 597,215.1 505.7 )

I 260 235 268 0.01 /07 0.01657 6,665.0 0.0 799.2 77.2 2,629.4 603,963.2 819.0 I I 235 210 2M O.OIMl 0.01669 6, 137.9 0.0 735.7 7'I.O 2,900.4 610, 172.1 631.1 I I 210 200 268 O.0I669 0.01662 2,422.9 0.0 290A 28.0 2,926.5 612,623.0 $ 35.7 I I I

)TOTAL Rsut van Iscf 7Nlh.b osl lons I

I I

TABLE 2-70 I

PLANT COOL(%HI FRCFI 557 F TO 200 F; SANT AT 3.0 utX SORIC ACID; RNT AT 2000 ppa ROTI I (AVG.STS. TON'. PZR PRESS SPECIFIC VOLINIE SNRINKACE RANT VOL 0 RUT VOL Q 8/A ADDED TOTAL 8/A TOTAL STS. NASS FINAL CONC. f I (F) (paia) (cu.f t./Iba) NASS(lba) 70 F (gal) 50 F (gal) (lba) (lba) (lba) (ppaa boron) ]

Ti TF Vi Vf I I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I 5S7 %10 7700 0.07 IS7 0.07DT7 77 3 7IVI.D 0.0 $ 4C.9 SCC.9 C95,815.C 297.9 I

'319.'%,972.2 510 490 2200 0.02032 0.01990 1,197.3 0.0 30$ A I ~ 153A 506,096.0 39$ .4 I C90 480 2200 0.01990 0.01970 4,$ 98.1 588.1 0.0 151.5 1,30C.S 511, 145.6 446.3 )

4$ 0 470 2200 0.0'l970 0.01951 4,746.2 569.$ 0.0 1C6.8 1,451.6 516,038.6 491.8 I 470 460 2200 0.01951 0.01933 C,M2.5 550.2 0.0 141.7 1,593.4 520,762.8 534.9 (

460 450 2200 0.01933 0.01916 4,406.9 529.1 0.0 136.3 1,729.7 525,306.0 575.7 )

450 4CO 2200 0.01916 0.01900 ~

4,219.8 506.6 0.0 130.5 1,860.2 529,656.3 614.0 I 440 C30 2200 0.01900 0.01885 4,021.1 C82.$ 0.0 124.4 1,984.5 533,801.7 650.0 I 420 2200 0.01885 0.01870 C,OS5.6 490.5 0.0 126.C 2,110.9 53$ ,013.7 6S6.0 )

4 I2 2200 0.01870 0.01858 3,316.0 398.1 0.0 102.6 2,213.4 541,432.2 714.7 I I C12 400 2200 0.01858 0.01$ C2 4,488.5 0.0 53$ .0 51.9 2,265A 545,972.6 725.4 )

I 400 390 2200 0.0'Ib(2 0.0182$ 3,991.9 0.0 47$ .5 46.2 2,31'I.e 550,0I0.7 734.8 )

I 390 380 2200 0.01828 O.0I816 3,4l0.6 0.0 416.0 40.2 2,351.7 553,521.5 742.8 I 3$ 0 370 2200 0. 01816 D.OIS04 3,516.8 0.0 421.5 40.7 2,392.4 557,079.0 750.$ (

370 360 2200 0.0180C 0.01792 3,563.9 0.0 427.2 C1.2 2,C33.7 560,6S4 ~ 1 758.9 )

'3M 350 2200 0.01792 0.01781 3,309.1 0.0 396.6 3$ .3 2,C72.0 56C,031.5 766.2 )

350 3CO 2200 0.01lSI 0.01770 3,350.2 0.0 C01.6 38.d 2,510.7 567,420 A 773.6 )

340 330 2200 O.0I770 0.01759 3,392.1 0.0 C06.6 39.3 2,550.0 570,85 I.S 7$ I.O I 330 325 2200 0.01759 0.0175C 1,555.9 0.0 186.5 18.0 2,568.0 572,C25.7 784.3 (

325 310 2M O.OI754 0.01754 0.0 0.0 0.0 0.0 2,568.0 581,962.5 771.5 )

I 310 300 268 0.0175C 0.01744 3;13$ .6 0.0 376.2 36.3 2,604.3 5$ 5,137.4 77$ .1 I I 300 260 2M 0.01744 0.0'I 707 11,932.7 0.0 ~ I,C30.3 13$ .1 2,742.4 597,2M.2 802.$ )

I 260 235 2M 0.01707 0.016Sl 6,66$ .0 0.0 799.2 77.2 2,819.5 603,953.4 816.2 I I 235 210 26$ 0.01687 0.01669 6,137.9 0.0 735.7 71.0 2,d90.6 610,162.3 82S.3 )

I 210 200 268 0.01669 0.01662 2,422.9 0.0 290.4 2$ .0 2,91$ .6 el2,613.2 832.9 J I I

]TOTAL RANT VOLUNE $ 592.6 gallons I

I I

TABLE 2-2l I

PLANT COOLDORI FROH 557 F TO 200 F; BAHT AT 2.75 VIX BORIC ACID; RVT AT 2000 gm BORON I

I (AVC.SVS ~ TON . PZR PRESS SPECIFIC VOLIRIE SNRINKACE BAHT VOL Q RVT VOL 6 6/A ADDED TOTAL 6/A TOTAL SYS. HASS FINAL CONC. (

I (F) (psis) (cu.fc./Iba) HASS(lba) 70 F (Bsl) 50 F (Bsl) ( lba) ( Ibs) (Iba) (ppa boron) (

Tl Tt VI Vf I

557 557

-" ""."."""""".""-- -I I 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 ce1,es1.2 0.0 I 557 510 2200 0.02157 0.02032 21,319.3 3,280.0 0.0 772.5 772.5 495,743.0 272.4 (

510 490 2200 0.02032 0.01990 9,912.2 1,197.3 0.0 282.0 1,054.5 505,997.1 364.4 (

490 460 2200 0.01990 0.01910 4,698.1 SM.1 0.0 138.5 1,193.0 511,033.7 40b. 1 CSO 470 2200 0.01970 0.01951 4,746.2 569.8 0.0 13C.2 1,327.2 515,914.1 449.8 I C70 C60 2200 0.01951 0.01933 4,582.5 550.2 0.0 129.6 1,456.8 520,62d.2 489.2 I 460 450 2200 0.01933 0.01916 4,C06.9 529.1 0.0 124.6 1,581.4 525, 157.8 526.5 (

450 4CO 2200 0.01916 O.0I900 4,219.8 506.d 0.0 119.3 1,700.7 529,496.S 561.6 (

440 C30 2200 0.01900 O.OIMS 4,0Zl. 1 482.8 0.0 113.7 1,814.4 533,631.6 594.5 I 430 420 2200 O.OIMS O.0I870 4,065.6 490.5 0.0 115.5 1,930.0 531,832.7 627.4 (

420 410 2200 0.01870 0. 01655 4,151.7 498.5 0.0 117.C 2,047.C SC2,101.S 660.3 (

410 COO 2200 0.01855 0.01642 3,652.8 438.6 0.0 103.3 2,150.6 545,857.9 6M.S (

400 390 2200 0.01842 0.01828 3,991.9 479.3 0.0 112.9 2,263.5 549,962.7 719.6 (

390 360 2200 0.01828 0.0'Ibid 3,470.6 416.7 0.0 98.1 2,361.7 553,531.C 745.9 I 380 370 2200 0.01816 0.01604 3,516.8 0.0 421.5 40.7 2,402.4 557,08S.9 753.9 (

370 360 2200 0.0160C 0.01792 3,563.9 0.0 427.2 41.2 2,443.6 560,69C.O 7e2.0 (

360 350 2200 0.01792 0.017SI 3,309.1 0.0 396.6 36.3 2, C$ 1.9 564,041.4 769.3 I 350 340 2200 0.01781 0.01710 3,350.2 0.0 401.6 38.8 2,520.7 567,430.4 77e.7 (

340 330 2200 0.01770 0.01159 3,392.1 0.0 Ccb.d 39.3 2,559.9 570,861 ~ 7 78C.O (

330 325 2200 0.01759 0.01754 1,555.9 0.0 166.5 lb.0 2,577.9 572,435.7 781.3 I 325 310 266 0.01754 0.01754 0.0 0.0 0.0 0.0 2,577.9 SS1,972.4 774.C (

310 300 266 0.0175C 0.01744 3,138.6 0.0 376.2 36.3 2,61C.2 585,1C7.4 781.1 I 300 260 266 0.0174 C 0.01101 11,932.7 0.0 1,430.3 13S.1 2,752.3 597. 218. 1 605.7 (

260 235 268 0.01707 0. 0 1681 6,666.0 0.0 199.2 77.2 2,829.5 603,963.3 819. I I 235 210 268 0.016S7 0.01669 6,137.9 0.0 735.7 71.0 2,900.5 610,'I72.2 831.1 I 210 200 266 0.01669 0.01662 2,422.9 0.0 290A 2S.O 2,928.5 dl2,623.1 835.S (

I (TOTAL BAHT VOIUHE 1002/.4 gsllons I

I I

TABLE 2-22 I

I' PLANt COOLDOQI FROI 557 F TO 200 f; BAHt AT 2.50 NIX BORIC ACID; RVT At 2000 ppa BORON I

l I

)AVG.STS. TEHP. PZR PRESS SPECIFIC VDLINE SNRINXAGE BAHT VOL 0 RNT VOL 0 9/A ADOfD TOTAL 9/A TOtAL STS. HASS FIIQL CONC. (

I (F) (pal ~ ) (cu.f C./Iba) HASS(lba) 70 f (Bal) 50 f (Bal) (Iba) (Iba) ( lba) (ppa boron) f TI tf Vi Vf I I

I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 Cer.esl.2 0.0 I I 557 510 2200 0.02157 0.02032 27,319.3 3,250.0 0.0 700.5 700.5 495,671.0 247.1 I I 510 490 2200 0.02032 0.01990 9,972.2 I ~ 197.3 0.0 255.7 956.2 505,895.8 330 4 I 490 450 2200 0.01990 0.01970 4,895.1 SM.1 0.0 125.6 ',081.8 510,922.5 370.2 )

I CSO C70 2200 0.01970 0.01951 4,746.2 569.8 0.0 121.7 1,203.5 515,790.4 407.9 I I 470 C60 2200 0.01951 0.01933 4,582.5 550.2 0.0 117.5 1,32'I.O 520,490.C C43.7 I I C60 450 2200 0.01933 0.01916 4,406.9 529.1 0.0 113.0 1,43C.Q 525,010.3 Clr.s )

I CSO 4CO 2200 0.01916 0.01900 4,219.8 506.6 0.0 108.2 I,SC2.1 529,338.3 509.C )

I 4CO 430 2200 0.01900 O.OIMS 4.021.1 482.8 0.0 103.1 1,6C5.3 533,462.5 539.2 )

I 430 420 2200 O.OIMS 0.01870 4,055.d C90.5 0.0 104.8 1,750.0 537,652.5 569.1 I I 420 410 2200 0.01870 0.01555 4,151.7 C95.5 0.0 106.5 1,556.5 541,910.9 595.9 I I 410 400 2200 0.01855 O.OISC2 3,652.5 438.6 0.0 93.7 1,950. I 545,657.C 624.8 I I 400 390 2200 0.01842 O.OM2d 3,991.9 479.3 0.0 102A 2,052.5 sc9,7sl.e es2.r (

I 390 350 2200 0.01828 0.01516 3,470.6 C16.7 0.0 59.0 2,1C1.5 553,311.2 ere.r ~

I 380 370 2200 0.0'I816 0.0150C 3,516.5 C22.2 0.0 90.2 2,231.6 556,9ld.2 700.6 )

I 370 360 2200 0.01504 0.01792 3,5d3.9 C27.9 0.0 91.4 2,323.0 560,573.4 724.5 I I 350 2200 0.01792 0.01751 3,309.1 397.3 0.0 SC.S 2,407.9 563,967.4 7C6.5 I I 350 336 2200 0.01751 0.01766 4,702.0 56C.S 0.0 120.d 2,528.4 SM,759.9 ill.2 )

I 336 330 2200 0.01766 0.01759 2,0C0.3 0.0 244.6 23.d 2,552.0 570,853.5 78'1.6 I I 330 325 2200 0.01759 0.01754 1,555.9 0.0 Me.s lb.0 2,570.0 572,C27.8 785.0 I I 325 310 26S 0.01754 0.0175C 0.0 0.0 0.0 0.0 2,570.0 5SI,96C.S 772.1 I I 310 300 2M 0.0175C D.0I744 3,138.6 0.0 376.2 36.3 2,606.C 555,139.5 rrs.b ~

I 300 260 26S 0. 01744 0.01707 11,932.7 0.0 1,430.3 138.1 2,744.4 597,210.2 503.4 I 260 235 2M 0.01707 0.016Sl e,eM.D 0.0 799.2 77.2 2,S21.6 603,955.C SI6.8 I I 235 210 2M 0.01657 O.OI669 6,137.9 0.0 735.7 71.0 2,892.6 610, 164. 3 82S.S )

I 210 200 265 0.01669 0.01662 2,422.9 0.0 290.C 28.0 2,920.6 6I2,615.2 833.5 I I I ITDTAL Butt WN.IBIE 11S39.4 Bal Iona I

I I

TABLE 2-23 I

PLANl COOLDOAI FROI 557 f IO 200 Fl RANT Al 3.5 utX BORIC ACIDI RNT Al 2150 ppa BORON I I

(AVG.STS. TON . P?R PRESS SPECI fIC VOLIRIE SNRINKAOE RANT VDL 8 RMT VOL 0 8/A ADDED TOlAL 8/A TDIAL STS. HASS flNAL CONC. )

I (F) (Pcia) (cu.f t./Ibs) HASS(Itaa) 70 F (Bal) 50 f (Bal) (IIaa) (Ilaa) (Itaa) (ppe boron) )

li lt Vi Vf I """""--- -" """""" -"-"- """ """"-"" I I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 461,651.2 0.0 I 557 510 2200 0.02157 O.OC052 21,319.5 3,2$ 0.0 U.O 990.9 990.9 495,9&1.3 349.3 )

510 490 2200 0.02032 0.01990 9,912.2 1,191.3 0.0 361.7 1,352.5 506,295.2 467.1 )

490 480 2200 0.01990 0.01910 4,898.1 5$ 8.1 0.0 177.7 1,530.2 511,310.9 523.2 )

. 480 C70 2200 0.01910 0.01951 4,746.2 569.8 0.0 172.1 1 '02.3 516,269.3 576.5 )

C70 455 2200 0.01951 0.01925 6,776.2 813.d 0.0 245.8 1,948.1 523,311.3 650.8 )

455 450 2200 0.01925 0.01916 2,213.2 0.0 265.3 27.d 1,975.7 525,552.1 657.2 I 450 440 2200 0.01916 0.01900 4,219.8 0.0 505.8 52 6 2,02$ .3 529,824.4 669.3 )

440 430 2200 0.01900 O.ON85 4,02'l.1 0.0 482.0 50.1 2,018.4 533,695.d &M.& i 430 420 2200 O.ON65 0.01870 4,0$ 5.6 0.0 489.7 50.9 2,129.3 538,032.1 691.9 I 420 410 2200 0.01870 0.01655 4, '151.7 0.0 497.6 51.7 2,181.0 SC2,235 5 703.2 )

410 COO 2200 0.01655 0.0lbC2 3,652.8 0.0 437.8 45.5 2,226.6 545,933.8 713.1 I 390 2200 0.01842 0.01828 3,991.9 0.0 478.5 49.7 2,216.3 SC9,915.5 723.6 I I 390 360 2200 0.01828 0.01816 3,470.6 0.0 416.0 43.3 2,319.6 553,489.3 732.1 (

I 360 370 2200 0.01816 0.0180C 3,516.8 0.0 421.5 43.8 2,363.4 557,049.9 741.8 I 370 360 2200 0.01604 0.01792 3,563.9 0.0 427.2 44.4 2,407.8 560,d58.2

'II 360 350 2200 0.0 I792 0.01781 3,309.1 0.0 396.6 41.2 2,C49.0 56C,008.5 750.8 )

759.2 )

I 350 3CO 2200 0. 01781 0.01770 3,350.2 0.0 401 6 41.8 2,490.8 567,400.5 767.5 I I 3CO 330 2200 0.01770 0.01759 3,392.1 0.0 406.6 C2.3 2,533.1 570,834.9 775.8 )

330 325 2200 0.01759 0.0175C 1,555.9 0.0 16&.5 19.4 2,552.5 572,C10.2 779.6 )

325 310 26$ 0.0175C 0.0175C 0.0 0.0 0.0 0.0 2,552.5 581,947.0 766.8 )

310 300 26b 0.01754 0.01744 3,138.6 0.0 37&.2 39.1 2,591.6 585,124.7 714.4 I 300 260 268 0. 01744 0.01707 11,932.7 0.0 1,C30.3 1C8.7 2,740.3 591,206.1 602.2 )

260 235 2M 0.01707 0. OIM1 6,6M.O 0.0 799.2 83.1 2,823.C 603,957.2 bl7.3 I 235 210 268 0.01661 O.bi&69 6,137.9 0.0 735.7 76.5 2,899.9 610, 171.6 830.9 I 210 200 2M 0. 01669 0.01662 2,422.9 0.0 290.4 30.2 2,930.0 612,624.d 836.2 )

I I

)TOTAL BAHI VDLUHE &CC8.8 Bal iona I

I I

TABLE 2-24 I

PLANT COOLDOQI fRQI 557 f TO 200 f; BAHT AT 3.25 vtX BORIC ACID; RMT AT 2'ISO ppa BORON I I

(AVG.STS. TEIN'. PZR PRESS SPECIFIC VOLWE SHRINKAGE BAHT VOL 0 RUT VOL 0 8/A ADDED TOTAL 8/A 'IOTAL SYS. HASS F INAL C(NC. )

(f) (psi ~ ) (cu.ft./Ibs) HASS(Ibs) 70 f (gal) 50 F (gal) (Ihs) (Iba) (Iba) (ppa hornist))

I Ti Tf Vi Vf I I

~ ~ ~ ~ i ~ ~ ~ ~

557 557 2200 1.00000 1. 00000 0.0 0.0 0.0 0.0 0.0 Cel,e51.2 0.0 )

557 510 2200 0.02157 0.02032 27,319.3 3,260.0 0.0 917.7 917.7 495,M8.2 323.6 I 510 490 2200 0.02032 0.01990 9,9g.2 1 ~ 197.3 0.0 335.0 1,252.7 506,195.3 432.7 I C90 CM 2200 0.01990 O.OI910 C,896.1 SM.1 0.0 164.5 ',417.2 511,258.0 464.7 ( =

C60 410 2200 0.01970 0.01951 C,746.2 569.8 0.0 '159.C 1,516.7 Sld,163.6 534.0 )

470 460 2200 0.01951 0.01933 4,582.5 550.2 0.0 153.9 1,730.6 520,900.0 580.9 )

C60 CSO 2200 0.01933 0.01916 4,C06.9 529.1 0.0 148.0 'I,bib. 7 525,CSS.O 625.1 C50 4C1 2200 0.01916 0.01902 3,79C.6 455.6 0.0 127.5 2,006.1 529,311.1 662.5 )

441 430 2200 0.01902 O.DIMS 4,4C6.3 0.0 532.9 55 4 2,061.5 533,618.7 675.1 C30 C20 2200 0.01685 0.01810 4,085.d 0.0 489.7 50.9 2, I I2.4 536,015.2 686.5 )

420 C10 2200 O.0I810 0.01855 4,151.7 0.0 491.6 51.7 2,16C.2 542,218.6 697.8 )

CIO 400 2200 0.01855 0.01842 3,652.8 0.0 437.8 45.S 2,209.1 545,917.0 707.7 I COO 390 2200 0.018C2 0.01628 3,991.9 0.0 478.5 49.7 2,259.5 549,958.6 /lb.3 I 390 380 2200 0.01828 0.01816 3,470.6 0.0 416.0 43.3 2,302.7 553,472.5 127.4 )

380 370 2200 0.01816 O.0I804 3,516.8 0.0 421.5 43.8 2,346.5 557,033.1 736.5 )

sm 2200 0.01804 0.01192 3.563.9 0.0 427.2 44.4 2,390.9 560,6C1.4 745.6 I 360 350 2200 0.01192 O.OI781 3,309.1 0.0 396.6 C1.2 2,432.2 563,991.7 754.0 )

350 3CO 2200 0.01781 0.01770 3,350.2 0.0 401.6 41.d 2,473.9 567,383.6 762.3 )

340 330 2200 0.01710 0.01159 3,392.1 0.0 C06.6 42.3 2,516.2 570,818.0 710.7 I 330 325 2200 0.01159 0.0175C 1,555.9 0.0 166.5 19.C 2,535.6 572,393.3 714.5 I 325 310 268 0.01754 0.0'l7S4 0.0 0.0 0.0 0.0 2,535.6 58'1,930.1 761.8 I 3'IO 300 268 0.017SC 0.01744 3,138.6 0.0 376.2 39.1 2,574.7 585,101.8 769.3 )

300 260 268 0.0174C 0.01707 11,932.7 0.0 1,C30.3 1Cb.l 2,723.4 597,169.2 797.3 )

260 235 266 0.01707 0.01687 6,668.0 0.0 799.2 63.'I 2,606.5 603,940.4 812.5 I 235 2IO 268 0.01667 0.01669 d,137.9 0.0 735.7 76.5 2,883.0 610,154.7 826.1 )

210 200 268 0.01669 0.0!662 2,C22.9 0.0 290.4 30.2 2,913.2 612,601.8 831.C I I

[TOTAL BAHT VOLINE 7110.1 gallons I I I

TABLE 2-25 I

PLANT COOLDORI FROI 557 F TO 200 F; BAHT AT 3.0 Nt'I BORIC ACID; RIIT AT 2150 ppo BORON I I

(AVG.STS TEIN'. PZR PRESS SPECIFIC VOLIRIE SNRIIN'AGE RANT VOL 8 RIIT VOL Q 8/A ADDED TOTAL 8/A TOTAL STS. HASS FINAL CONC.)

(F) (pole) (cu.f t./lba) HASS(lba) 70 F (Ool) 50 F (Ool) (lba) (lba) ( lba) (ppaa boron) )

I Tl Tf VI Vf I I

I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 4&7.&S1.2 0.0 I I 557 510 2200 0.02157 0.02032 27,319.3 3,280.0 0.0 8C4.9 8C4.9 495,$ 15.4 297.9 f I 510 C90 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 30$ .4 1,153.4 506,096.0 398.4 )

I 490 C80 2200 0.01990 0.01970 4,89b.1 SM.1 0.0 151.5 1,304.8 511,1C5.6 446.3 )

I 480 470 2200 0.01970 0.01951 4,746.2 . 569.$ 0.0 146.8 1,451.6 SI&,03$ .& 491.$ I I C70 C&0 2200 0.01951 0.01933 4,582.5 550.2 0.0 141.7 1,593.4 520,762.$ 534.9 f I 460 450 2200 0.0'I933 0.019 I6 4,406.9 529.1 0.0 136.3 1,729.7 525,306.0 575.7 )

I 450 440 2200 0.01916 0.01900 C,219.8 506.d 0.0 130.5 1,860.2 529,656.3 614.0 I I 440 430 2200 0.01900 O.OIMS 4,021.1 C82.8 0.0 124.4 1,9$ C.S 533,801.7 650.0 )

I 430 C20 2200 O.OIMS 0.01870 4,085.d 490.5 0.0 126.4 2,110.9 538,013.7 6$ 6.0 )

I 420 4 IO 2200 0.01870 0.01855 4,151.7 0.0 497.6 51.7 2,1&2.6 542,217.1 697.3 I I 410 COO 2200 O.0I855 0.018C2 3,&S2.$ 0.0 437.8 45.5 2,20$ .1 545,9I5.4 707.2 i I 400 390 2200 0.01$ C2 O.OI828 3,991.9 0.0 478.5 49.7 2,257.9 549,957.0 717.8 I I 390 380 2200 O.OI$ 2d 0.01816 3,470.6 0.0 41&.0 43.3 2,30I.I 553,C70.9 726.9 I I 380 370 2200 0.01$ I& 0.01804 3,516.8 0.0 421.5 C3.8 2,345.0 557,031.5 736.0 )

I 370 360 2200 0.01804 0.01792 3,563.9 0.0 427.2 44.4 2,389.C 560,639.$ 745.1 I I 360 350 2200 0.01792 0.01781 3,309.1 0.0 396.d 41.2 2,430.6 563,990.1 753.5 I

'50 340 2200 0.01781 0.01770 3,350.2 0.0 C01.6 41.8 2,C72.4 567,382.1 761.8

)

I I 3CO 330 2200 O.0I770 0.017S9 3,392.1 0.0 406.6 42.3 2,51C. & 570,$ 16.5. 770.2 )

I 330 325 2200 0.01759 0.01754 1,555.9 0.0 186.5 19.4 2,534.0 572,391.8 774.0 I I 325 310 268 0.017SC 0.01754 0.0 0.0 0.0 0.0 2,534.0 581,928.5 761.3 I I 310 300 26$ 0.0175C 0.0174C 3;138.d 0.0 376.2 39.1 2,573.1 5$ 5,106.3 76$ .9 J I 300 260 26$ O.0I744 11,932.7 0.0 1,C30.3 148.7 2,72I.9 597, 187. 7 796.9

'.01707

)

I 260 235 268 0.01707 0.01687 6,66$ .0 0.0 799.2 83.1 2,805.0 603,938.8 812.0 I I 235 2 IO 268 0.01687 0.01669 6, 137.9 0.0 735.7 76.5 2,M1.4 610,153.2 825.7 )

I 210 200 268 0.01669 0.01662 2,C22.9 0.0 290.4 30.2 2,911.6 612,606.2 831.0 I I

I iTOTAL BAHT VOLUHE 8194.5 gallons I

I I

TABLE 2-26 I

PLANT COOLDORI FRCFI 557 F Tb 200 F; SANT AT 2.75 vtX SORIC ACID; RNT AT 2150 ppa RORON I I

)AVG.STS. TON'. PZR PRESS SPEClflC VOLIRIE. SHRINKAGE BAHT VOL 0 RMT )OL Q 5/A ADDED TOTAL 5/A TOTAL STS. HASS flNAL CONC. )

(pclI) (cu.f c./Iba) HASS(lba) 70 f (gal) 50 f (gal) (lba) (Iba) (lba) (ppa boron) )

I TI Tf vi vf I I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 C67,651.2 0.0 I 557 510 2200 0.02157 0.02032 27,319.3 3,2M.O 0.0 772.5 772.5 495,743.0 272.4 )

510 C90 2200 0.02032 0.01990 9,9l2.2 1,197.3 0.0 2S2.0 1,054.5 505,997.1 364.4 )

490 460 2200 0.01990 0.01970 4,d95.1 5M. I 0.0 135.5 1,193.0 511,033.7 405.1 CSO 470 2200 0.01970 0.01951 4,746.2 569.5 0.0 134.2 1,327.2 515,91C. I 449.5 I 470 460 2200 0.01951 0.01933 4,552.5 550.2 0.0 129.6 1,456.8 520,626.2 459.2 I 460 450 2200 0.01933 0.01916 4,C06.9 529.1 0.0 124.6 1,551.4 525,157.5 526.5 I 450 440 2200 0.01916 0.01900 4,219.8 50b.d 0.0 119.3 1,700.7 529,496.5 561.6 I 440 C30 2200 0.01900 O.0IM5 C,021.1 C52.5 0.0 113.7 I,SIC.4 533,631.6 59C.5 I 430 420 2200 O.OIMS 0.01870 4,055.6 C90.5 0.0 115.5 1,930.0 537,532.7 627.4 )

420 410 2200 0.01570 0.01555 4,151.7 496.5 0.0 117.4 2,047.4 542,101.8 660.3 )

410 400 2200 0.01555 0.01542 3,652.5 438.6 0.0 103.3 2,150.6 545,557.9 6SS.S )

COO 390 2200 0.01842 0.0152S 3,991.9 479.3 0.0 1 I2.9 2,263.5 5C9,962.7 719.6 I 390 380 2200 0.0152S O.0I516 3,470.6 0.0 416.0 43.3 2,306.S 553,476.5 726.7 I 380 370 2200 0.01816 0.01504 3,5ld.d 0.0 42'1.5 -43.5 2,350.6 557,037.1 D7.$ I 370 360 2200 O.0I804 0.01792 3,563.9 0.0 427.2 CC.4 2,395.0 560,6C5.4 7C6.9 I

'60 350 2200 0.01792 0.01761 3,309.1 0.0 396.6 41.2 2,436.3 563,995.S 755.2 [

350 340 2200 0.01751 0.01770 3,350.2 0.0 401.6 41.5 2,476.0 567,3S7.7 763.6 )

3CO 330 2200 0.0lllO 0.01759 3,392.1 0.0 ~ 406.6 42.3 2,520.3 570,522.1 771.9 I 330 325 2200 0.01759 0.0175C 1,555.9 0.0 166.5 19 4 2,539.7 572,397.C 775.7 )

325 310 265 0.0175C 0.01754 0.0 0.0 0.0 0.0 2,539.7 561,934.2 763.0 I 310 300 268 0.0175C 0.0174C 3,136.6 0.0 376.2 39.1 2,578.8 5$ 5, '111.9 770.5 )

3uu lou coo U,UIIIIII U Ullul I ly7JC ly1JVoa I II0 I CqlCI ~ 0 age, sv>.3 (70 J I 260 235 268 0.01/07 0. O'I 657 d,665.0 0.0 799.2 53.1 2,510.6 603,944.C 513.6 )

235 210 268 0.0'I 687 0.01669 6,137.9 0.0 735.7 76.5 2,M7.1 bio, 155.5 527.3 I 210 200 268 0.01669 O.0I662 2,422.9 0.0 290.4 30.2 2,917.3 612,6'11.$ S32.6 )

I (TOTAL BAHT VOLUHE 9610.8 gallons I

I I

TABLE 2-27 I I I PLANt COOLOOIRI FRCFt 557 F TO 200 F; SANT AT 2.5 atL RORIC ACIO; RMT AT 2150 ppa SOROR I I I IAYG STs ~ Tee%

a~

~ ~ eat'

~

PAPt ~ ct4 Im oat I'IIII IWOI'C

~ 04IIT WQ 0 OIIT

~ ~ ~

Mhl o ala annrn tnwi ala Tntai svs. NAss FINAL c(wc.l I (F) (paia) (cu.ft./Iba) IlASS(lba) 70 F (gal) 50 F (gal) ( lba) (Iba) (ppa boron) I Ti Tf Vi Vf I

I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 C67,651.2 0.0 I I 557 510 2200 0.02157 0.02032 27,319.3 3,2$ 0.0 0.0 700.5 700.5 495,671.0 247.1 I I 510 490 2200 0.02032 O.OI990 9,972.2 1,197.3 0.0 255.7 956.2 505,$ 9d.b 330.4 I I 490 480 2200 0.01990 0.01970 4,$ 98.1 5M.1 0.0 125.S 1,081.8 510,922.5 370.2 I I 4SO 470 2200 0.01970 0.01951 4,7C6.2 569.8 0.0 121.7 1,203.5 515,790.4 407.9 I I 470 CSO 2200 0.01951 0.01933 4,582.5 550.2 0.0 117.5 1,32I.O 520,490.4 443.7 I I 460 450 2200 0.01933 0.01916 4,406.9 529.1 0.0 113.0 1,434.0 525,010.3 477.5 I I 450 CCO 2200 0.01916 0.01900 4,219.8 506.d 0.0 108.2 1,542.1 529,33$ .3 509.4 I I 440 430 2200 0.01900 O.OIMS 4,021 F 1 482.8 0.0 103.1 1,6C5.3 533,C62.5 539.2 I I 430 C20 2200 0.01MS 0.01870 4,085.6 C90.5 0.0 10C.S 1,750.0 537,652.8 569.1 I I 420 410 2200 0.01870 0.01855 4 ~ 151.7 498.5 0.0 IOS.S 1,856.5 SC1,910.9 598.9 I I 410 400 2200 0.01855 0.01842 3,652.8 438.6 0.0 93.7 1,950.1 scs,esr.c 62C.S I I 400 390 2200 0.01842 0.0182d 3,991.9 479.3 0.0 102.4 2,052.5 549,751.S 652.7 I I 390 380 2200 O.0 IS28 0.01816 3,470.6 416.7 0.0 $ 9.0 2,141.5 553,311.2 ere.r I I 380 370 2200 O.0 ISIS O.OIINC 3,516.8 422.2 0.0 90.2 2,231.6 556,918.2 700.6 I I 370 360 2200 0.01$ 0C 0.01792 3,563.9 427.9 0.0 9I.4 2,323.0 560,573.C 724.5 I I 360 350 2200 0.01792 0.017SI 3,309.1 397.3 0.0 $ 4.$ 2,C07.9 563,967.C rce.s I I 350 3C5 2200 0.01781 0.01776 1,669.9 200.5 0.0 42.8 2,450.7 565,680.1 757.4 I I 345 330 2200 0.01776 0.01759 s,or2.c 0.0 608.0 63.2 2,513.9 570,815.7 770.0 I I 330 325 2200 0.01759 0.0175C 1,555.9 0.0 '186.5 19.4 2,533.3 572,391.0 773.d I I 325 3IO 268 0.0175C 0.01754 0.0 0.0 0.0 0.0 2,533.3 581,927.8 761.1 I I 310 300 268 0.0175C 0.01744 3,13S.d 0.0 376.2 39.1 2,572.4 585,105.5 768.7 I I 300 260 26S 0.01744 0.01707 11,932.7 0.0 1,430.3 1C8.7 2,721.1 597,186.9 796.6 I I 260 235 268 0.01707 0.01687 6,668.0 0.0 799.2 $ 3.1 2,M4.2 603,93S.O $ 11.8 I I 235 210 268 0.01687 0.01669 6,137.9 0.0 735.7 76.5 2,8S0.7 610,152.C S25.4 I I 210 200 268 0.01669 0.01662 2,C22.9 0.0 290.C 30.2 2,910.9 612,605.C S30.7 I I I ITOTAL RANT VOLtatE 11C75.4 gallons, I I I

TABI.E 2-28 I

PLANT COOLOQRI FROH 557 F lO 200 F; BAHT Al 3.5 st% BORIC ACIO; RNT Al 2300 ppa BORON I

I (AVG.STS. TEIN'. PZR PRFSS SPECIFIC VOLIRIE SNRINKACE BAHT VOL 0 RNT VOL 8 B/A ADOEO 'IOTAL 8/A TOTAL STS. HASS FINAL CONC.I (F) (paia) (cu. ft./IIaa) HASS(IIaa) 70 F (gal) 50 f (gal) ( I Iaa) ( I taa) (IIaa) (ppa boron) I Ti Tf Vi Vf I

.--- I 557 ssl 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I 557 500 2200 0.02 Isl 0.02011 32,253.3 3,872.4 0.0 1,169.8 1,169.8 501,074.3 40S.2 I 500 490 2200 0.02011 0.01990 5,038.1 60C.9 0.0 182.7 1,352.5 506,295.2 467.1 I 490 CSO 2200 0.01990 0.01970 4,89S.1 5M.1 0.0 1ll.l 1,5M.2 511,370.9 523.2 I 480 Clo 2200 O.0I970 0.01951 4,746.2 569.8 0.0 172.1 1,702.3 516,289.3 576.5 I 470 C64 2200 0.01951 0.019CO 2,739.3 328.9 0.0 99.C 1,801.7 519 127 9 606-8 I 464 450 2200 0.019CO 0.019 lb 6,250.1 0.0 749.1 83.3 T,M5.0 525,461.4 627.2 I 450 440 2200 O.OI9I6 0.01900 4,219.8 0.0 505.8 56.2 1,941.3 529,737.4 6CO.l I 4CO 430 2200 0.01900 O.OIM5 4,021+1 0.0 482.0 53.6 '1,99C.9 533,812.1 653.4 430 C20 2200 O.OIM5 0.01870 4,085.6 0.0 489.7 5C.5 2,0C9.3 537,952. 1 666.0 I I ch 420 410 2200 0.0'I870 0.01855 4,151.7 0.0 497.6 55.3 2, IOC. 7 542, 159.1 678.7 CD I 410 400 2200 0.01855 0.018C2 3,652.8 0.0 437.8 48.7 2,153.3 545,860.6 689.7 I COO 2200 0.018C2 0.01828 3,991.9 0.0 C78.5 53.2 2,206.6 5C9,905.7 701.5 I 390 380 2200 0.01828 0.01816 3,C70.6 0.0 416.0 C6.3 2,252.8 553,C22.6 711.7 I 380 370 2200 0.01816 0.01804 3,516.8 0.0 C21.5 46.9 2,299.7 556,986.2 721.9 I 370 360 2200 0.0'ISOC 0.01792 3,563.9 0.0 427.2 47.5 2,347.2 560,597.6 732.0 I

'360 350 2200 0.01792 0.01781 3,309.1 0.0 396.6 44.1 2,391.3 563,950.8 7C1.3 I

'50 3CO 2200 O.0I781 0.01770 3,350.2 0.0 401.6 44.7 2,C36.0 567.345.7 750.7 I 340 330 2200 0.01770 0.01759 3,392.1 0.0 406.6 45.2 2,481.2 570,783 .0 760.0 I 330 325 2200 0.01759 0.01754 1,555.9 0.0 186.5 20./ 2,501.9 572,359.l 764.2 I 325 310 268 0.01754 0.0175C 0.0 0.0 0.0 0.0 2,501.9 sbl, 896.4 751.7 I 310 300 2M 0.01754 0.01744 3,13S.d 0.0 376.2 41.8 2,543.8 585,076.9 760. 1 300 260 26S 0.0174C 0.01707 11,932.7 0.0 1,C30.3 159.1 2,702.8 597,1M.6 791.3 I 260 235 268 0.01707 0.0168l 6,668.0 0.0 799.2 88.9 2, 791.7 603,925.6 808.2 I 235 2IO 268 O.OI687 0.01669 6,137.9 0.0 735.7 81.8 2,873.5 610, TC5.2 823.4 I 210 200 268 O.OI669 0.01662 2,422.9 0.0 290A 32.3 2,905.8 612,6M.C 829.3 I I

IIOTAL BAHT VOLTE 596C.1 gal iona I

I I

TABTE 2-29 l

PLANT COOLO(RAI FROH 557 F To 200 F; RAHT AT 3.25 utX RELIC ACIO; RNT AT 2300 ppa RORON I I

)AVCi.STS. TEIN'f)

PZR PRESS SPECIFIC VOLQK SHRINKAGE RANT VOL 0 RMT VOL 0 8/A AOOEO TOTAL 8/A TOTAL SYS. HASS FINAL CONC (

(paia) (cu.f t./Lba) HASS(lba) 70 f (Oal) 50 f (Oal) (Lba) (Lbs) (Lba) (pfaa boron) )

) Ti Tf vi vf I l

I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 4d7,651.2 0.0 I I 557 510 2200 0.02157 0.02052 27,319.3 3,260.0 0.0 917.7 917.7 495,666.2 323.6 I I 510 490 2200 0.02032 0.0'l990 9,972.2- 1,197.3 0.0 335.0 1,252.7 506, 195.3 432.7 I I Coo tan n ninon n ninon ~ na coa n n abc c l 1't C ~ 4 '%4 4 ~ ~ yhpv 0 tM

~ 4 %

~

I 480 Cro 2200 0.01970 0.01951 4,7C6.2 569.8 0.0 159.4 1,576.7 516,163.6 534.0 )

I IPO C60 2200 0.01951 0.01933 4,582.5 550.2 0.0 153.9 '1,750.6 520,900.0 580.9 )

I 460 450 2200 0.01933 0.01916 4,C06.9 529.1 0.0 IC8.0 l,bib.l 525,C55.0 I 450 440 2200 0.01916 O.OI900 4,219.8 0.0 505.6 se.2 1,934.9 529,751.0 638.6 )

I 440 430 2200 0.01900 0.01665 4,021.1 0.0 482.0 53.6 1,966.5 533,805.7 651.3 )

I C30 420 2200 0.01665 O.0 idio C,MS.6 0.0 C69.7 54.5 2,043.0 537,945.8 664.0 )

I C20 410 2200 O.0 1870 O.OIOSS 4,151.7 0.0 497.6 55.3 2,098.3 SC2,152.8 676.7 I I 410 Coo 2200 0.01655 0.01642 3,652.8 0.0 43r.d 46.7 2,147.0 545,654.2 687.7 )

I 400 390 2200 0.01842 0.01828 3,991.9 0.0 C78.5 53;2'6.3 2,200.2 SC9,899.4 699.5 )

I 390 360 2200 0.01628 0.01616 3,470.6 0.0 416.0 2,246.5 553,416.2 709.7 )

I 360 370 2200 O.0I816 0.01604 3,516.8 0.0 421.5 46.9 2,293.3 Ssd,979.9 719.9 )

I 370 360 2200 0.0160C 0.01792 3,563.9 0.0 427.2 47.5 2,340.8 560,591.3 730.1 I 360 350 2200 0.01792 0.01781 3,309.1 0.0 396.6 C4.1 2,365.0 563,944.5 739.C )

I 350 340 2200 0.01761 0.01770 3,350.2 0.0 401.6 CC.7 2,429.6 567,339.3 748.7 )

I 340 330 2200 0.01770 0.01759 3,392.1 0.0 406.6 C5.2 2,474.8 Sro,rre.r 758.1 )

l 330 325 2200 0.01759 0.01754 1,555.9 0.0 166.5 2o.l 2,495.6 572,353.3 762.3 )

I 325 310 268 0.0175C 0.0175C 0.0 0.0 0.0 0.0 2,495.6 581,690. I 749.8 I I 310 300 268 O.OLTSC 0.01744 3,136.6 0.0 376.2 41.8 2,537.4 565,070.5 758.2 )

I 300 260 268 O.OI74C 0.01707 11,932.7 0.0 1,C30.3 . 159.1 2,696.5 597,162.3 789.5 )

l 260 235 268 0.01707 0.01667 6,666.0 0.0 799.2 66.9 2,765.4 603,919.2 606.C f I 235 2IO 268 0.01687 0.01669 6,137.9 0.0 735.7 81.8 2,667.2 610, 138.9 821.6 )

I 210 200 266 0.01669 0.01662 2,422.9 0.0 290.4 32.3 2,699.5 612,594.0 827.5 )

I I

)TOTAL RANT VOLLRLE 6714.5 gaLLons I I I

TABLE 2-30 I

PLANT COOLDONI FROI 557 F TO 200 F RANT AT 3.0 rrt'I RORIC ACID; RMT AT 2300 ppa 8ORON I I

)AVQ.STS. TOgr PZR PRESS SPECIfIC VOLWE SNRINKACE RANT VOL O RMT VOL 0 RIAAODm TOTAL RIA TOTAL SVS. NASS FINAL CONC.(

(f) (paia) (cu.f t./Ihar) IIASS(IIaa) 70 F (gal) 50 f (gal) ( (bra) ( IIaa) (IIaa) (ppra boron) i Ti Tf VI Vf I I

557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I 557 510 2200 0.02lsl 0.02032 27,319.3. 3,280.0 0.0 544.9 8CC.9 495,815 4 297.9 )

510 490 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 305.4 1,153.4 506,096.0 398.4 )

490 460 2200 0.01990 0.01970 4,898.1 585.1 0.0 151.5 1,304.5 511, N5.6 4C6.3 )

480 470 2200 0.01970 0.01951 4,746.2 569.8 0.0 Nd.b 1,451.d 516,038.6 491.5 )

470 C60 2200 0.01951 0.01933 4,582.5 550.2 0.0 141.7 1,593.4 520,762.5 534.9 (

450 2200 0.01933 0.019 I6 C,406.9 529.1 0.0 136.3 1,729.7 525,306.0 575.7 )

450 440 2200 0.01916 0.01900 4,219.8 506.d 0.0 130.5 1,860.2 529,656.3 614.0 I CCO 426 2200 0.01900 0.01879 5,647.5 675.1 0.0 174.7 2,034.5 535,475.4 66C.4 )

426 420 2200 0.01879 O.0 1570 2,459.2 0.0 29C.8 32.8 2,067.6 537,970.C 671.9 I 420 C10 2200 0.01870 0.01555 4,151.7 0.0 497.6 55.3 2,123.0 542,177.4 M4.6 i 410 400 2200 0.01555 0.01542 3,652.8 0.0 437.5 48.7 2,171.6 545,575.9 695.5 )

400 390 2200 0.018C2 0.01528 3,991.9 0.0 475.5 53.2 2,224.9 5C9,924.0 707.3 )

390 380 2200 0.01825 0.01816 3,470.d 0.0 416.0 C6.3 2,271.1 553,440.9 717.5 I 380 370 2200 0.01816 0.01804 3,516.8 0.0 421.5 46.9 2,318.0 557,00C.S 727.6 )

370 360 2200 0.0180C 0.01792 3,563.9 0.0

427.2 47.5 2,365.5 560,615.9 737.7 )

(

360 350 2200 0.01792 0.01751 3,309.1 0.0 396.6 C4.1 2,C09.6 563,969.1 747.0 I 350 340 2200 O.OI78I 0.01770 3,350.2 0.0 401.6 44.7 2,454.3 567,364.0 756.3 )

I 340 330 2200 0.01770 0.01759 3,392.1 0.0 C06.6 45.2 2,C99.5 570,501.3 76S.6 i I 330 325 2200 0.01759 0.0175C 1,555.9 0.0 186.5 20.7 2,520.2 572,378.0 769.8 (

I 325 310 268 0.01754 0.0175C 0.0 0.0 0.0 0.0 2,520.2 551,91C.l 757.2 )

I 310 300 265 0.01754 O.0I7CC 3,138.6 0.0 376.2 41.5 2,562.1 555,095.2 765.6 I I 300 260 2M 0.017CC 0.01707 11,932.7 0.0 1,430.3 159.1 2,721.1 597, 186.9 796.6 )

I 260 235 2M 0.01707 O.OIMl 6,668.0 0.0 799.2 85.9 2,810.0 603,9C3.9 813.5 I I 235 2IO 268 O.OIM7 0.01669 6,137.9 0.0 735.7 51.5 2,591.8 610,163.5 828.6 )

.I 210 200 268 0.01669 0.01662 2,422.9 0.0 290.$ 32.3 2,924.1 612,dlb.l 53C.5 I I I i TOTAL RANT VOLtatf. 7899.2 got lore, I

I I

TABLE 2-31 I

PLANT COOLDOW FRON 557 F'TO 200 FT RANT AT 2.75 stX BORIC ACID; RUT AT 2300 ppa INION I l

iAVG.STS. HS . PZR PRESS SPECIf IC VOLWE SHRINKAGE RANT VOL 0 Rill VOL 0 5/A AODEO TOTAL 8/A TOTAL SYS. NASS F INAL CONC- )

I (F) (Peia) (cu. ft./Iba) NASS(iba) lo f (Bal) 50 f (Bal) (Iba) (Iba) (Isa) (ppa terran) )

Ti Tf Vi Vf I I I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I 557 510 2200 0.02157 0.02032 27,3I9.3 3,260.0 0.0 772.5 772.5 CPi,743.0 272.4 I 510 490 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 262.0 1,054.5 505,997.1 364.4 )

C90 450 2200 0.01990 0.01970 C,898.1 SM.1 0.0 138.5 1,193.0 511,033.7 4M.1 i 480 470 2200 0.01970 0.019S1 4,7C6.2 569.5 0.0 134.2 1,327.2 515,914.1 449.8 1 Clo C60 2200 0.01951 0.01933 4,S62.5 550.2 0.0 129.6 1,456.5 520,626.2 459.2 I Cba 450 2200 0.01933 0.01916 4,C06.9 529.1 0.0 124.6 1,551.4 525,157.5 526.5 (

CSO CCO 2200 O.0I916 0.01900 C,219.8 506.6 0.0 119.3 1,700.l 529,496.5 561.6 )

440 430 2200 0.01900 O.albbS C,021.1 C52.5 0.0 113.7 1,5IC.4 533,631.6 594.5 (

430 420 2200 0.01MS 0.01570 4,085.6 C90.5 0.0 115.5 1,930.0 537,832.7 627.4 I 420 4IO 2200 0.01870 O.OISSS 4,151.7 495.5 0.0 117.C 2,047.4 SC2,101.5 660.3 )

410 Coa 2200 0.01655 0.01642 3,652.8 438.6 0.0 103.3 2,150.6 545,557.9 6$ 8.8 )

COO 390 2200 0.01842 0.01525 3,991.9 0.0 478.5 53.2 2,203.9 SC9,903.0 700.7 )

390 380 2200 0.01628 O.Olalb 3,470.6 0.0 416.0 46.3 2,250.1 553,419.9 710.5 I 380 370 2200 0.01516 0.01$ 0C 3,516.5 0.0 421.5 46.9 2,297.0 556,M3.5 721.0 )

370 360 2200 0.01604 0.01792 3,563.9 0.0 427.2 47.5 2,3CC.5 560,594.9 731.2 )

360 350 2200 0.01792 0.01781 3,309.1 0.0 396.6 44.1 2,365.6 563,948.1 740.5 I 350 3C0 2200 0.01751 0.01770 3,350.2 0.0 Cal.b 44.7 2,433.3 567,343.0 749.5 I 340 330 2200 0.0'Illa 0.01759 3,392.1 0.0 406.6 45.2 2,475.5 570,780.3 759.2 (

330 325 2200 0.01759 0.01754 1,555.9 0.0 186.5 20.7 2,C99.2 572,357.0 ~

763.C I 325 310 268 0.01754 O.all54 0.0 0.0 o.a o.a 2,499.2 551,593.7 750.9 )

310 300 2650.01754 0.0174C 3,138.6 0.0 376.2 41.5 2,541.1 555,074.2 759.3 )

300 260 2650.01744 O.allol 11,932.7 0.0 1,430.3 159.1 2,700.1 597, 165.9 790.5 f 260 235 2650.01707 0.016$ l 6,6M.O 0.0 799.2 M.9 2,789.0 603,922.9 807.C )

235 2IO 268 0.0 I 667 0.0'I 669 6,137.9 0.0 735.7 51.5 2,870.5 610, 1C2.5 822.d )

210 200 266 0. 01669 0.01662 2,422.9 0.0 290.4 32.3 2,903. I 612,597.7 525.5 I I

)TOTAL BAHT VOLIjNE 9131.5 gaI Ions I I I

TABLE 2-32 I

I PLANI COOLD(RW FROH 557 F to 200 F; RAHt At 2.50 vIX SDRIC ACID; RNt At 2300 ppa RINION I

I I

IAVO.sts. tFHP. Pzg PRcss sPSCIFIC VOLIRIE SNRINRA06 8AHI vm. g RNI VOL g RIA amo totAL RJA IOIAL SYS. HASS FINAL CONC.I (F) (paia) (cu.f t./Iba) HASS(lba) 70 F (gal) 50 F (gal) (Iba) (Iba) ( Iba) (ppaa boron) I ti tf Vi Vf

" -"I I 557 557 2200 1.00000 1.00000 0.0 0.0 0.0 0.0 0.0 467,651.2 0.0 I 557 510 2200 0.02157 0.02032 27,319.3 3,280.0 0.0 700.5 700.5 495,el 1.o 247.1 I 510 490 2200 0.02032 0.01990 9,972.2 1,197.3 0.0 255.7 95e.2 505,898.8 330A I C90 4M 2200 0.01990 0.01970 C,898.1 5M.1 0.0 125.6 . 1,081.8 510,922.5 370.2 I Cbo 470 2200 0.01970 0.01951 4,746.2 569.8 0.0 121.7 1,203.5 515,790.4 407.9 I 470 460 2200 0.01951 0.01933 4,562.5 550.2 0.0 117.5 1,321.0 520,490.4 443.7 I C60 450 2200 0.01933 0.01916 4,406.9 529.1 0.0 113.0 1,434.0 525,010.3 477.5 I 450 CCO 2200 0.01916 0.01900 4,219.$ 506.d 0.0 108.2 1,5C2.1 529,338.3 509.4 I 4CO C30 2200 0.01900 0.01865 4,021.1 CS2.S 0.0 103.1 1,6C5.3 533,C62.5 539.2 I 430 420 2200 O.OIM5 0.01870 4,085.d 490.5 0.0 10C.S 1,750.0 537,652.8 569.1 420 410 2200 0.01870 0.01655 4,151.7 498.5 0.0 106.5 1,856.5 5C1,910.9 596.9 I 410 Coo 2200 0.01655 O.OI642 3,652.6 438.6 0.0 93.7 1,950.1 scs,esr.c 624.8 I 400 390 2200 O.OISC2 0.01828 3,991.9 419.3 0.0 102.4 2,052.5 549,751.6 es2.7 I 390 3SO 2200 0.01628 0.01816 3,470.6 416.7 0.0 69.0 2,141.5 553,311.2 ere.r I 380 370 2200 0.01616 0.01604 3,516.8 422.2 0.0 90.2 2,231.6 556,916.2 700.6 I 370 360 2200 0.01604 0.01792 3,563.9 427.9 0.0 91.4 2,323.0 560,573.4 724.5 I 360 350 2200 0.01792 0.01781 3,309.1 397.3

'.0 2,407.9 SC.S 563,967A lce.s I

- 350 3CO 2200 O.0I761 0.01770 3,350.2 0.0 401.6 44.7 2,452.5 567,362.2 755.7 I 3CO 330 2200 0.01770 0.01759 3,392.1 0.0 406.6 45.2 2,C97.7 570,799.6 res.o I 330 325 2200 0.01759 0.01754 1,555.9 0.0 186.5 20.7 2,518.5 572,376.2 769.3 I 325 310 26$ 0.01754 0. 01754 0.0 0.0 0.0 0.0 2,518.5 581,913.0 756.l I 310 300 26S 0.01754 0.017CC 3,138.6 0.0 41.8 376.2 2,560.3 SS5,093.C res.l I 300 260 26S 0.01744 0.01707 11,932.7 0.0 1,430.3 159.1 2,719A 597,1$ 5.2 796.1 I 260 235 26S 0.01707 O.OIMl 6,668.0 0.0 799.2 86.9 2,80$ .3 603,942.1 S13.0 I 235 210 268 0. 01667 0.01669 6,137.9 0.0 735.7 81.8 2,890.1 610,161.S 828.1 210 200 26S 0.01669 0.01662 2,422.9 0.0 290A 32.3 2,922.C 612,616.9 834.0 I I

IIOIAL RAHI VOLTE 1127C.9 gallons I

I I

Table 2-33 Required Boron Concentration for a Cooldown from 557 Oegrees to 200 Degrees Temperature Concentration Oe rees F m boron 557 -75.4 510 110.9 490 181. 4 480 216.5 470 245.0 460 272.6 450 300.3 440 328.5 430 356.1 420 383.9 410 412.2 400 437.3 390 460.6 380 484.0 370 507.3 360 533.0 350 551.3 340 567.0 330 582.6 325 591.5 310 618.5 300 635.9 260 700. 1 235 735. 5 210 769.4 200 . 782.2 199.9* 667.9 199.9** 702.2

Note: After Shutdown margin change from 3.6X delta k/k to 2.(5 delta k/k.

~Note: The boration requirement for a 2.0X shutdown margin and core is xenon free.

2-65

Table 2-34 Minimum Boric Acid Makeup Tank Volume vs. Stored Boric Acid Concentration for Modes 1, 2, 3, and 4 Minimum Volume allons BAMT RWT at ,RWT at RWT at RWT at RWT at Conc ~1720 m ~1850 m 2000~m ~2150 m 2~300 m 3.5 7,317.1 7,068.3 6,714.5 6,448. 8 5,964.1 3.25 8,194.5 7,850.3 7,606.8 7,170.1 6,714.5 3.0 9,226.7 8,911.4 8,592.6 8,194.5 7,899.2 2.75 10,449.7 10i237.9 10,027.4 9,610.8 9,131.5 2.50 12,271.2 12,084.4 11,839.4 11,475.4 11,274.9 2-66

Table 2-35 Calculation of the 14,000 Gallon Volume In Specification 3/4.1.2 12,552.2 gallons Cooldown to 325 degrees and 268 psia (Part A)

+8,413.0 Cooldown to 200 degrees on shutdown cooling (Parts B 5 C)

-7 317.1 Smallest BAHT inventory value for 1720 ppm Boron in the RWT from Table 2-34 13,648.1 gallons Total 14,000.0 gal lons Total rounded up to the nearest 1000 gallons 2-67

Table 2-36 Calculation of the 45,000 Gallon Volume In Specification 3/4.1.2 for St. Lucie 1 23,040.0 gallons System feed-and-bleed (Part A) 12,552.2 Cooldown to 325 degrees and 268 psia (Part 8)

+ 8,413.0 Cooldown to 200 degrees on shutdown cooling (Parts C 5 0) 44,005.2 gallons Total 45,000.0 gallons Final volume (Part E) ~ounded up to the nearest 1000 gallons.

2-68

FIGURE 2 3 BORIC AC ID SOLUBILITY IN NATER ( weight 5 )

't T

16 12 10 0

20 40 6a aa 1aa 120 140 TEMPERATURE ( deggwi F )

FIGURE 2 2 ST. LUCIE i EFFECT OF COOLDOWN RATE ON BORATION REQUIREllENT a00 700 z 600 0

500 400 V

z 0

300 N

V a

W 200 D

0 4I IOO L

-100

)50 250 350 450 550

/hr TELIPERATURE (f) 12.5 I 2G rz nr u au rxnr 1UU t/hr

FIGURE 2 3 ST. LUCI E 1 RCS BORON CONC vs TEMP FOR MAKEUP FROM BAMT 790 780 770 0

IL I

0 E

750 z

0 740 I

0 z

0 720 0

0 K 710 700 690 120 140 160 180 200 220 Q

TEMr ERATURE (0 CURVE 1,REQUIREDppm CURVE 2, ACTUAL ppm

FIGURE 2 4 ST.LUCIE 1 RCS BORON CONC vs TEMP FOR MAKEUP FROM RWT 7SO 780 Z 770 0

0760 m

E 750 740 730 o 720 o

710 700 690 120 140 160 180 200 220 TEMPERATURE (F) 0 CURVE 1,REQUIREDppm + CURVE 2, ACTUAL ppm

FIGURE 2 5 ST.LUCIE 1 RCS BORON CONC vs TEMPERATURE for 12.5 F/hr COOLDOWN 900 800 z 700 0 (2) mO 600 E

500 z

400 300 o

z o200

+

o 100 100 600 500 400 300 200 TEMPERATURE (F) 0 CURVEl,REQUlREDppm +'URVE 2, ACTUAL ppm THE BORATION REQUIREMENT FOR A 2X SHUTDOWN MARGIN, XENON FREE CORE (I) THE BORATION REQUIREMENT FOR A 3 ~ 64 SHUTDOWN MARGIN (2) THE BORATION REQUIREMENT FOR A 2X SHUTDOWN MARGIN W/SOME XENON IN CORE

FIGURE 2 6 ST.LUCIE 1 MIN BAMT VOLUME VS STORED BAMT CONCENTRATION 14 13 12 C

0 11 0

bJ a

~ C0

~

~a 10 Q 0

>r

~ I-9 m

8 2.4 2.6 2.8 3.0 3.2 3.4 3.6 STORED BAMT CONC (wt X boric acid) 0 1720 + 1850 0 2000 4 2150 X 2300

FIGURE 2 7 ST.. LUCIE 1 REQUIRED vs ACTUAL CONC FOR BTP 5-1 COOLDOWN 700 600 Z 500 0

K I

0 400 E

300 Z

0 200

.Z 100 0

0 Z

0 O

O K -100

-200

-300 TIME ( hours )

0 REQUIRED CONC + ACTUAL CONC

FIGURE 2 8 ST. LUCIE 1 REQUIRED vs ACTUAL CONC FOR BTP 5-1 COOLDOWN 500 400 Z

0 300 0

m E

200 100 0

0 0

O

-100

-200

-300 3.4 3.8 4.2 4.6 TIME ( hours )

D REQUIRED CONC + ACTUAL CONC

FIGURE 2 9 ST.LUCIE 1 RCS BORON CONC vs TEMPERATURE for RWT COOLDONtN 900 800 700 z

0 K

0 600 m

E 500 z

0 300 0

z 0 200 0

0 K 100 0

-100 600 500 400 300 200 TEMPERATURE (F) 0 > CURVE1,REQUIREDppm + CURVE 2, ACTUAL ppm

3. 0 OP ERAT IONAL ANALYSIS 3.1 INTROOUCTION TO THE OPERATIONAL ANALYSIS The remaining Sections of this report present the results of an evaluation performed in order to demonstrate the general impact on plant operations of a reduction in boric acid makeup tank concentration. The specific areas that will be discussed in lude operator respon!e to emergency situations, typical plant feed-and-bleed operations, typical plant blended makeup operations, plant shutdown to refueling, and plant shutdown to cold shutdown. Because it is obviously an impossble task to evaluate each of these five areas and consider all possible combinations .

of plant conditions, initial plant parameters and analysis as. umptions that were used in the evaluation were selected, where possible, in a conservative manner in order to give worst case type answers. As a consequence, the results, i.e., the volumes and final concentrations that were obtained, should in general be bounding for any event or any set of initial plant conditions.

3.2 RESPONSE TO EMERGENCY SITUATIONS In general, credit is not taken for boron addition to the reactor coolant system from the boric acid makeup tanks for the purpose of reictivity control in the accidents analyzed in Chapter 15 of the plant' Final Safety Analysis Report. The response of an operator, therefo e, to such events as steam line break, overcooling, boron dilution, etc., will not be affected by a reduction in boric acid makeup tank concentrition. In particular, the action statements associated with Technical S)ecification 3.1.1.1 and Technical Specification 3.1.1.2 require that boration be commenced at greater than 40 gallons per minute using a solution of at least 1720 ppm boron in the event that shutdown margin is lost. Such statements are conservatively based upon the refueling water tank 3-1

concentratii)n and are therefore indeperdert of the amount of boror. in "he BANTs. In >ddition, the acceptance criteria developed for .he Reactivity Control Sec-.ion of the Fur ctional Recovery Guidelines c< Reference 4,"

are based u~)on a boron addition rate of 40 gallons per miru .e and are also independent of the exact boration source concentration.

3.3 FEED-AHO-BLEED 0PERATIONS Durirg a fend-and-bleed operation to increase system boron content, the charging pur)ps are used to inject concentrated boric acid into the RCS with the excess inventory normally being diverted to the liquid waste system via 'tdown. The rate of increase in boron concentraticn is propnr+iona to the difference between the system concentration at any given time >>nd the concentration of the charging fluid. From this basic relationshi]), an equation describing feed-and-bleed can be derived.

(Appendix I contains the derivation of the reactor coolant system feed-and-bl>>ed equation). In gereral, if the ccncentration within the boric acid ))akeup tanks is reduced to .he point where heat tracing is no longer requ red, the maximum rate cf change of RCS boron corcentration that an ope"ator can expect to see during feed-and-bleed wi 11 be less than curren".1<< achievable.

The purpose of the evaluation performed in this section of the report was to show the exact eed-and-bleed rates that can be expected using boric acid makeup tanks having a reduced concentration. The analysis was done assumirg ho". zero power conditions with other key parameters and conditions shown in Table 3-1. Both a one charging pump and a two charging pu>>p feed-and-bleed were evaluated from two init'.al system concentratii)ns: zero ppm and 800 ppm. The results are presented in

Table 3-2 to Table 3-5. Equation 9.0 of Appendix 1 was used to generate the results in these tables. The value of the system mass used to obtain the time constant in Equation 9.0 was calculated as follows for St. Lucie 1:

w RCS w loops w PZR ol (m )

9,601 ft + 460 ft w

0.020854 f ./lb 0.02669 ft /ibm From this system mass (477,626.2 ibm), the value of the feed-and-bleed time constant for one charging pump is T40

= 477 626.2 ibm 40 gpm x 8.329 ibm/gallon or

'40 1,433.6 min.

.and the value of the feed-and-bleed time constant for two charging pumps 15

'84 477,626.2 ibm 84 gpm x 8.329 ibm/gallon or T84 682. 7 min.

(1) Specific volume of compressed water at 532 degrees and 2200 psia.

(2) Specific volume of saturated water at-2200 psia.

(3) Water density at 70 degrees.

3-3

Several nf the concentration results shown in Table 3-2 through Table ".-'.

choric are plotted in Figures 3- l and 3-2 for comparison, ~emote that significant feed-anC-bleed ra'es will be achievable following the reduction ir.

acid makeup tank concentration levels.

3.4 BLENOEO l!AKEUP OPERATIONS Dur',ng typical plant blerdin'g operations, concentrated boric acid via FCV-2210Y ~s mixed with cemineralized water via FCV-2210X a. the blending tee and then added to the volume control tank. Since the ability to blend and add makeup to the reactor coolant svstem ard to other sys .ems's important to plart operations, three different oarametric studies were oerformed in order to demonstrate the effect o a reduction in boric acid makeup tank concentratior . The studies performed were as follows:

1. Flow .hrough FCV-"2: OY is varied between 0.5 gpm and 15.0 gpm while the flow through FC< -2210X is varied to give a total flow out of the blending tee 'of 44 c allons per minute.

2. Flow through FCV-22: QY is varied between 0.5 gpm and 15.0 gpm while the flow through FC) -2210X is varied to give a total flow out of the blending tee of 88 <al-lons per minute.

3. Flow through FCV-22:.OY is varied between 0.5 gpm ard 15.0 gpm while the flow through FC>'-2210X is varied to give a total lnw out of '.he blending tee of 132 gallons per minute.

In each o the three studies, the temperature of the boric acid makeup tank and the temperature of'.he demineralized water supply was assumed tn he 70 degrees. The results are shown in Table 3-6 through Table 3-8. The-final concentration out of the blending tee in each of these .ables was obtained using the following equation:

3-4

(F .C)

'out = (100) (1748.34).

(y' +

out '

In this equation, C ut is the concentration coming out of the blending tee in ppm boron, F is the flowrate coming out of CH-0210Y in gallons per minute, C is the concentration of the boric acid makeup tanks in ibm per gallon, F ut is the total flow coming out of the blending tee in gallons per minute, 0w is the density of water at 70 degrees in ibm per gallon, and 1748.34 is the conversion factor between concentration expressed in terms of weight percent boric acid and concentration expressed in terms of ppm boron. (See Appendix 4 for a derivation of this conversion factor). The data contained in Tables 3-6, 3-7, and 3-8 is plotted in Figure 3-3 through Figure 3-5. Note that following the reduction in BAHT concentration, a full range of flowrates and boron concentrations are available for blended makeup operations.

3.5 SHUTOOWN TO REFUELIsNG - MODES 6 The plant shutdown to the refueling is typically the most limiting evolution that an operator must perform with respect to system boration, i.e., this evolution normally requires the maximum amount of boron to be added to the reactor coolant system. A shutdown to refueling normally occurs at the end of core cycle when the critical boron concentration is low and requires an increase to the refueling boron concentration. In the most limiting case, boron concentration must be raised from zero opm to the present refueling concentration of 1720 ppm.

This section presents the evaluation results of a plant shutdown to refueling. The evaluation was performed specifically to demonstrate the effect on makeup inventory requirements of a. reduction in boric acid storage tank concentration. A list of key parameters and conditions assumed in the analysis is contained in Table 3-9. The evaluation was 3-5

performed for end-of-cycle conditions in order to maximize the amount o f boron that must be added to the reactor coolant system. As a result, the boron concentration within the RCS was required to be increased from zero ppm to the present refueling concentration of 1720 ppm. The shutdown for refueling was assumed to take place as follows:

1. The reactor is shutdown via rod insertion to hot zero power conditions.

2. Following shutdown, at time zero, operators commence system feed-and-bleed using three charging pumps and the boric acid makeup tanks. (BAMT concentration is assumed to be 3.5 weight percent boric acid).

3. The feed-and-bleeds are conducted for 40 minutes, after which time they are secured.

4. A plant cooldown and depr essurization is commenced from an average coolant temperature and system pressure of 532 degrees and 2250 psia to an average coolant temperature and system pressure of 325 degrees and 268 psia. An overall cooldown rate of approximately 100 degrees per hour is assumed. Makeup inventory is supplied from the boric acid makeup tanks.

5. The shutdown cooling system is placed in operation at 325 degrees and 268 psia. (Prior to initiation, the concentration within the SOCS is assumed to be equal to the concentration in the reactor coolant system).

6. The plant cooldowns are continued following shutdown cooling initiation from 325 degrees to 135 degrees at 268 psia. A rate of 100 degrees per hour is assumed. between 325 degrees to 175 degrees, 3"6

a rate of 75 degrees per hour is used between 175 degrees and 156 degrees, and 50 degrees per hour is used between 156 degrees and 135 degrees. Makeup inventory is supplied from the boric acid makeup tanks.

Evaluation results showing the system concentrations as a function of time and total boric acid makeup tank inventory requirements are contained in Table 3-10. Loop average temperature and system boron concentration data from this table is plotted in Figure 3-6.

Concentrations during the initial feed-and-bleed operations were calculated using the methodology discussed in Section 3.3 above.

Concentrations during the subsequent plant cooldown were calculated in the same manner as the concentrations for the plant cooldowns in Section 2.4. Note that the boron content of the RCS was raised from zero ppm at the start of the evaluation to greater than 1720 ppm by the time the plants had been cooled and depressurized to 135 degrees and 268 psia. A total volume of 23,440. 1 gallons of a 3.5 weight percent boric acid solution were required. Of this volume, 5120 gallons were used during the initial forty minute plant f ed-and-bleed operati'on, and 18,320. 1 gallons were charged into the system to compensate for shrinkage during the cooldown process.

As can be seen from the results in Table 3-10, the volume of a 3.5 weight percent boric acid solution that is required in order to perform the shutdown to refueling is approximately 2.3 times the capacity of one boric acid makeup tank. Note that this result is conservative or bounding, and therefore, represents the maximum volume that would be required to be available assuming a refueling concentration of 1720 ppm boron and a boric acid makeup tank concentration of 3.5 weight percent boric acid. Since there are only two boric acid makeup tanks in each plant, with the combined capacities of approximately 19,400 gallons, additional provisions or operator actions are required in order to place the plant in Mode 6. These provisions could include some combination of the following:

3-7

l. An extended plant feed-and-bleed could be performed using the refueling water tank. This would decrease the amount of inventory needed from the boric acid makeup tanks.

2. Prior to conducting the evolution, both boric acid makeup tanks are full and available for use.

3. During the initial part of the evolution, charge from one boric acid makeup tank until depleted, then transfer to the second 8AMT.

Concurrent with continued cooldown, replenish inventory in the first tank.

These provisions, or operator actions, would need io be considered only once during core cycle, just prior to conducting a shutdown for refueling. Note that they are relatively simple a( tions that should be well within the current plant operating procedures, In addition, they can be planned for in advance so as to have no imp<st on maintenance activities or the plant refueling schedule.

3.6 SHUTDOWN TO COLO SHUTDOWN - MODE 5 As discussed in the previous Section, the shutdown to refueling is the most limiting evolution that an operator must perf( rm wi:h respect to system boration. This evolution is normally performed once during a fuel cycle just prior to refueling. Situations (s~ ch a. unscheduled plant maintenance, etc.) can occur during a fuel cycle, oweva~, arC require that an operator perfcrm a plant shutdown to cola . nu .-.c~n c"ndi tions.

Although not limiting with respect to boratior. rea;.i ro.~en:s, >t is important for an operator to be able to perform su<.n a s-u:down cuickly and efficien.ly.

3-S

'I'his section presents the evaluation results of a plant shutdown,to cold

hutdown. The analysis was performed specifically to demonst.ate the

-.ffect on makeup inventory requirements of a reduction in boric acid

torage tank concentration. A list of key parameters and conditions assumed in the analysis is contained in Table 3-11. In addition to the parameters in Table 3-11, the evaluation was performed for end-of-cycle

onditions assuming a cold shutdown concentration of 800 ppm boron. As a

, "esult, boron concentration had to be increased from zero ppm to 800 ppm

~oron. The operator scenario employed in the shutdown to cold shutdown is as follows:

I. The reactor is shutdown to hot zero power conditions via rod insertion.

2. A plant cooldown and depressurization is immediately commenced from an average coolant temperature and system pressure of 532 degrees and 2200 psia to an average coolant temperature and system pressure of 325 degrees and 268 psia. An overall cooldown rate of approximately 100 degrees per hour is assumed. Makeup inventory is supplied from the boric acid makeup tanks.

3. The shutdown cooling system is placed in operation at 325 degrees and 268 psia.

4. The plant cooldown is continued following shutdown cooling initiation from 325 degrees to 135 degrees at 268 psia. Makeup inventory is supplied from the boric acid makeup tanks.

Evaluation results showing the system concentrations as a function of time and total boric acid makeup tank inventory requirements are contained in Table 3-12 and Table 3-13. Note that two cases were analyzed for comparison for each plant. In Case I the concentration 3>>9 .

within the shutdown cooling svstem was assumed to be equal to 'he concentration of the reactor coolant sy"tern at the time of shutdown coolira initiation. In Case ! I the concen.ration within the sou .down cooling system was assumed to be eoual to the concentration of the refueling water tank at the time of shutdown coolira initiation. System boron concertration data from these two tables are plotted in Figure 3-and Figure 3-8. Concentrations during the plant cooldown were calculated using the methodology discussed in Section 2.4. Ouring those pnr.ions of the plant cooldown in which blended makeup was used, data was calculated using the methodology contained in Section 3.4.

A total volume of '.0,468.0 gallons of a 3.5 weight percent boric. acid solution were required in order to perform the shutdown to cold shutdown for the case in which the concentration o: the fluid within the shutdown cooling system was assumed to be equal to that of the reactor coolant system at the time of shutdown cooling initiation. In the case where. the concentration within the shutdown cooling system was assumed to equal that of the refueling water tank at the time o. shutdown cooling initiation, a total volume of 7471.3 gallons was required. Note -.hat approximately 2996.7 gallons less of the boric acid makup tank inventories were required to be used in the Case II cooldown. Since the plant operating procedures require that the shutdown cooling system be operated via recirculation with the refueling water tank prior to initiation, the concentration within that system will normally be very near that of the R~AT any time that the shutdown cooling svstam is placed in operation.

3.7 LONG TERM COOLING ANO CONTAINMENT SOMP pH

he impact of'he Boric Acid Reduction Effort on oost LOCA long ter~

cooling and containment sump pH control was reviewed. Each analysis is discussed qualitatively below.

3-10

Performance of the Emergency Core Cooling System (ECCS) during extended periods of time following a loss-of-coolant accident (LOCA) was analyzed in the respcnse to NRC Ouestion 6.28 contained in the appendix to Chapter 6 of the St. Lucie Unit I FSAR. Long term residual heat removal is acccmplished by continuous boil-off of fluid in the reactor vessel. As borated water is delivered to the core region via safety injection and virtually pure water escapes is steam, high levels of boric acid may accumulate in the reactor vessel. As an input to this analysis, boric acid makeup tank (BNT) boron concentration was assumed to be 12 weight percent. This calculation conservatively bounds the maximum boric acid makeup tank boron concentration of 3.5 weight X.

A detailed calculation will be performed by Florida Power and Light Company to cetermine the effects of boric acid concentration reduction on the post LO(A sump P and containment spray P . This evaluation will be H H conducted tc determine if the sodium hydroxide addition rate or total quantity in.'ected by the containment spray system needs to be changed to 0 H maintain ths sump and containment spray within the P ranges specified in the St. Lucie Unit 1 FSAR.

3-11

Table 3-1 Key Plant Parameters and Conditions Assumed in Generating the Feed-and-Bleed Curves

a. Reactor coolant system volume = 9,601 ft3 .

b. Reactor coolant system pressure = 2200 psia.

c. Reactor coolant system average temperature = 532 degrees.

d. Pressurizer volume 460 ft .

e. Pressurizer is saturated.

f. Zero reactor coolant system Technical Specification leakage.

g. Boric acid makeup tank temperature = 70 degrees.

h. Complete and instantaneous mixing between the pressurizer and the reactor coolant system.

i. Constant pressurizer level maintained during the feed-and-bleed process.

j. Letdown flowrate from one charging pump = 40 gpm.

k. Letdown flowrate from two charging pumps 84 gpm.

3-12

Table 3-2 Feed-and-Bleed Using 0>>e Charging Pwnp from an Initial RCS Concentration of 0 ppm Boron St. Lucie Nl RCS Boron Concentration (ppm boron)

BAHT at BAHT at BAHT at BAHT at BAHT at BAHT at

~Time mie 0.98 wt 9 2.50 wt X 2.75 wt X 3.00 wt X 3.25 wt X 3.50 wt C 10 12.0 30.4 33.4 36. 5 39.5 42.5 20 23.8 60.6 66.6 72. 7 78.7 84.8 30 35. 6 90. 5 99.6 108. 6 117.7 126.7 40 47. 3 120.3 132.3 144.3 156.3 168.4 50 59.0 149.8 164.8 179.8 194.8 209.7 60 70..5 179.2 197.1 215.0 232.9 250.8 70 82.0 208.3 229.1 250.0 '70.8 291.6 80 93.4 237.2 261.0 284.7 308.4 332.1 90 104. 7 266.0 292.6 319.2 345.7 372.3 100 115.9 294.5 323.9 353.4 382.8 412.3 110 127.0 322.8 355.1 387.4 419.7 451.9 120 138.1 351.0 386.1 421.2 456.3 491.3

Table 3-3 Feed-and-Bleed Using Two Charging Pumps from an Initial RCS Concentration of il ppm Boron St. Lucie 81 RCS Boron Concentration (ppm boron)

BAHT at BAHT at BAHT at BAHT at BAHT at BAHT at Time min 0.98 wt X 2.50 wt X 2.75 wt I 3.00 wt X 3.25 wt X 3.50 wt X 10 25.0 63.6 69.9 76.3 82.6 89.0 20 49.7 126.2 138.8 151.4 164.0 176.7 30 73.9 187.9 206.7 225.5 244.3 263.1 40 97.9 248.7 273.6 298.5 323.3 348.2 50 121.5 308.7 339.5 370.4 401.3 432.1 60 144.7 367.8 404.5 441.3 478.1 514.8 70 167.6 426.0 468.6 511.1 553.7 596.3 80'0 190.2 483.3 531.7 580.0 628.3 676.6 212.4 539.9 593.8 647.8 701.8. 755.8 100 234.4 595.6 655.1 714.7 774. 2 833.7 110 256.0 650.5 715.5 780.5 845. 6 910.6 120 277.2 704.6 775.0 845.4 915. 9 986.3

Table 3-4 Feed-and-Bleed Using One Cbarging Pumps from an Initial RCS Concentration of 800 ppm Boron St. Lucie Nl RCS Boron Concentration (ppm boron)

BAHT at BAH1 at BAHT at BAHT at BAHT at BAHT at Time min 0.98 wt X 2.50 wt X 2.75 wt X 3.00 wt X 3.25 wt X 3.50 wt '4 10 806.4 824.9 '827.8 830.9 833.9 836.9 20 812.7 849.5 855.5 861.6 867.6 873.7 30 819.0 873.9 883.0 892.0 901.1 910.1 40 825.3 898.3 910.3 922.3 934.3 946.4 50 831.6 922.4 937.4 952.4 967.4 982.3 60 837.7 946.4 964.3 982.2 1000.1 1018.0 70 843.9 970.2 991.0 1011.9 1032.7 1053.5 80 850.0 993.8 1017.6 1041.3 1065.0 1088.7 90 856.0 1017.3 1043.9 1070.5 1097.0 1123.6 100 862.0 1040.6 1070.0 1099.5 1128.9 1158.4 110 868.0 1063.7 1096.0 1128.3 1160.6 1192.8 120 873.9 1086.8 1121.9 1157.0 1192.1 1227.1

Table 3-5 Feed-and-Bleed Using Two Charging Pumps from an Initial RCS Concentration of 800 ppm Boron, St. Lucie 81 RCS Boron Concentration (ppm boron)

BAHT at BAHT at BAHT at BAHT at BAHT at BAHT at Time min 0.98 wt X 2.50 wt X 2.75 wt I 3.00 wt X 3.25 wt X 3.50 wt X 10 813.4 852.0 858.3 864.7 871.0 877.4 20 826.6 903.1 915.7 928.3 940.9 953.6 30 839.5 953.5 972.3 991.1 1009.9 1028.7 40 852.4 1003.2 1028.1 1053.0 1077.8 1102.7 50 865.0 1052.2 1083.0 1113.9 1144.8 1175.6 60 877.4 1100.5 1137.2 1174.0 1210.8 1247.5 70 889.6 1148.0 1190.6 1233.1 1275.8 1318.3 80 901.7 1194.8 1243.2 1291.5 1339.8 1388.1 90 913.6 1241.1 1295.0 1349.0 1403.0 1457.0 100 925.4 1286.6 1346.1 1405.7 1465.3 -1524.7 110 936.9 1331.4 1396.4 1461.4 1526.5 1591.5 120 948.2 1375.6 1446.0 1516.5 1586.9 1657.3

Table 3-6 Typical Blended Hakeup Operations at 44 gpm out of Blending Tee Concentration Out of Tee (ppm boron)

Flow (gpm) BAHT at BAHT at BAHT at BAHT at BAHT at FCV-2210Y FCV-2210X 2.50 wt X 2.75 wt X 3.00 wt X 3.25 wt X 3.50 wt I 0.5 43.5 50.9 56. 2 61.4 66.7 72.0 1.0 43.0 101.8 112.3 122.8 133.4 144.0 1.5 42.5 152.7 168.4 184.1 200.0 215.9 2.0 42.0 203.5 224.4 245.4 266.6 287.8 3.0 41. 0 305.1 336.4 367.9 399.5 431.3 4.0 40.0 406.6 448.3 490.2 532.3 574.6 5.0 39.0 507.9 560.0 612.3 664.9 717.6 6.0 38.0 609.2 671.6 734.3 797.2 860.4 7.0 37.0 710.3 783.0 856.0 929.4 1003.0 8.0 Rl 1. 3 894.3 977.6 1061.3 1145.4 9.0 35.0 912.2 1005.4 1099.1 1193.1 1287.5 10.0 34.0 1012.9 1116.4 1220.3 1324.7 1429.4 15.0 29.0 1515.0 1669.3 1824.2 1979.5 2135.4

Table 3-7 lypscai uienaeo makeup Operations ai 88 gpm out of Blending Tee Concentration Out of Tee (ppm boron)

Flow (gpm) BAHT at BAHT at BAHT at BAHT at BAHT at FCV-2210Y FCV-2210X 2.50 wt I 2.75 wt X 3.00 wt X 3.25 wt X 3.50 wt X 0.5 87.5 25.5 28.1 30.7 33.4 36.0 1.0 87.0 50.9 56.2 61.4 66.7 72.0 1.5 86.5 76.4 84.2 92.1 100.1 108.0 2.0 86.0 101.8 112.3 122.8 133.4 144.0 3.0 85.0 152.7 168.4 184.1 200.0 215.9 4.0 84.0 203.5 224.4 245.4 266.6 287.8 5.0 . 83.0 254.3 280.4 306.7 333.1 359.6 6.0 82.0 305.1 336.4 367.9 399.5 431.3 7.0 81.0 355.9 392.4 429.1 465.9 503.0 8.0 80.0 406.6 448.3 490.2 532.3 574.6 9.0 79.0 457.3 504.2 551.3 598.6 646.1 10.0 78.0 507.9 560.0 612.3 664.9 717.6 15.0 73.0 760.8 838.7 916.9 995.4 1074.2

Table 3-8 Typical Blended Makeup Operations at 132 gpm out of Blending Tee Concentration Out of Tee (ppm boron)

Flow (gpm) BANT at BAHT at BANT at BAMT at BAMT at .

FCV-2210Y FCV-2210X 2.50 wt X 2.75 wt X 3.00 wt X 3.25 wt X 3.50 wt X 0.5 131.5 17.0 18.7 20.5 22.2 24.0 1.0 131.0 34.0 37.4 41.0 44.5 48.0 2.0 130.0 67.9 74.9 81.9 88.9 96.0 3.0 129.0 101.8 112.3 122.8 133.4 144.0 4.0 128.0 135.7 149.7 163.7 177.8 191. 9 5.0 127.0 169.6 187.1 204.6 222.2 239.9 6.0 126.0 203.5 224.4 245.4 266.6 287.8 7.0 125.0 237.4 261.8 286.3 310.9 335.6 8;0 124.0 271.3 299.1 327.1 355.2 383.5 9.0. 123.0 305.1 336.4 367.9 399.5 431. 3 10.0 122.0 339.0 373.7 408. 6 443.8 479.1 15.0 117.0 507.9 560.0 612.3 664.9 717.6

~ .

Table 3-9 Key Plant Parameters and Conditions Assumed in the Shutdown to Refueling Evaluation

a. Reactor coolant system volume = 9,601 ft3 .

b. Initial RCS average loop temperature = 532 degrees.

c. Pressurizer volume = 460 ft .

d. Pressurizer is satruated.

e. Zero reactcr coolant system leakage.

f. Boric acid makeup tank temperature = 70 degrees.

g. Complete ard instantaneous mixing between the pressurizer and the reactor coc lant system.

h. Constant pressurizer'level maintained during the feed-and-bleed process.

i. Initial RC! concentration = 0 ppm boron.

j. BANT concer tration = 3.50 weight percent boric acid.

k. RMT concento.ration 1720 ppm boron.

Shutdown cr oling system volume = 3000 ft .

m. Boron concentration in the shutdown cooling system is equal to the boron concentration in the RCS at the time of shutdown cooling initiation.

Refueling concentration, Node 6 = 1720 ppm.

3-20

Table 3-10 Evaluation Results for Plant Shutdown tn Refueling Temp Pressure Concentration Total RABAT de rees) ( sia) ( m boron) Vc 1 ume al 532 2200 0 0 532 2200 135. 1 1,280 532 2200 267.2 2,560 532 2200 396.3 3,840 532* 2200 522.7 5,120 500 2200 724.2 7,193.5 450 2200 975.6 10,007.)

400 2200 1173.5 12,424.1 350 2200 1336.7 14,567.4 3250 268 1350 15,'865 9 325 268 1350 15,865.9 300 268 1418.3 17,116.1 250 268 1538.9 19,413.7 200 268 1638.1 21,396.1 150 268 1715.8 23,012.7 135 268 1736.0 23,440.1

~ Cooldown stopped for one hour for shutdown coolirg svstem alignment.

3-21

Table 3-11 Key Plant Parameters and Conditions Assumed in the Shutdown to Refueling Evaluation

a. Reactor coolant system volume = 9,601 ft3 .

b. Initial RCS average loop temperature = 532 degrees.

c. Pressurizer volume = 460 ft .

d. Pressurizer is saturated.

e. Zero reactor coolant system leakage.

f. Boric acid makeup tank temperature = 70 degrees.

Oemineralized water supply temperature = 70 degrees.

g.

h. Complete and instantaneous mixing between the pressurizer and the reactor coolant system.

i. Constant pressurizer level maintained during the plant cooldown.

j. Initial RCS concentration = 0 ppm boron.

k. BANT concentration = 3.50 weight percent boric acid.

l. RWT concentration = 1720 ppm boron.

Shutdown cooling sys tern volume = 3000 ft .

n. Boron concentration in the shutdown cooling system is equal to the boron concentration in the RCS at the time of shutdown cooling initiation for Case I.

0. Boron concentration in the shutdown cooling system is equal to the boron concentration in the RWT at the time of shutdown cooling initiation for Case II.

3~22

Table 3-12 Case I Evaluation Results for Plant Shutdown to Cold Shutdown with SDCS Concentration Equal to R".S Concentration at the Time of Shutdown Cooling Initiation Temp Blending Pressure Concentration Total BAMT de rees Ratio *) sia m boron Volume al) 532 2200 0 0 500 2200 221.0 2,073.5 450 2200 496.6 4,887.1 400 2200 713.5 7,304.1 350 0.85:1 2200 799.8 8,462.7 325 1.51:1 268 800.0 9,508.1 3254 268 800.0 9,508.1 300 6.9 :1 268 800.0 9,666.3 250 6.89:1 268 800.0 9,957.5 200 6.89:1 268 800.0 10,208.8 150 6.89:1 268 800.0 10,413.7 135 6.87:1 268 800.0 100468.0 0 After T <<b1 shutdown cooling system alignment.

3-23

Table 3-13 Case I Evaluation Results for Plant Shutdown to Cold Shutdown with SDCS Concentration Equal to RMT Concentration at the Time of Shutdown Cooling Initiation Temp Blending Pressure Concentration Total BAMT de rees) Ratio *) sia) ( m boron) Volume ( al) 532 2200 0 0 500 2200 221.0 2,073.5 450, 2200 496.6 4,887.1 400 4.24:1 2200 523.0 5,348.3 350 11.1:1 2200 523.0 5,525.5 325 2.88:1 268 523.1 6,511.8 3258 268 800.0 6,511.8 300 6.9 :1 268 800.0 6,670.0 250 6.9 :1 268 800.0 6,960.8 200 6.89:1 268 800.0 7,212.1 150 6.89:1 268 800.0 7,417.0 135 6.87:1 268 800.0 7,471.3 A

8 After shutdown cooling system is aligned and circulated.

3-24

FIGURE 3 1 ST.LUCIE 1 FEED AND BLEED FROM HOT ZERO POSER FROM 0 PPM BORON 0.9 T

Z 0.8 0

K Om 07 E

0.6

~ Il Z C Oaa p.5

.~

4Z~

4J pg o

Z o 0 o

K 0.2 01 ~

= 0 0

20 60 80 100 120 TIME ( minutes )

0 40-1720 + 40-3.0 O 80 30 80-3.5 GiW- IiVN GPH-HT'L GPH-C'i GPI4-WT'i

FIGURE 3 2 ST.LUCIE 1 FEED ANDBLEED FROM HOT ZERO POWER FROM 800 PPM BORON 1.7 1.6 1.5 0

'IL' I 1.4 E

zc 13 p 0 Q f2 Z~

1.2 4J 0

1.1 0

U) 0 K

0.9 0.8 20 40 60 80 100 120 TlME (minutes) 0 40-1720 + 40-3.0 0 80-3.0 80-3.5 gpll-ppA gpm-wt% g pn-wt'L gpm-wt4

FIGURE 3 3 BLENDED MAKEUP OPERATIONS AT 44 GPM OUT OF BLENDING TEE 1.4 1.3 1.2 E

a. 1 0.9 Om z co 0.8 Q 0 I- 0 0.7 I-0.6 5

0.5 0

0.4 0.3 0.2 0.1 FLOW AT FCY-2210Y (gpm)

Q AALLT hT AhllT AT;% A ...pa O RAklT AT A.5 e..e.a

FIGURE 3 4 BLENDED MAKEUP OPERATIONS AT 88 GPM OUT OF BLENDING TEE 800 700 600 E

Q.

500 0

Z o . 400 300 O

Z 0

O 200 100 FLOW AT FCV2210Y (gpm) 0 BAMT AT 2 5 wta + BAMT AT 3.0wta . BAMT AT 3.5wtw

FIGURE 3 5 BLENDED MAKEUP OPERATIONS AT 132 GPM OUT OF BLENDING TEE 500 400 E

300 0

z 0

200 0

z 0

O 100 FLOW AT FCV-2210Y (gpm) 0 BAMT AT 2.5 wtt + BAMT AT 3.0 wt% 0 BAMT AT 3.5wta

FIGURE 3 6 ST.LUCIE 1 RCS BORON CONC vs TEMP FOR REFUELING SHUTDOWN 1.8 1;7 1.6 1.5 0 lA 0 1.3 1.2 E

1.1 O a no 0.8 0.7 0

0.6 0

0.5 Ul 0.4 0.3 0.2 0.1 450 350 250 150 TEMPERATURE (F) 0

FIGURE 3 7 ST.LUCIE 1 RCS BORON CONC vs TEMP FOR REFUELING SHUTDOWN 900 aoO Z 700 0

600 E

500 400 O

Z 300 0

O 200 100 550 450 350 250 150 TEMr aVTURE (Q

FlGURE 3 8 ST.LUCIE 1 RCS BORON CONG vs TEMP fOR REFUELING SHUTDOWN 900 800 z 700 0

K I

0 600 E

Z 500 0

400 O

z 300 0

O O 200 K

100 550 450 350 250 150 TEMPERATURE (F)

4.0 REFERENCES

4. 1 Technical Oata Sheet IC-11, US Borax II Chemical Corporation, 3-83-J.W.

4.2 Combustion Engineering's Emergency Procedure Guidelines, CEN-152, Revision 2, Hay, 1984.

4.3 An Evaluation on the Natural Circulation Cooldown Test Performed at the San Onofre Nuclear Generating Station, compliance with the Testing Requirements of Branch Technical Position RSB 5-1, CEN-259, Combustion Engineering, January 1984.

4.4 U.S. Nuclear Regulatory Commission Standard Review Plan NUREG-0800 Section 5.4.7. "Residual Heat Removal (RHR) System" and Branch Technical Position (RSB) 5-1 "Oesign Requirements of the Residual Heat Removal System".

Appendix of the Reactor Coolant

'erivation System Feed-and-Bleed Equation Pur ose of Definitions This appendix presents the detailed derivation of an equation which can be used to compute the reactor coolant system (RCS) boron concentration change during a feed-and-bleed operation. For this derivat.ion, the following definitions were used:

miin

= mass flowrate into the RCS mooutt ma s s f 1 ow t ra e o u t o f th e RCS mb boron mass flowrate w = water mass flowrate

= boron mass mb

= water mass Cin

= boron concentration going into RCS boron concentrati on go i ng out ofRCS Gout C ~ initial boron concentration C(t) boron concentration as a function of time

= RCS boron concentration CRCS Sim lif in Assum tions During a feed-and-bl ed operation, the reactor IQ coolant system can be pictured as shown in the figure out C

as a closed container having a certain volume, a C out 0 certain mass, and an ini.tial boron concentration.

Coolant is added at one end via the charging pumps.

RCS The rate of addition is dependent on the number of charging pumps that are running with the lof 5

concentration being determined by the operator. Coolant is removed at the other end via letdown at a rate that is approximately equal to the charging rate and at a concentration determined by fluid mixing within the reactor coolant system. The mass flowrate into the reactor coolant system is given by the following equation:

(I m).

For typical boron, concentrations within the chemical and volume control system, q is very much greater than mb. (For example, a 3.5 weight percent boric acid solution contains only 0.04 ibm of boric acid per ibm of water). Therefore the above equation can be simplified to the fol owir g:

1

)

In a siriilar manner, the mass flowrate coming out of the reactor coolant system, given by out b w out'ar be . implified by again realizing that m is very much greater than mb or out w out'2.0)

For a feed-and-bleed operation with a constant pressurizer level and a constan-. system temperature, the mass flowrate into the RCS will be equal to the repass flowrate out of the RCS, or =

in out w in w .

out'of 5

Finally, if it is assumed that the boron which is added to the reactor coolant system mixes completely and instantly with the entire RCS mass, the concentration of the fluid coming out of the system will be eoual to RCS'C.o) the system concentration, or out =

Oerivation The rate of change of boron mass within the reactor coolant system is equal to the mass of boron being charged into the system minus the mass of boron leaving via letdown. In equation form, this becomes b RCS ~ in in out out'e From Equation 3.0, b RCS ~ in in oui w in in out '5.0)

The concentration of boron in the reactor coolant system, i.e,. the weight fraction of boron, is defined as follows:

RCS ~

b w RCS Since m))m>,

m RCS =

w RCS 3of5

Where (m ) is a constant for a constant system temperature. The rate of w RCS chance of the RCS concentr>tion is therefore I> RCS IICS (6.0)

~pcs Substituting Equation 5.0 into Equation 6.0 yields the following:

RCS = w in in out and from Equation 4.0, RCS = w in in RCS (7.0)

Solving Equation 7.0 for concentration yields:

RCS w in dt, I>> RCS ~wRCS or c(t)

(th w)

RCS in dt .

I>> 'RCS w RC C

Integrating from some initial concentration C to some final concentration C(t) and multiplying through by a minus one gives the following:

c(t)

( RCS IN) = - ( w)in t, (m

3 RCS C

or 4of5

,. C(t) - C,.n (e ~

in t.

o in Continuing to solve for C(t), this equation becomes:

-(--win

) t/ ( )

wRCS, Ct -Cii e o in or

-(0 ). in t/ (m w)

RCS

= p- ( o)

( ) ; ( in) ~

If we define the time constant T to be as follows:

T

w RCS

~mn then Equation 8.0 becomes

/ - /

C(t) C 0

e + C in (I e ) .

5of 5

Aopendix 2 A Proof that Final Svstem Concentration is Independent of System 'lolume Pur ose of Definitions This appendix presents a detailed proof that during a plant ccoldown where an operator is charging only as necessary to makeup for coolant contraction, the final svstem concentra.ion that results using a given boration source concentration will be independent of the total system volume. For this proof, the following definitions were used:

ci = initial boron concentration Plant i mb. = initial boron mass Plant 1 m,wi initial water mass Plant 1 cf ~ final boron concentration Plant 1 c ~ boron concentration of n akeup solution Plant 1 mb

= mass of boron added Plant 1 m

wa mass of water added Plant 1 mbf

= final boror. mass Plant 1 Ci initial boron concentrat.'or. Plant 2 Hbi initial boron mass Plant 2

= ini .ial water mass Plant 2 wi Cf ~ final boron concentration Plant 2 C ~ boron concentration of rrakeup solution Plant 2 Nb mass of boron added Plart ".

Y.

'wa

~ mass of water added Plart 2 Proof For this proof, consider two plants at the same initial temperature, the same initial pressure, and the same initial boron concentration. O..e plart, Plant 2, has exactly twice the system volume as the other plant,

Plant 1. Initially, boron concentration Plant 1 = boron concentration Plant 2, or m

bi bf' wl

=

Mbl ' bi wi (1.0)

Since the volume of Plant 2 is twice that of Plant 1, Mwi = 2mi Substituting this relationship into Equation 1.0 and solving yields the following:

bi bf 'wf bi wi bf'bf + mbf"lwf biMbi 'wf'bf and t tbi 2mbf (2.0)

Therefore, the initfal boron mass in Plant 2 is exactly twice the initial boron mass fn Plant 1.

Ourfng the cooldown process for Plant 1, the final boron mass in the system will equal the initial boron mass plus the added boron mass, or mbf mbf m b

0 (3.0)

If, during this cooldown process, operators charge only as necessary to makeup for coolant contraction, water and boron will be added only as space is made available in the system due to coolant shrinkage. The final boron concentration from Equation 3.0 can therefore be expressed as follows:

m bf bf ba 'wf wa bf Ill + Ill + m + Ill b b i 2of4

If concentrat:on is expressed in terms of weight percent, this last equation becomes mbf mb mb N i

+ mcf (4.0)

Similarly, the remaining two components of Equation 3.0 become Nbi

=

illbi + m C. (5.0) and ba ba wa a (6.0)

Substituting Equations 4.0, 5.0, and 6.0 into Equation 3.0 and solving for the final concentration yields the following:

Cf Ill + m + + c i ~

Ci m a (7.0) mbi 'b + lll i+ lll For Plant 2, Equation 7.0 becomes

+ N Ci + + H

'i Cf N . M C i (8.0) bi ba wa Ouring a cooldown, the shrinkage mass, i.e., ths mass of fluid that must be added to the system in order to keep pressurizer level constant, is calculated by dividing the system volume by the change in specific volume, or m System Volume Plant 1 (g.o) and M System Volume Plant 2 (10.0) peer sc vo ume where System Volume Plant 1 = (1/2) System Volume Plant 2.

3of4

For a given cooldown, dividing Equation 9.0 by Equation 10.0 gives following:

wa 2m wa (11.0)

In addition, if the charging source for both plants is at the same concentration and temperature, Ca ca and

= (13.0)

Hb 2mb Substituting Equations 2.0, 11.0, 12,0, and 13.0 into Equation 8.0 yields the following:

Cf 2m>> + H Ci + 2mba ca bi ba wi wa Since the initial concentrations are the same, Ci ~ ci, and since Plant 2 is twice as large as Plant 1, Mi 2mi, C< L2m><

+ 2g q

+ Q2 + 2

~ c<

bi ba Ni Na Cf cf Therefore, for a cooldown where pressurizer level is maintained constant, the final boron concentration for Plant 2 is equal to the final boron concentration for Plant 1, i.e., the change in boron concentration is independent of the exact system volume.

4of4

0 Appendix 3 Methodology for Calculating Cissolved Boric Acid per Gallon of Mater

~Pur oee The purpose of this appendix is to show the methodology used -.o calculate the mass of boric acid dissolved in each gallon of water for "olutions of various boric acid concentrations. Two solution temperatures were used corresponding to the minimum allowable refueling water tank temperature of 50 degrees and a boric acid makeup temperature of 70 degrees in the absence of tank heaters.

Methodolo and Results Boric acid concentration expressed in terms of weight percent 'is defined as follows:

C mass of boric acid x 100 tota so utson mass or mass of boric acid x 100.

mass o or c ac1 + mass o water If we define mb to be the mass of boric acid and mw to oe the mass of water, and if we substitute these defined terms into Equation 1.0 and solve for the mass of boric acid we have the following:

ba x 100, ba w or C x m ba 100 - C lof2

From Appendix A of the Crane Company Manual (Flow of Fluids Through Valves, Fittings, and Pipe, Crane Co., 1981, Technical Paper No. 410),

the density of water at 70 degrees is 8.3290 ibm / gallon and at 50 degrees is 8.343 ibm / gallon. Using these water masses and Equation 2.0 above, the mass of boric acid per gallon of solution is as follows:

Mass of acid per gallon Concentration of solution at source wt. X boric acid m boron 50 de rees 70 de rees RWT 0.98379 1720 0.08289 ibm RWT 1.05815 1850 0.08923 ibm RWT 1.14394 2000 0.09654 ibm RWT 1.22974 2150 0.10387 1 bm 1.31553 2300 0.11121 ibm BAMT .2.25 3934 0.19172 ibm BAMT 2.50 4371 0.21356 ibm BAMT 2.75 4808 0.23552 ibm BAMT 3.00 5245 0.25760 ibm BAMT 3.25 5682 0.27979 ibm BAMT 3.50 6119 0.30209 ibm 2of2

Appendix 4 Methodology for Calculating the Conversion Factor Between Weight Percent Boric Acid and ppm Boron

~Pur ose The purpose of this appendix is to show the methodology used to derive the conversion factor between concentration in terms of weight percent boric acid and concentration in terms of parts per million (ppm) of naturally occurring boron.

Results For any species (solute) dissolved in some solvent, a.solution having a concentration of exactly 1 ppm can be obtained by dissolvinq 1 ibm of solute in 999,999 ibm of solvent. An aqueous solution having a concentration of 1 ppm boric acid, therefore, can be obtained by dissolving 1 ibm of boric acid in 999,999 ibm of water, or 1 ppm 1 ibm boric acid 1 ibm boric acid 1 ibm boric acid + 999,999 ibm water 10 ibm solution For any species (solute) dissolved in some solvent, a solution having a concentration of 1 weight percent (wt. ) can be obtained by dissolving 1 ibm of solute in 99 ibm of solvent. An aqueous solution'having a concentration of 1 wt. X boric acid, therefore, can be obtained by dissolving 1 ibm of boric acid in 99 ibm of water, or 1 wt. X 1 ibm boric acid , 1 ibm boric acid 111 ~ + ~

4 Dividing these last two equations yields a ratio of 10, or 1 wt. boric acid = 10,000 ppm boric acid. (1.0) lof 2

To convert from ppm boric acid (weight fraction) to ppm boron (weight fraction), multiply Equation 1.0 by the ratio of the molecular weight of boric acid (naturally occurring H3B03) to the atomic weight of naturally occurring boron. From ::he Handbook of Chemistry and Physics, CRC Press, 1 wt. X boric acid =

( 10,000)

~$ 'pm boron ,

1 wt. ~ boric acid = 1748.34 ppm boron.

2of 2

Appendix 5 Bounding Physics Data Inputs The following Phvsics Data Inputs for St. Lucie Unit are provided to 1

facilitate review of .his effort. The conservatisms, uncertainties, and biases incorporated in the BAMT Boric Acid Concentration Reduction effort =or St. Lucie Unit are contained in Table 1. The St. Lucie Unit EOC Phys.'cs 1 1 Data Irputs are contained in Table 2 and Ficures 1 through 8. Durinq uture cycles, the new core parameters must be compared with these inputs to ensure that they are still bounding.

The ourpose of this section is to describe the methodology used to compute the core reac:ivity during the cooldown. This method has been devised to conservatively bound the reactivity affects of the natural circulation cooldown described in Section 2'.2. l. 1 of this report. The cooldown scenario and the method used to compute core reactivity are discussed in detail in the following paragraphs.

A descriptior. of the core reactivity affects is provided. Ip addition a brief description is provided to show tha. these assumptions conservative'. i bound all similar cooldowns at any time during the fuel cycle.

I. Conservative core physics parameters were used to determ'.ne the required boron concentration and the required Boric Acid Makeup Tank volumes to be added during plant cooldown.

End-of-cycle (EOC) initial boron concentration is assumed to be zero.

End-of-cycle moderator cooldown effects are used to maximize the react~vity changes during plant cooldown.'

of 16

Positive reactivity is added tn the ccrc as the moderator temperature is lowered during the cooldcwn. The moderator temperature effects or, core reactivity vary over the fuel cycle. The moderator temperature ef ect at beginning-of-cycle (BOC) is very small while the moderator temperature effec. EOC provides the maximum reactivi y insertion. Figure 1 of this appendix was used.

Beginning-of-Cycle boron reactivitv worths are used to maximize the amount o boron that must be added to provide the required reactivity change.

BOC Integral Boron Wor+hs (Table 3) were determined by comparinq the data on Figure 5 with similar data for other cores. The data in Table 3 will conservatively . equire a greater increase in ppm boron for a given change in reactivity. This table will bound (exceed) +he IBW requirements for the remainder of the cycle.

2. Scram Worth A conservative scram worth was used i this calculation. The available scram worth was computed utilizing th: hot zero power scram worth for all rods in minus the worst rod stucl; full out (Table 2}. From this value the Power Oependent Insertion Limit w)rths (Table 2) were subtracted tc obtain a ne. available scram worth. .h combined Bias and Uncertainty of 10".. was sub+racted from the avai'.able scram worth for added conservatism.

This scram worth is further reduced bg subtracting an EOC reactivity value associated with the Full Power .'efect (from Figure 7).

2of 16

3. Oetermiration of Excess Scram North Excess scram wnr+h was determined bv comparing the available scram worth at zero power and subtracting the required technical specification shutdown margin. Required Shutdown i~argin:

SON ave

> 200'F > 3.6~ dk/k

< 200'F > 2.05 hk/k It was determined by this method that there was a 0.04 Lk/k excess scram worth available for temperatures above 200'F and an excess scram worth of 1.64 ak/k or temperatures below 200'F.

4. Core Reactivity Effects A reactivity calculation has been per:ormed to account for posit'.ve reactivity insertion due to the decay of xenon and the positive reactivity due to the cooldown of the moderator and fuel. Uncertainties and biases were applied to all reactivitv a,fects. Table 1 delinea.es the biases and uncerta;nties used in this calculation.

Xenon Reactivity Effects As shown in Figure 4 cf the xenon worth peaks a+ its most negative reactivity worth arcund eight hours after the reactor is shu+down. Ãencn decav reduces the negat:ve reactivitv nf the xenon back .o .'ts steady state operating value at approximately 26 hours3.009259e-4 days 0.00722 hours 4.298942e-5 weeks 9.893e-6 months a,ter shutdown. At times after 26 hours3.009259e-4 days 0.00722 hours 4.298942e-5 weeks 9.893e-6 months the plant must be borated to compensate for the further reduc.ion in xenon concentration. As an added conservatism +his .

calcula+ion never credited the extra neoative reac+ivi+y inserted by the xenon peak that occurs after shutdown. Instead the plant was maintained at hot standby for 26 hours3.009259e-4 days 0.00722 hours 4.298942e-5 weeks 9.893e-6 months .o allow xercn to return .o the 100% steady 3 of 16

state value and further xenon decay to add reactiv iy simultaneously with the plant cooldown effects. Figure 3 was used to determine the positive reactivity inserted into the core for times after l'.6 hours6.944444e-5 days 0.00167 hours 9.920635e-6 weeks 2.283e-6 months at discreet time intervals. Note that a slow cooldown rate wi 1 prolong the timi recuired to reach Yode 5 where the shutdown margin drops from 3.6 ak/k to 2.0 t.k/k and therefore would require a larger borori concentration to counteract xenon decay during the cooldown. A 12.!i degree per hour cooldown rate has been utilized in this calculation. It should be no .ed that this method accounts for xenor. decay for a fu 1 54 hours6.25e-4 days 0.015 hours 8.928571e-5 weeks 2.0547e-5 months which is a much longer time frame than is expec+ed to achieve cold shutdown.

Reactor Cooldown Ef ects The affect of the reactor cooldown was calculated l>y determining the fuel temperature and moderator temperature reactivity e 'fects for each incremental temperature decrease. Figures I and ? were utilized ?o determine these effects. It should be noted that ".hese reactivity effects are independent of time anC solely denende it on the change in temperature of the core.

Boration Requirements Having determined the reactivity effects due ~o xe ion, moderator cooldown and fuel temperature cooldown for discreet time in:ervals after the plant is shutdown, the necessary boron concentration to :ompensate for this reactivity change is determined. The Integral Bor~n North values of Table 3 were used to determine the ppm boron recessary in the PCS'to compensate for the positive ",eac+ivities determine9 above. All the conservatisms, uncertainties and biases applied to this calcula+ion are included ir. Table J.

4of '6

Table Uncertainties and Biases

'onservatisms, Incorpnrated in the BAl4T Boric Acid Concen ration Reduction E ort for St. Lucie Unit 1 The initial scram is assumed to proceed from the hot full power PDIL (power dependent insertion limit) to the all rods in, with the worst case rod stuck in the fu'.1 out position conditions.

2. A bias and uncertainty of -10>> was applied to the scram worth data.

3. A conservative correction was applied to the St. Lucie Unit 1 moderator cooldown data to adjust the cooldown curve to the Technical Specification i~'TC of -2.8 x 10 ap/'F.

4. A combined bias and uncertainty of 1:3>> was applied to the moderator data for Unit 2 and to the corrected moderator data.

5. A bias of 15>> and an uncertainty of 15% was applied to the Ooppler data.

6. The assumption that the cooldown beains at 26 hours3.009259e-4 days 0.00722 hours 4.298942e-5 weeks 9.893e-6 months is conservative in relation to the buildup and decay of Xenon.

5of 16

Table 2 St. Lucie Unit 1 EOC Physics Cata*

Required Shutdown Yargin:

Tavg SDM

> 200'F > 3.6 >> 6 k/k

< 200'F > ?.0 , a k/k The moderator cooldown curve from HFP to 68'F with al', rods orat is presented in Figure 1. The moderator reactivity is given here a~ a function of the normalized water densitv for a iNTC of -2.5 X 10 delta q/'F. CE will applv a conservative correction to the moderatcr cooldown curve to make it in agreement ~ith the most neoative technical specification NTC of -2.8X10 aq/'F.

The Doppler Curve is shown in Figure 2.

Xenon Worth versus time after shutdown from 100" power is shorn in Figures 3 and 4 for cycles 6 and 7, respectively.

Scram Worths for the ARI/WRSO condition:

HZP 7214 pcm HFP 8280 pcm HZP and CZP Differen+ial Boron Horths are shown in Figures 5 end 6 for cycles 6 and 1,, respectively.

Power Defects for ARO conditions for cycles 6 and 7 are shown in Figures 7 and 0, respec+ively.

The value of 8-e f used in the moderation cooldown reactivitycurve is 0.0049.

Power Dependent Insertion Limit PDIL) worths in pcm for St. Lucie Unit l.

PDIL Position EOC 6 EOC 7 HZP Gr. 6 8 55" 1426 1288 HFP Gr. 7 9 103" 167 '200 The value of 8-eff used in the Doppler curve is 0.0049.

The combined bias and uncertainty for scram wor+hs '.s -10~.

Items 11 and 12 were transmitted to CE informally through telephone conversations.

6of 16

Table 3 Integral Ooron t4orth TEMP IBM 55?.0 85.5 544.5 85.5 532.0 es.s 507.0 84.3 482.0 83.1 457.0 81.7 432.0 80.3 407.0 79.0 382.0 77.7 357.0 76.5 332.0 75.4 307.0 . 74.4 282.0 73.5 257.0 72.8 232.0 72.1 219.5 71.8 207.0 71.5 200.0 71.4 200.0 71.4 200.0 71.4 130.0 70.2 7cf 16

Table 4 Required Boron Concentration <or a Cooldown from 557of to 130of Tempera .ures Concentration (Degrees F) (ppm borcn) 557 -75.4 510 110.9 490 181.4 480 216.5 470 2<5.0 460 272.6 450 300.3 440 328.5 430 356.1 420 383.9 410 412.2 400 437.3 390 460.6 380 484.0 370 507.3 360 533.0 350 551.3 340 567.0 330 582.6 325 591.5 310 618.5 300 635.9 260 700.1 235 735.5 210 769.4 200 782.2 199.9* 667.9 199.9** 702.2 190 712.8 180 723.5 170 734.1 160 744.8 150 755.4 140 766.1 135 771.4 130 776.7

After shutdown margin charge from 3 .6S delta k/k to 2.0'f. delta k/k

- The boration reou',rement for a 2.0,. shutdown margin and core is xenon ,ree 8 o

10 L

0 0

Q I

Ll W

lK 0

ILIN 0.95 1.IN 1.05 1.10 1 15 1 20 1 251 Rl 1.35 1.4l NNHALI7EO HOOERATOR DENSITY Figure l Hoderator Reactivity vs. IIorealized iioderator Oensity, %P

RM 4$ OQ $ 00 lSXI l2M 140 INN lN 2$ N F90 FLAIL TENPERATlNK. dag f Figure 2 Doppler Reactivity vs. Fuel Taaperature, Model I, %P

I

)I s rl. II ltl ,I'!,si ls I

I

~~~~

III s)I ls Peak Xenon Morth

, 'll.

I sl ssl I

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s

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Ir ~ . II' i.,ss .I s.ii "I 100 5,57l 8.5 i ilss I ~

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I lO 20 30 40 50 60 70 Tiara After Shutdown (Hours) figure 3 St. lucie Unit 1 Cycle 6. Xenon orth versus Time After Shutdown, ll,300 E<PH

Rl 40 50 I0 70 80 Yfao Aftor Shutdown (Ho~)

Figure 4 St. lucie Unit l, Cyc)e 7 ~ xenpu North versus Tiie After Shut~, 9,8OO fFi'H

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00 200 300 400 Itodcrator lecF<cratsrc g F)

F jgwe 5 St. tucje tjlljt 1 CKlc C. DIFFcrcattal Ioroa ICIrtiI versus fcepcratwc. 11,3 KFHI, Ml-1~ So Rcaoo

110 13 0 L1L 0 1io 0

~ ILD LO 0 1 RN RS 4$ RO 5 lb'~ Teap~tare lR F)gure 6 St. Lucite Un)t I, Cycle 7, 0<fferentfal Soron North versus Temperature, ARI-l, No Xenon, 9,800 EFPH 14 of 16

Toto) Parer 0eFect 0- lan Pwr ffPH ~ t C 200 1,6I9 6,000 1,87I 12,075 2,353 1600 1200 I00 0

50 75 0

Parer (X)

Figure 7 St. lucie limit 1 Cycle 6, P~r Defect

50 I'asar Cll)

Figure 8 St. lucie Unit 1. Cycle ? ~ Pmeer pefect versus Percent Pomr

NRC COMPLIANCE BULLETIN.87-02 Page One ITEM I Describe a) the characteristics currently examined during receipt inspection of fasteners (i.e., head markings for grade and manufacturer symbols, review of certified material test report or certificate, of conformance), and b) internal controls utilized during storage and issuance from stock to assure the appropriate use of fasteners.

RESPONSE la I

Fastener characteristics examined during receipt at the St. Lucie Plant are dependent on two criteria:

J

1. The quality level I Il
2. The specific characteristics specified in applicable procurement documents.
Only those items designated as QL-l, QL-2 or QL-3 are receipt inspected by Quality Control personnel. Quality Control receipt inspections are not performed on items procured as NOT QL-l, 2 or 3. (See Attachment 3 for definitions of the quality levels.) NOT QL-1, 2 or 3 fasteners are inspected, by Stores personnel during receipt for compliance to,P.O. requirements, damage, and cleanliness.
For QL-1, 2 6 3 items, characteristics examined during the receipt inspections are dependent on the requirements specified by the purchase order. Specifications imposed on the vendor through use of special quality assurance documents (SQAD's), Quality Control Notices (QCN's), and other purchase order requirements are verified by Quality Control on receipt of the material. For any particular item procured, any number of QCN's and other requirements may be invoked and verified when the material is received. In addition to the P.O. requirements, a visual inspection is performed for cleanliness, damage; markings, and packaging.
(A copy of our SQAD's have been included (Attachment 4) for your review.)
RESPONSE Ib Internal control on issuance of fasteners fs maintained by our procurement method and use of individual Material and Supply (MGS) numbers. At PSL, a majority of safety related fasteners are ordered directly from the vendor or supplier which manufactured or supplied the component on which the fasteners are used.
(This includes most valves, pumps, RCS components, etc.) Bach of the fasteners ordered in this manner, and are Stores items, are assigned an MGS number.
When a part is required, the MGS number is determined for that specific piece of gear, and the part is drawn from Stores under that number. By drawing stock in this- manner, assurance is maintained that the correct stock is being used for the correct application. Additionally, QL-1 and QL-2 fasteners are tagged.
with Quality Identification Tags which list the Purchase Order Number, MGS number, Receiving Inspection Required Number, Quality Level and Environmental Qualification as applicable. Generally, the ordering information for the original order and MGS specifications came directly from the manufacturer's drawing and parts numbers.
NRC COMPLIANCB BULLBTIN87-02 Page Two Por those safety related fasteners in Stores which were not ordered for a specific component, (i.e., structural), usage would be specified on a specific Plant'Work Order, Plant change or modification package, design documents or other Plant instructions.
1 ITBMS 2, 3, 4 Ez 5 Select a minimum sample of ten (10) non-safety related fasteners (studs, bolts, and/or cap screws), and ten (10) safety-related fasteners (studs, bolts, and/or cap screws) from current, in use, stock. The sample is to be obtained by the licensee with the participation of an NRC inspector. Pasteners procured to, meet the following chemical and mechanical properties are of interest: A-193.
grades 87, 88, and 816; SAE J429 grades 5 and 8; A-449; A-325 Types 1, 2, or 3; A-354 grades BB, BC, BD; A-490; A-320 LTM; A-307; A-563; or equivalent.
Por the selected sample of fasteners in Item 2, include a sample of typical nuts that would be used with each fastener (one-for-one). In particular, nuts purchased to the chemical and mechanicai.specifications of A-194 are of interest.
I Chemical testing shall be performed on all samples. Mechanical testing shall be performed on each safety-related fastener. Hardness testing shall be performed on each nut and non-safety related fastener. All testing shall be performed by a laboratory which the licensee has qualified for this type of testing and appears on the licensee's approved vendor list. Testing performed shall be done in accordance with the requirements of the fastener's specification, grade, and class, and the test shall evaluate the ultimate tensile strength, hardness and chemical properties as required by the fastener's specification, grade and class. Bach sample shall be tagged with the sample's ID number.
The results of all tests, together with supporting information, are to be reported to the NRC utilizing the format shown in Attachments 1 and 2 of this bulletin.
Include the names and addresses of suppliers and manufacturers of safety-related fasteners and, to the extent possible, of non-safety-related fasteners. Por any fastener'ound out of specification, provide an evaluation of the safety significance including consideration of the most limiting application.
NRC COMPLIANCE BULLETIN87-02 Page Three RESPONSE TO ITEMS 2, 3, 4, 6 5 Attachments 1 6 2 contain the information requested in Items 2, 3, 4 6 5 of the subject bulletin. The following notes apply to the information provided by the St. Lucie Plant:
I. The words "various manufacturers" or "various" will appear on some Attachment I forms. When this occurs, it,indicates that the fastener was purchased on the open market. Parts bin mixing occurs for the particular fastener and formal tracing of manufacturer is not possible. This condition exists only for non-class non-safety-related fasteners. These fasteners are not subject to a Quality Control receipt inspection.
2. For QA requirement definitions, see Attachment 4.
3. Por Quality Level definitions, see Attachment 3.
4. Some duplication of ID numbers occurs. This happens when identical type and size nuts were sent for testing to meet the "one to one" requirement of the bulletin. (Different type bolts using identical nuts.)
5. For the three safety related fasteners that did not meet specifications, engineering evaluations are supplied as Attachment 5. The ID¹ for the fastners were 028-25277-2-PSL, 030-61820-7-PSL, and 030-92120-1-PS L.
One of the safety related fastners was not indicated as out of specification on the . testing vendors report. However, the hardness for ID¹ 030-92120-1-PSL was determined to be out of specification by PPL.
6. Pasteners, which are not used in safety applications and did not pass the testing, were only marginally out of specification with the exception of only one bolt..Since these bolts are not used in safety applications and are small in size (5/8" or less in diameter), no further evaluation is considered necessary.
7. Seven fasteners which were ordered without any specifications or grade (and not used in safety applications) were inappropriately marked out of specification by the test laboratory. These specimens meet ASTM-A563 standards for nuts and A276 for 316 stainless steel. Since no specification or grade was ordered, and the material meets these specifications, the asterisks were removed.
8. The test laboratory was unable to run tensil tests on two bolting specimens.
(3/8" cap screws). Attachment 2 has "++++" entered into the data field for these two items. Retesting was not considered necessary since the chemical properties were in specification for both screws and because of their small size. These screws are not used in safety-related applications.
NRC COMPLIANCE BULLETIN87-02 Page Pour ITBM 6 Based on the, results of the testing and review of current procedures, describe any further actions being taken to.assure that fasteners used in the Plant meet the requisite specifications and requir'ements and that the operability of safety-related Plant components is not affected.
I RESPONSE TO ITEM 6 PSL intends to take the followin'g,action as a result of this Bulletin:
1. The manufacturers of the three fasteners found to be out of specification and used in safety applications will be contacted by our QA organization and supplied with the results of our testing. Plorida Power and Light Company is also considering having the manufactureis running the same testing on back up specimens now being retained at the Plant site.
Comparisons would then be made on consistency between the manufacturers new results, the CMTR's received during purchasing, and.the test lab results.
Further action could result pending review of the data.'he ID numbers for these three specimens are 028-25277-2-PS L, 030-61820-7-PSL, and 030-92120-1-PSL.
2. PSL is considering upgrading the quality level and procurement requirements for future purchases of fasteners not being used in safety applications".
3. Based on review of the evaluations for all out of specification fasteners identified by the testing in this bulletin:
I
a. Operability of safety-related Plant components are got affected by the results obtained in this bulletin.
b. No further action is deemed necessary for installed Plant fasteners or existing stocks.
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IO'8 028 25265 9-PSL 4
'ASTENER DESCRIPTION: STUD BOLT; CARBON STEEL, SIlE'/8-16x8",,
COARSE THREAD. I DESCRIPTION OF SAHPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS'DOCUHENTED BY LICENSEE RECORDS: ASIDE SA-193 GRADE B7 CARBON STEEL, ANSI 816.5, B1.1 CONTINOUS CLASS 2A COARSE THREAD, ASME,SECTI,ON III, CLASS 2.
HEAD MARKING SPECIFICA'TION ANO MANUFACTURER C, 87, K2. CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENDO LAS VEGAS, NEVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL-1 GENERAL PLANT APPLICATION E.G. PRESSUREiBOUNDARY STRUCTURAL PRESSURE BOUNDRY VENDOR: HUB INC; 2142'I FL INTSTONE ORIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IHPOSEO ON VENDOR: lgCFR 21, SQAO 1001, MANUFACTURER S CERTIFICATE OF COMPLIANCE OR MANUFACTURER'S CERTIFIEO MATERIAL TEST REPORT(CHTR) .
L ICENS'EE REPRESENTATIVE:
SIGNATURE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE Ioi 028 25277 2"PSL FASTENER DESCRIPTION: BOLT, STUD, CARBON STEEL, CLASS 2A THREAD, SIZE 5/8 -ll x 12 .
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO'WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: ASME SA-1 3 GR DE B7 CARBON STEEL, ANSI B16.5, B1.1 CONTINOUS CLASS2A THREAD, ASME SECTION III, CLASS 2, MATERIAL TO BE MARKED WITH
~
HEAT CODE TRACEABLE TO MANUFACTURER CERTIFICATE OF COMPLIANCE.
HEAD MARKING SPECIFICATION AND MANUFACTURER:
C, 8, HI, CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENDO LAS VEGAS, NEVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL-1 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
P<~<<~C God~d<Y -/I/ ]et, VENDOR: HUB INC.
21421 FLINTSTONE ORIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSED ON VENDOR: 10CFR 21, SQAD 1001, SQAD 100, QN LICENSEE REPRESENTATIVE:
SIGNATU E DATE~ P Pcf
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 028 25284 5-PSL FASTENER DESCRIPTION: BOLT, STUD, CARBON STEEL, CONTINUOUS CLASS 2A COARSE THREAD 3 4 -10 x 8".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: ASME SA-193 GRADE B7,'ARBON STEEL, ANSI B16.5, Bl. 1 CONTINOUS CLASS 2A COARSE THREAD.
HEAD MARKING SPECIFICATION AND MANUFACTURER :
C, B7, HI,CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENDO LAS VEGAS, NEVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL"1 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL i/rgb
-p VENDOR: HUB INC.
Z46 FCINTSTONE DRIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSED ON VENDOR: 10CFR 21, SQAO 1001,SQAO 1002 MANUFACTURER S ER FI E OF COMPLIANCE. MATERIAL TO BE MARKED WITH HEAT CODE TRACEABLE TO THE MANUFACTURER'S CERTIFICATE OF COMPLIANCE.
LICENSEE REPRESENTATIVE:
SIGNATUR DATE ~ cP PP
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 69105 2-PSL FASTENER DESCRIPTION: NUT, HEX FINISHED, ZINC PLATED, 3 8-24.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE 'RECORDS: GRADE 8, SAE', lINC PLATED.
~
" j ll HEAD MARKING SPECIFICATION ANll MANUFACTURER:
VARIOUS MANUFACTURER S (
CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDk'29 69610 1-PSL FASTENfR DESCRIPTION:, NUT, HEX, ZINC PLATED.
SIZE 7 16-20.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: GRADE 8, SAE, ZINC PL'ATfD.
lf HEAD MARKING SPECIFICATION AND MANUFACTURER VARIOUS MANUFACTURER S CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE Rf PRf SENTATIVE:
SIGNATUR DATE cP-
ATTACHMENT 1 FASTENER TESTING,DATA SHEET SAMPLE 108 029 69800 6-PSL Q1 FASTENER DESCRIPTION: NUT, HEX FINISHED, lINC PLATED, 1 2 -13.
F DESCRIPTION OF. SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE 4
MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL ZINC 'PLATED HEAD MARKING SPECIFICATION AND MANUFACTURER:. NO 'HEAD MARKINGS, VARIOUS MANUFACTURER S.
t CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
'GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHHENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 029 69800 6-PSL (93 FASTENER DESCRIPTION: NUT, HEX FINISHED, ZINC PLATED, 1 2 -13. (2NO NUT OF THIS ID 8)
DESCRIPTION OF SAHPLE STOCK LOCATION: UNIT ONE WEARHOUSE HATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL'INC PLATED HEAD HARKING SPECIFICATION AND HANUFACTURER: NO HEAD HARKINGS, VARIOUS HANUFACTURER S.
CLASS/PROCUREHENT LEVEL: NOT QL;1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL GENERAL NON-SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREHENTS IHPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU DATE
ATTACHMENT 1 fASTENER TESTING'ATA SHEET SANPLE IDP 029 76105 8-PSL (Q)
FASTENER DESCRIPTION: NUT, HEX fINISHEO, ZINC PLATED, SIZE 1/2-20.
~
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTEO BY LICENSEf RECORDS: GRADE 8, SAE, ZINC PLATED.
HEAD MARKING SPECIFICATION AND MANUFACTURER:(
VARIOUS MAUFACTURER S
, i, CLASS/PROCUREMENT LfVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL GENERAL NON-SAFETY, NON-CLASS USf.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSEO ON VfNOOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SARPLE IDP 029 70105 8-PSL (55)
I FASTENER DESCRIPTION:. NUT, HEX FINISHED, lINC PLATED, SIZE 1 2-20. 2ND,NUT OF SAME ID8)
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTE6 BY LICENSEE RECORDS: GRADE 8,! SAE, ZINC PLA ED.
[
HEAD MARKING SPECIFICATION AND MANUFACTURER: f V RIOUS MAUFACTURER S I
'CLASS/PROCUREMENT LEVEli: NOT QL-1,2 OR 3.
i GENERAL 'PLANT APPLICATION (E.G., P ESSURE BOUNDARY STRUCTURAL :
GENERAL NON"SAFETY, NON-CLASS USE.
I VRROdR:, VARIOUS I
I QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU E DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 70300 0-PSL'ASTENER DESCRIPTION: NUT, HEX FINISHED, STEE L, ZINC PLATED, 9 16'12.
I DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: , STEELj ZINC PLATED. C I
I I
I I
HEAD MARKING SPECIFICATION AND MANUFACTURER:
NO HEAD MARKINGS, VARIOUS MANUFACTURER'.
CLASS/PROCUREMENT LEVEL: NOT gL-1,2 OR 3.
I GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENER L NON-SAFETY, NON-CLASS USE.
VENOOR: VARIOUS OA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNAT DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 81300 0-PSL
FASTENER DESCRIPTION: SCREW, CAP,, HEX HEAD, ZINC PLA ED, 1 4 -20 x 3/4.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR , L ED.
HEAD. MARKING SPECIFICATION AND MANUFACTURER:,, KS.,
RI RER CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION (E.G., PRESSURE BOUNDARY STRUCTURAL GENE L NON-SAFETY, NON" L SS USE.
VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNAT DATE
ATTACHHENT 1 FASTENER TESTING DATA SHEET SAHPLE 108 029 82100 2-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 1 4 -20 x 1-1/4.
DESCRIPTION OF SAHPLE STOCK LOCATION: UNIT ONE WEARHOUSE HATERIAL SPECIFICATION AS DOCUHENTED BY LICENSEE RECORDS: STEEL GR , IN PLA ED.
'EAD HARKING U NU SPECIFICATION AND HANUFACTURER :
UR S. i , KS, I
CLASS/PROCUREHENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VENOOR: YARIOUS QA REQUIREHENTS IHPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 82125 8-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 1 4-28 x l-l/4.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: SAE J29, ROE HEAT TREATED, ZINC PLATED.
HEAD MARKING SPECIFICATION AND MANUFACTURER :
V RIOUS MANUFACTURER S w
li , KS, CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
GENE NON- FE Y, NON-CLASS .US VEROOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNAT DATE +t P'f
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 82800 7-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 1 4 -20 x 2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR , L D.
HEAD MARKING R OU NU (SPECIFICATION AND MANUFACTURER:
U S.
~, KS, CLASS/PROCUREMENT LEVEL: NOT gL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
GENER L NON-SAFETY, NON-CLASS USE.
VEROOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE g'
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDf 029 83300 1-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC P tED, 1 4 -20 x 2-1/2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTEO BY. LICENSEE. RECORDS: STEEL GR,, ZNC, L ED..
HEAD MARKING (SPECIFICATION AND MANUFACTURER:.
Vi(RIOUS MANUFACTURER'S CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATIO E.G.', PRESSURE BOUNDARY STRUCTURAL :
GENER L NON-SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU DATE
ATTACHMENT 1 FASTENER TEST1NG DATA SHEET SAMPLE 108 029 85100 9"PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 5 16 -18 x 1/2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE I
I i I MATERIAL SPECIfICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR,'
HEAD MARKING SPECIFICATION AND MANUFACTURER,:
V RIOUS MANUFAC URER S.
i, KS, LEVEL: gL-1,2 3.
ly'LASS/PROCUREMENT NOT OR I
I GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFET , NON-CLASS USE.
VENDOR: VARIOUS I
QA REQUIREMENTS IMPOSED ON VENDOR: NONE I
LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT TESTING DATA SHEET 1'ASTENER SAMPLE ID8 029 87100 0-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, lINC PLATED, 5 16 -18 x 2-1/2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE I
I I MATERIAL SPECIFICATION AS DOCUMENTEO BY LICENSEE RECORDS: STEEL GR , NC PL D.
HEAD MARKING (SPECIFICATION AND MANUFACTURER:,FM, 0 UR R CLASS/PROCUREMENT LEVEL: NOT gL-1,2 OR 3.
l I
l GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VEROOR: VARIOUS QA REQUIRE MENTS IMPOSEO ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 88800 0".PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, lINC PLATED, 3 8 -1 x 1/2".
DESCRIPTION Of SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR," NC PLA ED.
j HEAD MARKING V RIOU M NU (SPECIFICATION CTURER AND MANUFACTURER:,fM,
-/xj LEVEL: NOT QL"1,2 OR 3. 'LASS/PROCUREMENT GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAfETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE ~ f Z$'
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDP 029 90851 5-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, HEAT TREATED, ZINC PLATED.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: GRADE 8, SAE J429, ZINC PLATED.
HEAT TREATED.
HEAD NARKING SPECIfICATION AND NANUPACTURER: ~ l+
VARIOUS MANUFACTURER S
~] N CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENER L NON-SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 91100 1-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED,,
3 8 -16 x 2-1 2 DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL'PECIFICATION'AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR , N L D.
I HEAD@ MARKING 0
(SPECIFICATIOA U
AND MANUFACTURER
/i CLASS/PROCUREMENT LEVEL: ,NOT QL-1,2 3.
OR
-L(E.G.,
GENERAL PLANT"APPL1CATION ~ PRESSURE BOUNDARY STRUCTURAL GN S ~
VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE:REP SENTATIVE:
SIG NATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 94101 6-PSL FASTENER DESCRIPTION: 'CREW, CAP,, HEX HEAD, ZINC PLATED, 7 16-20 x 2" DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: SAE J429, GRADE 8 HEAD MARKING SPECIFICATION AND MANUFACTURER:
VARIOUS MANUFACTURER S.
CLASS/PROCUREMENT LEVEL: NOT QL"1,2 OR 3.
e GENERAL PLANT APPLICATION E.G.
GENERAL NON-SAFETY, NON-CLASS USE.
PRESSURE BOUNDARY STRUCTURAL :
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIG NATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 97301 5-PSL FASTENER .DESCRIPTION: SCREW, CAP, HEX HEAD, N ATED, 1/2"-20 x 2".
DESCRIPTION-OF-.SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE I
MATERIAL SPECIFICATION. AS DOCUMENTED BY LICENSEE RECORDS: SAE HEAT TREATED.
HEAD- MARKING"(-SPECIFICATION AND MANUFACTURER: ~ <
<, H, CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION (E.G., PRESSURE BOUNDARY STRUCTURAL :
G N R L NON- FETY, NON"CL SS U VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATURE DATE
e AYTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 029 97313 9-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, HEAT TREATED, ZINC PLATED.
SIZE 1/2"-20 x 2-1/4" DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: SAE J 429, GRADE 8, HEAT TRE TED, ZINC PLATED.
NEAR NARKING SPECIFICATION ANO NANUFACTURER:
VARIOUS MANUFACTURER S i/1iM CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL G R N-S FETY NON- LASS US VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
e ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE.IDf 029 97351 1"PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, SIZE 1 2-20 x 3 '.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 'SAE J429, GRADE 8, HEAT TREATED, ZINC PLATED.
HEAD MARKING SPECIFICATION AND MANUFACTURER: '~ s p s VARIOUS MANUFACTURER'S CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL GENERAL NON-SAFETY, NON-CLASS USE; VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATURE DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDf 029 97600 6-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 1/2 -13 x 2-1/2.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL'PECIFICATION AS DOCUMENTED, BY LICENSEE RECORDS: STEEL GRADE 5, ZINC PLATED.
HEAD MARKING SPECIFICATION AND MANUfACTURER:
VARIOUS MANUFACTURER S CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
P GENERAL PLANT APPLICATION E.G.
GENERAL NON-SAFETY, NON-CLASS USE.
PRESSURE BOUNDARY STRUCTURAL ':
VENOOR: VARIOUS QA RE UIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 029 98300 2-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 1 2 -13 x 4" DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GRADE) 5, .ZINC PLATED.
HEAD MARKING SPECIFICATION AND MANUFACTURER: NO HEAD MARKINGS, VARIOUS MANUFACTURER S.
CLASS/PROCUREMENT: LEVEL: NOT QL-1,2 OR 3.
GENERAL ]PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL GENERAL NON-SAFETY, NON"CLASS USE.
t VENDOR: VARIOUS I'
I i QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRES NTATIVE:
SIG NATU DATE I
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 029 99100 5-PSL H
I I
FASTENER DESCRIPTION:
SCREW, CAP, HEX HEAD', STEEL, lINC PLATED 9/16"-12 x 1".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE I
MATERIAL SPECIFICATION AS DOCOMENTED BY LICENSEE ~RECORDS: STEEL
'G ADE 5, ZINC PLATED I
HEAD MARKING SPECIFICATION AND MANUFACTURER:
VARIOUS MANUFACTURER S.
J CLASS/PROCURENENT LEVEL:, NOT OL-1,2 OR 3.
I GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.'ENOOR:
VARIOUS l I
QA REQUIREMENTS IMPOSED ON VENDOR: NONE REPRESENTATIVE:
'ICENSEE SIGNATUR TE I
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 01100 1-PSL'ASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 8 -11 x 1-1/ 2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 'TEEL GR , NC PL D.
HEAD MARKING (SPECIFICATION AND MANUFACTURER:, NF, R U N C URER S.
CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
I GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 01800 5-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLA ED, 18 -11 x 2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR 5, ZIN PL TED.
HEAD MARKING (SPECIFICATION AND MANUFACTURER:, N, ROU I N UR /X CLASS/PROCUREMENT LEVEL: NOT QL"1,2 OR 3.
GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL GENER L NON-SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRES ATIVE:
SIGNATURE DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDf 030 02615 6-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, 5 8-1 x 2-3 4 DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTEO BY LICENSEE RECORDS( SAE J 0GRO HEAT TREATED, ZINC PLATED. ~
HEAD MARKING"(SPECIFICATION AND MANUFACTURER:
I U U UR R S.
i i, FM, CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT. APPLICATION (E.G., PRESSURE BOUNDARY STRUCTURAL GENER L NON"SAFETY, NON-CLASS US VENDOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATURE DATE
ATTACHMENT 1 FASTENER TESTING DATA SHf ET SAMPLE ID8 030 05800 7-PSL FASTENER DESCRIPTION: SCRf W, CAP, HEX HEAD, 9/q'ESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUHENTED BY LICENSEE RECORDS: STEEL GR 5, lINC PLATED.
HEAD MARKING RI US ANU (SPECIFICATION C UR S.
AND MANUFACTURER :
i l
, KS, CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
G ENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL GENER L'NON"SAFETY, NON-CLASS USE.
VENDOR: VARIOUS QA REQUIRf MENTS IMPOSED ON VENDOR: NONE LICENSEf REPRES NTAT VE:
SIGN ATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 030 09600 6-PSL FASTENER DESCRIPTION: SCREW,* CAP, HEX HEAD, lINC PLATED, 7 8 -9 x 3".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR , INC PLATED.
HEAD, MARKING SPECIFICATION AND MANUFACTURER:, NF, N 7 R U UR R S.
CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION (E.G., PRESSURE GENERAL NON-S FETY, NON-CLASS USE.
BOUNDARY'TRUCTURAL :
VENDOR: VARIOUS QA RE UIREMENTS IMPOSED. ON,VENDQR: NONE LICENSEE. REPRESENTATIVE:
SIGNATU E. DATE
ATTACHHENT 1 fASTENER TESTING DATA SHEET SAMPLE ID8 030 10300 2-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, ZINC PLATED, 7 8 -9 x 4".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: STEEL GR, ZINC PLA D.
HEAD MARKING (SPECIFICATION AND HANUFACTURER:
VARIOUS H NU ACTURER S. /4 NF, CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.,
GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURA GENERAL NON-S FETY, NON-CLASS USE.
VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDP 030 12100 1-PSL FASTENER DESCRIPTION: SCREW, 'CAP, HEX HEAD, ZINC PLATED, 1 -8 x DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE j
MATERIAL SPECIFICATION A'S DOCUMENTED BY LICENSEE RECORDS: STEEL GR , N T D.
HEAD MARKING SPECIFICATION AND MANUfACTURER RIOU MANUFACTURER S.
..l NF CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
I GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL :
G NE AL ON"SAfETY, NON-CLASS USE.
'ENOOR: VARIOUS II i
QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTAT E:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDH 030 16256 4-PSL FASTENER DESCRIPTION: BOLT, HEAVY HEX HEAD, COARSE THREAD GALVANIZED, SIZE 1 2 -13 x 2 1/2" DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE I I MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: A325 YPE 1, HO 0 PP D GALV NI ED A153.
HEAD MARKING SPECIfICATION AND MANUFACTURER: A325, l5TS, PRESTIGE STAMPING, INC.
23605 GROESBECK HIGHWAY WARREN, MICHIGAN 48089.
GENERA PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL STRUCTURAL VENDOR: ENERGY STEEL lh SUPPLY"CO.
1681 W. NANLIN RD ROCHESTER, MI 48063 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006,QAP-83-337.
LICENSEE REPRESENTATIVE:
SIGNATURE DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDIO 030 16270 0-PSL FASTENER DESCRIPTION: SCREW, CAP, HEAVY HEX HEAD, COARSE THREAD, HOT DIP GALVANIZED, SIZE 3/4"-10 x 2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: ASTM A-325 TYPE 1, HOT DIP GALVANIZED ASTM A-153.
HEAD MARKING SPECIFICATION AND MANUFACTURER: A325, LE, LAKE ERIE SCREW CORP RA ION 13001 ATHENS AVENUE CLEVELAND, OHIO 44107 216-521-1800 CLASS/PROCUREMENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
STRUCTURAL VENDOR: NOVA MACHINE PRODUCTS CORP
~1868 SNELOON RO PO BOX 30287 MIDDLEBURG HEIGHTS OH 44130 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006, SQAD 1005, QCN 4Y 4M.
LICENSEE REPRESENTATIVE:
SIGNATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 030 16280 7-PSL I'ASTENER DESCRIPTION: BOLT, HEAVY HEX HEAD, COARSE THREAD, HOT OIP GALVANIZED, SIZE 7/8"-9 x 2".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE I
MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: A 325, TYPE 1 HOT DIP GALVANIZED A 153.
I'EAD MARKING SPECIFICATION AND HANUFACTURER: A-325, TEXAS BOLT,~ ~
TEXAS BOLT COMPANY P.O. BOX 1211
~
HOUSTON, TEXAS 77251-1211
'I CLASS/PROCUREMENT LEVEL: QL"2 GENERAL PLANT APPLICATION E G. PRESSURE BOUNDARY STRUCTURAL:
STRUCTURAL VENDOR: ENERGY STEEL 5 SUPPLY COMPANY 1681 WEST HAMLIN ROAD ROCHESTER MI 480635207 QA REQUIREMENTS IMPOSED ON VENDOR: SQAO 1006, CERTIFICATE OF COMPLIANCE.
LICENSEE REPRESENTATIVE:
SIGNATURE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 030 16294 7-PSL FASTENER DESCRIPTION: BOLT, HEX, HEAVY, GORSE THREAD, HOT DIP GALVANIZED, SIZE 1"-8 x 5" DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION 'AS'OCUMENTED BY LICENSEE RECORDS: A325, TYPE 1, HOT DIPPED GALVANIZED (
I A153.
HEAD MARKING SPECIFICATION AND MANUFACTURER:
A325, LE, CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENDO LAS VEGAS,'EVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G.. PRESSURE BOUNDARY STRUCTURAL :
STRUCTURAL VENDOR: NUO INC.
2146 FLINTSTONE ORIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006,AL'L MATERIAL CERTIFI ATES OF COMPLIANCE SHALL BE CERTIFIEO BY THE FINAL MANUFACTURERS QA ORGANIZATION AS HAVING MET THE REQUIREMENTS OF THE MATERIAL SPECIFICATION OR SHALL BE BASED ON THE ORIGINAL MATERIAL MANUFACTURERS CMTR/MTR WHICH MUST BE ON FILE AT YOUR FACILITY SUBJECT TO FPL AUDIT. SUCH DOCUMENTATION MUST BE TRACEABLE TO THE ITEM PROVIDED AND WILL BE VERIFIED BY FPL UPON RECEIPT.
LICENSEE REPRESENTATIVE:
1 SIGNATUR DATE
ATTACHMENT 1 fASTENER TESTING DATA SHEET SAMPLE ID8 030 59599 1-PSL FASTENER DESCRIPTIO,N: NUT-HEAVY HEX STEEL, 3/8"-16.
I II DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT,TWO WAREHOUSE MATERIAL, SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: ASME SA-194 GR. 2H,.CL SS 2B, ASME SECTION I'I I CLASS 2, MATERIAL TO BE MARKED WITH'EAT CODE TRACEABLE TO MFG.'ERTIFICATE OF, COMPLIANCE.
2H, Q, HEAD MARKING SPECIFICATION AND MANUFACTURER CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENDO LAS VEGAS, NEVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL-1 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL PRESSURE BOUNDARY VENDOR: HUB INC.
2146 FLINTSTONE DRIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSED ON VENDOR: 10CFR 21, SQAD 1001,SQAD 1005, QCN 4Y, LICENSEE REP SENTATI VE:
SIGN ATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 030 60598 9"PSL FASTENER DESCRIPTION: NUT, HEAVY HEX, STEEL, CARBON, SI2E 5 8 -11. N DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE t
MATERIAL SPECIFICATION AS DOCUMENTEO BY LICENSEE RECORDS: ASME SA"194 GR. 2H, CLASS 28, ASME SECTION III, CLASS 2, MATERIAL TO BE MARKED WITH HEAT CODE TRACEABLE TO MANUFACTURER'S CERTIFICATE OF COMPLIANCE.
HEAD MARKING SPECIFICATION ANO MANUFACTURER:
2H, C"U, K-4, 0, CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENOO LAS VEGAS, NEVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL-1 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
STRUCTURAL Nassau= GouvduV VENDOR: HUB INC.
2146 FLINTSTONE ORIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSEO ON VENDOR: 10CFR 21, SQAD 1001 SQAD 10 , SQAO 0 , QCN 4Y 4M LICENSEE REPRESENTATIVE:
SIGNAT RE DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 60798 1-.PSL FASTENER DESCRIPTION:, NUT, HEAVY HEX, CARBON STEEL, SIZE 3 4 -1 DESCRIPTION OF SAMPLE 'STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED. BY LICENSEE RECORDS:
SA-194, GRADE 2H; ASME SECTION III, CLASS 2.
HEAD MARKING SPECIFICATION AND MANUFACTURER:
HAMANAKA NUT MFG. CO., LTD. HIME'JI JAPAN.
2H, H, AMC, CLASS/PROCUREMENT LEVEL: QL-1 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL STRUCTURAL gt~o<): g~~~y VENDOR: A fc G ENGINEERING CO II INC AGAO EAST LAPALMA AVE ANAHEIM CA 92806.
QA REQUIREMENTS IMPOSED ON VENDOR:
10CFR 21, SQAD 1001, SQAD 1002, SQAD 1005, QCN 4D, 4Y, 4M LICENSEE REPR NTATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDf 030 61820 7-PSL FASTENER DESCRIPTION: NUT, HEAVY HEX, GALVANIZED SIlE 1 2 -13.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: A194 "GRADE 2H HOT DIP GALVANIZED TO A153.
HEAD MARKING SPECIFICATION AND MANUFACTURER: 2H, T, TEX S BO T COMPANY P.O. BOX 1211 HOUSTON, TEXAS 77251-1211 CLASS/PROCUREMENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
STRUCTUR L VENDOR: ENERGY STEEL 5 SUPPLY CO.
1681 W. HAMLIN RD ROCHESTER, MI 48063 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006, CERTIFICATE OF COFORMANCE.
LICENSEE REPRESENTATIVE:
SIGNAT E DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 61835 5-PSL I
., I
FASTENER DESCRIPTION

NUT, HEAVY HEX, CARBON STEEL, HOT DIP GALVANIZED; SIZE 3 4 -10.
I DESCRIPTION.'OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE I
MATERIAL SPECIFICATION A'S DOCUMENTED BY LICENSEE RECORDS: A"194 GRADE 2H, HOT DIP GALVANIZE ASTM A"153.
I II HEAD MARKING SPECIFICATION AND MANUFACTURER: H, 2, T, TEXAS BOLT COMPANY P.O. BOX I1211, HOUSTON, TEXAS 77251-1211 I
CLASS/PROCUREMENT LEVEL: OL-2 f
I GENERAL 'PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
S TRUCTU AL I VENDOR: NOVA MACHINE PRODUCTS CORP
~1 685 SHELOON RO PO BOX 30287 MIDDLEBURG HEIGHTS OH 44'130 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006, SQAD 1005, QCN 4Y 4M. j I I I l
I LICENSEE REPRESENTATIVE:
SIGNATURE DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDP 030 61840 1-PSL I
rl FASTENER DESCRIPTION: NUT-HEAVY, HEX, SIZE 7/8"-9.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE I
MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: ASTM A-194, GRADE 2H, GALVANIZED A-153. I HEAD MARKING SPECIFICATION AND MANUFACTURER: 2H, @S, BETHLEHEM STEEL CORPORATION BETHLEHEM, PA 18016.
l CLASS/PROCUREMENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
STRUCTURAL VENDOR: FLORIDA BOLT & NUT CO
. BOX 6427 WEST PALM BEACH FL 33405.
QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006, SQAD 1005, QCN 4Y, 4A, 4B.
LICENSEE REPRESENTATIVE:
D II SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 61845 2-PSL FASTENER DESCRIPTION:, NUT, HEAVY HEX, CARBON DIPPEO GALVANIZED, SIZE 1"-8.
STEEL,'OT DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUHENTED BY LICENSEE RECORDS: A"194 GRADE 2H, HOT DIPPED GALVANIZED ASTH A-153.
HEAD MARKING SPECIFICATION AND MANUFACTURER: 2H, J, BERGEN-PATERSON PIPE SUPPORT CORP.
P 0 BOX 4011 74 COMMERCE WAY WOBURN HA 018880000.
CLASS/PROCUREMENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
STRUCTURAL VENDOR: BERGEN-PATERSON PIPE SUPPORT CORP.
P 0 BOX 4011 74 COHHERCE WAY WOBURN HA 018880000.
QA REQUIRE HENTS IHPOSED ON VENDOR: SQAO 1006, SQAD 1005, QCN 4Y.
LICENSEE REPRESENTATIVE:
SIG NATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 030 92110 4-PSL(A FASTENER DESCRIPTION: NUT, HEAVY HEX, SIlE 1/4"-20.
DUPLICATE NUT DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE SPECIFICATION AS OOCUMENTEO
'ATERIAL BY LICENSEE RECORDS: 304
'S.S., A194, GRADE 8, HEAD MARKING SPECIFICATION AND MANUFACTURER:
B8, CF, CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENOO LAS VEGAS, NEVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY. STRUCTURAL :
STRUCTURAL VENDOR: HUB INC.
2146 FLINTSTONE DRIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSEO ON VENDOR: SQAD 1006, SQAD 1005, QCN 4Y AND 4M.
LICENSEE REP NTATIVE:
SIGNATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SANPLE 109 030 92110 A-PSL (8)
FASTENER DESCRIPTION: NUT, HEAVY HEX, SIZE 1/4"-20.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 304 S. S., A194, GRADE 8, HEAD MARKING SPECIFICATION AND MANUFACTURER BB, CF, CARDINAL INDUSTRIAL PRODUCTS CORP.
3873 WEST OQUENDO LAS Vf GA'S, NEVADA 89118-3098.
CLASS/PROCUREMENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL TRUCTURAL VENDOR: HUB INC.
2146 FLINTSTONE DRIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006, SQAD 1005, QCN 4Y AND 4M.
LICENSEE REPRESENTATIVE:
SIGNATU E DATE Pg'
ATTACHHENT TESTING DATA SHEET 1'ASTENER SAHPLE ID8 030 92120 1-PSL FASTENER DESCRIPTION: NUT, HEAVY HEX, SIlE 1/2"-13.
DESCRIPTION OF SAHPLE STOCK LOCATION: UNIT TWO WAREHOUSE HATERIAL SPECIFICATION AS DOCUHENTED BY LICENSEE RECORDS: 304 S. S., A-194, GRADE 8.
HEAD HARKING SPECIFICATION AND HANUFACTURER: BBH, BERGEN-PATERSON PIPESUPPORT CORP PO BOX 4011 74 COHHERCE WAY WOBURN HA 018880000 CLASS/PROCUREHENT LEVEL: QL-2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY 'STRUCTURAL STRUCTURAL VENDOR: BERGEN-PATERSON PIPESUPPORT CORP PO BOX 4011 74 COHHERCE WAY WO8 URN HA 018880000 QA REQUIREHENTS IMPOSED ON VENDOR: SQAD 1006, SQAD 1005, QCN 4Y.
LICENSEE REP SENTATIVE:
SIGN ATU
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 92140 6-PSL fASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, SIZE 1/4"-20 x 1"1 4 DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED" BY LICENSEE RECORDS: 304 S. S., A193, GRADE 8, HEAD MARKING SPECIFICATION AND MANUFACTURER: BBTB, C3, TEXAS BOLT COMPANY P.O. BOX 1211 HOUSTON, TEXAS 77251-1211 LEVEL: QL-2
'LASS/PROCUREMENT GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL STRUCTURAL VENDOR: NOVA MACHINE PRODUCTS CORP 18685 SHELDON RD PO BOX ~87.
MIDDLEBURG. HEIGHTS OH 44130 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006, SQAD 1005, QCN 4Y, 4M.
LICENSEE REPRESENTATIVE:
SIGNATUR oavr~g~
'TTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 92145 7-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, SI1E 1/4"-20 x 2" DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE
'~. MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: A-193, GRADE B-8, 304 S.S.
.I HEAD MARKING SPECIFICATION AND MANUFACTURER: B8, N, NOVA MACHINE PRODUCTS 18685 SHELDON ROAD MIDDLEBURG HEIGHTS, OH.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL STRUCTURAL VENDOR: HUB INC.
2146 FLINTSTONE DRIVE TUCKER, GEORGIA. 30085 QA REQUIREMENTS IMPOSED ON VENDOR: SQAD 1006, SQAD 1005.; QCN 4Y 4M.
LICENSEE REPRE ATIVE:
SIGNATUR DATE
ATT'ACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 92170 8-PSL I
FASTENER DESCRIPTION: SCREW, CAP, HEAVY'EX HEAD, SIlE 1/2"-13 x 2
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT TWO WAREHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS 304 S.S., 'A193, GRADE B-8, HEAD MARKING SPECIFICATION AND MANUFACTURER: B8, TB, TEXAS BOLT COMPANY P'A. BOX 1211 HOUSTON, TEXAS 77251-1211 CLASS/PROCUREMENT LEVEL: QL"2 GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
STRUCTURAL I
I VENDOR: ENERGY STEEL 5 SUPPLY COMPANY 1681-"WEST HAMLIN ROAD ROCHESTER MI 480635207 QA REQUIREMENTS IMPOSED ON VENDOR: 'SQAD 1006, SQAD 1005, QCN 4Y AND 4M.
LICENSEE REPRES NT TIVE:
SIGNATUR DATE
ATTACHHENT 1 FASTENER TESTING DATA SHEET SAHPLE ID8 030 94600 0-PSL FASTENER DESCRIPTION: NUT, HEX FINISHED, 3/8""16.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE" MATERIAL SPECIFICATION AS DOCUHENTED BY LICENSEE RECORDS: 31'6 S.S.
t I
HEAD MARKING SPECIFICATION AND'ANUFACTURER: 316, VARIOUS MANUFACTURER'S.
CLASS/PROCUREMENT LEVEL: NOT QL-1,2,0R 3.
e GENERAL PLANT APPLICATION E.G.
GENER L NON-SAFETY, NON"CLASS USE.
PRESSURE BOUNDARY STRUCTURAL :
VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRE TATIVE:
SIGNATUR DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 95000 7-PSL FASTENER DESCRIPTION: NUT, HEX FINISHED, 1/2"-13.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 316 S.S.
HEAD MARKING SPECIFICATION AND MANUFACTURER: 316, VARIOU MANUFACTURER S.
CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL GENERAL NON-SAFETY, NON-CLASS USE.
VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU E DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 030 95400 2-PSL FASTENER DESCRIPTION: NUT, HEX FINISHED, 5/8"-.11 E ~
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 316 S.S. H I HEAD MARKING SPECIFICATION AND MANUFACTURER: 316, VARIOUS MANUFACTURER S ~
CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON"CLASS USE.
VENDOR: VARIOUS A RE UIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDf 031 15700 9-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, 3/8"-16,x 1/2.
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS OOCUMENTEO BY LICENSEE RECORDS: 316 S.S.
HEAD MARKING SPECIFICATION AND MANUFACTURER: 316, VARIOUS MANUFACTURER'S.
CLASS/PROCUREMENT LEVEL: NOT gL-1,2 OR 3.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VENOOR: VARIOUS
(}A REOUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTA IVE:
SIGNATUR
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 031 24600 1"PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, 1/2"-13 x 3".
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 316 S.S.
HEAD MARKING SPECIFICATION AND MANUFACTURER: 316, VARIOUS MANUFACTURER'S.
CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
j G ENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VSNOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET
.SAMPLE ID8 031 27200, 2-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, SIZE 5/8"-ll x '3".
'I II 4
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: '16 S.S. ~ I N
HEAD MARKING SPECIFICATION AND MANUFACTURER: 316, VARIOUS MANUFACTURER S.
I CLASS/PROCUREMENT LEVEL: NOT gL-1,2 OR'.
GENERAL PLANT APPLICATION E.G. PRESSURE BOUNDARY STRUCTURAL GENERAL NON"S FETY, NON"CLASS USE.
VEROOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU DATE
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE 108 031 27600 8-PSL FASTENER DESCRIPTION: SCREW,.CAP, HEX HEAD, 5 8 -11 x 4 DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS:. 316 S.S.
HEAD MARKING SPECIFICATION AND MANUFACTURER: H, 316, V RIO S MANUFACTURER S.
CLASS/PROCUREMENT LEVEL: NOT QL-1,2 OR 3.
GENERAL PLANT APPLICATION (E.G., PRESSURE BOUNDARY STRUCTURAL :
GENERAL NON-SAFETY, NON-CLASS USE.
VENOOR: VARIOUS QA REQUIREMENTS IMPOSED ON VENDOR: NONE LICENSEE REPRESENTATIVE:
SIGNATU E DATE I ' 1 h I I hP
~ ( hhl h I,, ~
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE IDP 031 32800 8-PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, SI2E 7 8 -9 x 4-1 4 DESCRIPTION OF SAMPLE STOCK LOCATION: 'UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 316
'S.S., STH A193, GR 8BM HEAD MARKING SPECIFICATION AND MANUFACTURER: A, BBH, 316, BYRON J CKSON PUMP DIVISION BORG WARNER CORP 3109 MAPLE DRIVE N.E. SUIT 415 ATLANTA GEORGIA 30305.,
GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY STRUCTURAL PRESSURE RETAINING VENDOR: BYRON JACKSON PUMP DIVISION BORG WXRWGR CORP 3109 HAPLE DRIVE N.E. SUIT 415 ATLANTA GEORGIA 30305.
QA REQUIREMENTS IHPOSED ON VENDOR: SQAD 1001, SQAD 1002, SQAD 10 QCN 4Y.
LICENSEE REPRESENTATIVE:
SIGNATU DATE
~ > . >. ~ ~
ATTACHMENT 1 FASTENER TESTING DATA SHEET SAMPLE ID8 031 34500 0"PSL FASTENER DESCRIPTION: SCREW, CAP, HEX HEAD, 1"-8 x 3" .
DESCRIPTION OF SAMPLE STOCK LOCATION: UNIT ONE WEARHOUSE MATERIAL SPECIFICATION AS DOCUMENTED BY LICENSEE RECORDS: 316 I
S.S.
'EAD MARKING SPECIFICATION AND MANUFACTURER: H, 316, V RIOUS MANUF CTURER S.
CLASS/PROCUREMENT LEVEL: NOT Qi-l,2 OR 3.
GENERAL PLANT APPLICATION E.G., PRESSURE BOUNDARY. STRUCTURAL :
GENER L NON-S FETY, NON"CLASS USE.
VENOOR: VARIOUS
'AI REQUIREMENTS IMPOSED ON VENDOR: NONE
~
LICENSEE REPRESENTATIVE:
SIGNATUR DATE
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 028-25265-9-PSL CHEMICAL ANALYSIS I
I ( l Si P Cr Ni Mo
.380 .73 .29 .022 .011 .93 .15 A
MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS XRA A- ,8 C 67,67,67.5 34 146.4 138.8 16.8 56.0
'TTACHMENT 2 OATA
SUMMARY
PSL 028-25277-2-PSL CHEMICAL ANALYSIS I
C Mn Si P ~, S Cr Ho
.391 .84. .28 .018 .008 .90 .17 MECHANICAL ANALYSIS NARONESS UTS 0.2%VS %EL %RA A C 65,65,64.5. 30 144.2 134.0 17.7 48.0*
t
ATTACHMENT 2 DATA
SUMMARY
PSL ID¹ 028-25284-'5-PSL CHEMICAL ANALYSIS
.391 '.68 S1
.33 .020 S
.009 Ct 1.06 '18 N't Mo MECHANICAL ANALYSIS HARONESS UTS 0.2XYS %EL %RA
.A 8 59,58,57. 95 133.6 125.6 22.8 62.0
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 029-69105-2-PSL CHEMICAL ANALYSIS Si iP S Cr Ni Mo
..210* .020 013 MECHANICAL ANALYSIS BARONESS UTS 0.2XYS '1oEL %RA A 8 C 66,66,66.5. 31*
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 029-69610-1-PSL CHEMICAL ANALYSIS Mn Si Cr Mo I
.228* .022 .019 MECHANICAL ANALYSIS BARONESS UTS 0.2XYS 1oEL %RA A C 67,67.5,67. 34
ATTACHMENT 2 DATA
SUMMARY
PSL ID 029-69800-6-PSL CHEMICAL ANALYSIS f ~
I C Si P Ct Ni Mo
.075 .019 .006 MECHANICAL ANALYSIS NARONESS UTS 0.2XYS %EL ERA A B 60,59.5,60. 98
ATTACHMENT 2 OATA
SUMMARY
PSL IOf 029-69800-6-PSL <5 ~
II r 1 CHEMICAL ANALYSIS C
.072 Si I
P.,
1 S, ll Cr, s
Mo
.020 .007 MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS A B 60,60,60. 98
ATTACHMENT 2 DATA
SUMMARY
PSL I08 029-70105-8-PSLfA)
CHEMICAL ANALYSIS C Si Cr Ni
.232* .014 009 MECHANICAL ANALYSIS HARDNESS UTS 0. 2XYS %EL %RA A C 68,67,65.
ATTACHMENT 2 DATA SUHHARY PSL IDf, 029-70105-8-PSL($ )
CKEHICAL ANALYSIS Mn Si S Cr "
Ni Mo
.225* .023 .009 MECKANICAL ANALYSIS HARONESS UTS 0.2XYS. %EL A 8 C 67,66,66.5. 33
ATTACHHENT 2 DATA SUHHARY PSL Ii08 029-70300-0-PSL I
CHEHICAL ANALYSIS I
Si Cr Ho l
.061 HECHANICAL ANALYSIS e HARDNESS UTS 0.2XYS %EL XRA A
57,56.'5,55.5. 93 I
ATTACHMENT 2 DATA
SUMMARY
PSL IOO 029-81300-0-PSL CHEMICAL ANALYSIS .
Si s, Cr Mo I I
.300 .024,', .017 MECHANICAL ANALYSIS II HARORESS 'UTS 0.2SYS '1oEL %RA A B C 64,64,63. II 27 BOLT,)3002 I
II
ATTACHHENT 2 DATA SUHHARY PSL
?08 029-82100-2-PSL
. CHEHICAL ANALYSIS I
C Si S ~
Cr Ni
.314 .015 .015 ~
HECHANICAL ANALYSIS BARONESS UTS 0.2XYS %EL %RA A C 66,66.5,64. 30 148.3 140.0 24.6 66.6
ATTACHMENT 2 DATA
SUMMARY
PSL I08 029-82125-8-PSL CHEMICAL ANALYSIS I
C Mn i
Si P S Cr Ni, Mo
.258* .Oll I
MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS %EL A C 69,70,70. 39 ,
179.2 164.2 22.1
ATTACHHENT 2 OATA SUHHARY PSL I08 029-82800-7-PSL CHEH ICAL ANALYSIS C Si Cr Ni'o
.329 .016 .001 HECHANIGAL ANALYSIS HARONESS UTS 0.2XYS %RA A C 61,61,63. 25 145.8 138.8 28.8 58.3
ATTACHHENT 2 DATA SUHHARY PSL ID8 029-83300-1-PSL CHEHICAL ANALYSIS Si S " Cr
.342 .015 ;017 HECHANICAL ANALYSIS NARONESS UTS 0.2XYS %EL %RA A
65,65,66.
8 30:
C 157.5 149.2 '6.3 58.3 yp \ 8 . ~ h hi/ 0 h 'I,P- h
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 029-85100-9-PSL CHEMICAL ANALYSIS Mn Si 'Cr Ni Mo
.331 .020 .021 MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS %RA A B C 67,66,66. 33 BOLT,85008
ATTACHMENT 2 OATA
SUMMARY
PSL I08 029-87100-0-PSL CHEMICAL ANALYSIS C. Hn Si Cr Ho
,,I
.379 .017 MECHANICAL ANALYSIS HARONESS UTS 0.2XYS %RA A B C 65! 5,65,65.5 30 151.6 142.0 15.5 56.0 II l
I
, I I
I V W 8 '
V.
ATTACHMENT 2 DATA
SUMMARY
PSL IDO 029-88800-0-PSL CHEMICAL ANALYSIS Si S Cr. Ni Mo
'C'333 'I
'018 007 1
1 MECHANICAL ANALYSIS I
HARORESS uTS 0.2XYS 'XEL %RA A B 0 65.5,65.5,65. ++++ ++++ ++++
I 1
ATTACHMENT 2 DATA
SUMMARY
PSL I08 029-90851-5-PSL CHEHICAL ANALYSIS C," Hn Si P 'Cr Ho
.374 .019, .008 MECHANICAL ANALYSIS I
HARDNESS UTS 0.2XYS XRA
%EL'2 A B C 69,69,67.5. 36 170.4 161.2, 7
ATTACHMENT 2 DATA SUMHARY PSL I08 029-91100-1-PSL CHEMICAL ANALYSIS Si Cr Ho
.356 .013 013 HECHANICAL ANALYSIS HARONESS UTS 0.2XYS /GAEL %RA C
65,64,64.5. 29 150.4 142.4 '8.2 64.0
ATTACHMENT 2 DATA SUHHARY PSL IO¹ 029-94101-6-PSL CHEMICAL ANALYSIS Si Cr Ni Ho
.379 .017 .018 MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS loEL KARA A C 68.5,68,71. 36 171.6 160.0 12.9 56.0
ATTACHMENT 2 BATA
SUMMARY
PSL ID8 029-97301-5-PSL CHEMICAL ANALYSIS Si P S Cr Ni Mo
. 223* .025 .010 MECHANICAL ANALYSIS HARONESS UTS 0.2XYS %RA A C 69,67,68. 34 167.6 161.6 15.9 72.0
~ ',* em ~
ATTACHMENT 2 OATA
SUMMARY
PSL I08 029-97313-9-PSL CHEMICAL ANALYSIS C Si Ho
.388 .020 .012 HECHANICAL ANALYSIS HARONESS UTS 0.2XYS XfL %RA A B C 65,66,67. 32* 168.3 157.1 14.6 58.3
ATTACHMENT 2 OATA
SUMMARY
PSL IDf 029-97351-1-PSL CHEMICAL ANALYSIS
,Si Cr Mo
.336 .019 .021 MECHANICAL ANALYSIS HARDNESS 0.2XYS %RA A C 68.5,68,66.5. 34 174.0 '164.0 12.1 52.0
ATTACHMENT 2 DATA
SUMMARY
PSL IDIml - 029-97690-6-PSL CHEMICAL ANALYSIS Hn Si Cr Ho
.322 .023 009 HECHANIGAL ANALYSIS BARONESS UTS 0.2XYS %RA A C 63,64.64. 27 131.6 118.8 16.0 68.0
ATTACHHENT 2 OATA SUHHARY PSL
?08 029-98300-2-PSL CHEH ICAL ANALYSIS Mn Si Cr Ni Ho
.095* ;016 .014 HECHANICAL ANALYSIS NARONESS UTS 0.2XYS %EL %RA A
46. 5,50,49. 79* 71.6* 69.6* 12.6* 64.0 l
ATTACHMENT 2 OATA
SUMMARY
PSL ID8 029-99100-5-PSL CHEMICAL ANALYSIS
,C 'n Si P S Cr, Ni Mo
.404 .022 .008 MECHANICAL ANALYSIS BARONESS UTS 0. 2XYS %EL A' C 65,63,65.5. 28 136.0 112.5 29.7
ATTACHHENT 2 DATA SUHHARY PSL IOIII 030-01100-1-PSL CHEHICAL ANALYSIS 1
C Si P Cr Ni Ho
.321 .022 .011 HECHANICAL ANALYSIS NARONESS UTS 0.2XYS %EL 1oRA A B- C 63.63.5,62.5. 26 137.6 126.0 24.3 80.0
ATTACHMENT 2 DATA
SUMMARY
PSL I08 030-01800-5-PSL CHEMICAL ANALYSIS
.347 Mn Si P
.015 S
'006
'r I
Ni Mo MECHANICAL ANALYSIS HARDNESS UTS D.2XYS %EL %RA A B 65.5,66.5,66.5. 32 136.4 126.4 18.1
ATTACHMENT 2 DATA SUMHARY PSL ID8 030-02615-6-PSL, CHEMICAL ANALYSIS
~ g C Mn Si P S Ni Ho
.261* .011 .014 HECHANICAL ANALYSIS NARONESS UTS 0.2XYS %RA A B C 69,69 j68.5. 37 179.8 171.4 16.3 65.3
ATTACHMENT 2 OATA
SUMMARY
PSL ID8 030-05800-7-PSL CHEMICAL .ANALYSIS I
I
.C Mn .,Si II S'" Cr Ni Mo
'I i P'023
.327 0
.009 MECHANICAL ANALYSIS NARONESS UTS 0.2XYS %EL A B C 65,66,66. 31 138.0 126.4 19.3
ATTACHMENT 2 DATA SUMHARY PSL ID8 030-09600-6"PSL CHEMICAL ANALYSIS Si Cr Ni Ho II
.315 .018 015 Hf CHANICAL ANALYSIS HARDNESS D.2XYS %EL A B 30'TS 66,65.5,65.5. 135.0 121.0 22.1
ATTACHHENT 2 DATA SUMHARY PSL IDP 030-10300-2-PSL CHEMICAL ANALYSIS Si Cr Mo 334 .015 .013 MECHANICAL ANALYSIS
'ARONESS UTS 0.2XYS XRA A C 65,63.5,63.5. 28 127.6 108.0 18.8 63.3
ATTACHMENT 2 DATA SUMHARY PSL ID8 030-12100-1-PSL CHEMICAL ANALYSIS Mn Si P Cr Ni "Mo
.333 .017 .013 HECMANICAL ANALYSIS HARDNESS UTS 0.2XYS A C 67,67,67. 34 122.2 95.9 23.3 61.2
ATTACHMENT 2 DATA
SUMMARY
PSL I08 030-162)6-4-PSL I
'I ~
CHEMICAL 'ANALYSIS C,"'80 Mn I
Si Cr Ni Mo
.343 .017 .016 W
MECHANICA ANALYSIS I
l HARDNESS UTS 0.2XYS %EL %RA
, 8 C 63],63.5,6P .5 27 150.4 140.0 14.3 52.0
~
I I
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030-16270-0-PSL CHEMICAL ANALYSIS I
C Si P Mo I
.393 .68 .024 .005 MECHANICAL ANALYSIS BARONESS UTS 0.2XYS %EL I
'%RA A B 67.5,67,67.5. 34 II,148.0 14.3 52.0
~ 2
ATTACHMENT 2 DATA
SUMMARY
PSL IOS 030-16294-7-PSL CHEMICAL ANALYSIS C Si Cr' "Ni Mo S'007
.374 .88 .016 MECHANICAL ANALYSIS HARONESS UTS 0. 2XYS %RA A B C 64,65,65. 30 148.8 134.0 15.8 50.0 I
ATTACHHENT 2 DATA SUHHARY PSL ID8 030-16280-7-PSL CHEHICAL ANALYSIS Si Cr Ni Ho
.454 .60 .024 .022 HECHANICAL ANALYSIS HARDNESS UTS 0.2XYS %EL %RA A B 66.5,66.5,67.5, 33 148.0 126.0 14.8 40.0
ATTACHMENT 2 DATA
SUMMARY
PSL I08 030-59599-1-PSL CHEHI GAL ANALYSIS C Hn Si Cr Ho
.401 .024 .018 MECHANICAL ANALYSIS HARONESS UTS 0.2XYS /oEL %RA A B C 66,67,67. 33
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030-60598-9-PSL CHEMICAL ANALYSIS Mn Si Mo
.447 .023 008 MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS %EL %RA A C 66,64.5,67. 33
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030-60798-1-PSL CHEMICAL ANALYSIS Mn Si Cr Mo
.468 .018 014 MECHANICAL ANALYSIS BARONESS UTS 0.2XYS 1oEL %RA A C 68,68.67.5. 35
ATTACHMENT 2 OATA
SUMMARY
PSL 108 030-61820-7-PSL CHEMICAL ANALYSIS C Si S Cr Ni Mo
.362* r024 .018 MECHANICAL ANALYSIS BARONESS UTS 0.2XYS 'EL'RA A B C
.67,68,68. 35
ATTACHHENT 2 DATA
SUMMARY
PSL ID8 030-61835-5" PSL-CHEMICAL ANALYSIS Si Cr Mo
.469 .019 .010 MECHANICAL ANALYSIS NARONESS UTS 0.2%YS XfL A 8 C 64,63. 5,64 . 27 II
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030-61840-1-PS L CHEMICAL ANALYSIS C Si, Cr Mo
.505 .017 .020 MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS %EL %RA A C 64.5,65.65. 30
ATTACHMENT 2 OATA
SUMMARY
PSL
?08 030"61845-2-PSL CHEMICAL ANALYSIS Si S Cr Mo .
.442 .024 .010 MECHANICAL ANALYSIS RARORESS UTS 0.2XYS %EL %RA A B C 66,66,65.5. 31
ATTACHMENT 2 DATA
SUMMARY
PSL E08 030-92110-4A-PSL
'i CHEMICAL ANALYSIS I
C Mn I
Cr Mo
.063 "
1;60', .69 .008 '8.58 '013 9.02 MECHANICAL ANALYSIS HARORESS UTS 0.2XYS %EL XRA A C 49,49,49.5 79
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030"92110"48" PSL CHEMICAL ANALYSIS I
"C, Mn Si. S Ct I
1
.065 1.45 .66 .01$ ~ 012 18 23 "8 ~ 53 MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS %EL %RA A B C 45,47.5,49.5. 76.0
ATTACHMENT 2 DATA
SUMMARY
PSL I08 030-92120-1-PSL II CHEMICAL ANALYSIS C i4ln Si P Cr. Mo.
.043 1.48 .47 .007 .012 18.10 9.15 MECHANICAL ANALYSIS HARDNESS UTS D. 2XYS %EL A C 66,65,$ 6. 32
ATTACHHENT 2 DATA SUHMARY PSL I08 030 "92140-6-PSL CHENI GAL ANALYSIS Si P'011 S,Cr, Ni Ho
.048 1.46 .55 .018 '18.14 9.46 HECHANICAL . ANALYSI S HARDNESS UTS 0.2XYS /aRA C
1038HN '9.2 50.0 80.9 75;0
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030-92145-7-PSL CHEMICAL ANALYSIS Mn Si S Cr ~ Mo
.065 1.49 .62 .Oll .028 18.26 9.02 MECHANICAL ANALYSIS BARONESS UTS 0.2XYS %EL 'ERA A B 48,46.5,46.5. 127 BHN 97.1 43.3 54.5 75.0
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030-92170-8-PSL CHEMICAL ANALYSIS Si Cr Ni Mo
.067 , .80 .61 -
'..012 18.05 8.40 MECHANICAL ANALYSIS NARONESS UTS 0.2%%uYS %EL %RA A B C 49,51,50. 153 BHN 96.8 40.0 72.3- 76.0
ATTACHMENT 2 DATA
SUMMARY
PSL ID8 030-94600-0-PSL CHEMICAL ANALYSIS S Ct Mo C'030 1.45 '52 .008 17.20 11.63 2.40 MECHANICAL ANALYSIS JI HARDNESS UTS ~
0.2XYS %EL %RA A 8 66,64.5,67. I I
II 4
II I
ATTACHHENT 2 DATA SUHHARY PSL lDP 030-95000-7-PSL CHEH ICAL ANALYSIS I
Si S Cr Ni N
I
.056 1.42 .51 .005 17.03 10.72 "2 22 HECHANICAL ANALYSIS HARDNESS UTS 0.2XYS'j 'RA I
%EL II A B 68.5,68.5,67.5. 36
ATTACHMENT 2 OATA
SUMMARY
PSL ID8 030-95400-2-PSL CHEMICAL ANALYSIS
.031 Mn 1.47 Si
.62 P
.009 S'r Mo
'2.39
.010 17.11 10.65 MECHANICAL ANALYSIS HARDNESS UTS 0.2XYS XfL %RA A 8 C 68,68,68. 35
'\ ~ ply'<<. g"' ~;i w s,, y e,sew.- ~ r ",,', a>>'; ~ my 2 gq E r w ~ .' ~ ~ r ew a ~ << ~
ATTACHMENT 2 OATA SUHHARY PSL
?08 031-15700-9-PSL CHEMICAL ANALYSIS Mn Si Cr Ni Ho
.080 1.45 .55 .014 .008 17.15 11.48 2.28 MECHANICAL ANALYSI S HARONESS UTS 0.2XYS %EL %RA A B C 71,70,71. 41 ttttt +++++
ATTACHMENT 2 OATA
SUMMARY
PSL j08 031-24600-1-PSL CHEMICAL ANALYSIS C Si Cl" Ni Mo
.043 1.62 .26 .008 .025 "
17.06 10.66 2.29 MECHANICAL ANALYSIS NARONESS UTS 0.2XYS %EL %RA A 8 59,59,59. 96 101.2 85.6 15.6* 72.0
ATTACHMENT 2 OATA
SUMMARY
PSL I08 031-27200-2-PSL CHEMICAL ANALYSIS Il Si Cr Mo
.028 1.63 .53 .007 .013 17.11 12.95 2.28 MECHANICAL ANALYSIS NARONESS UTS 0.2XYS %EL %RA A
54,55.5 55.5. 90 85.7, 58.2 54.4 77.6
ATTACHMENT 2 DATA
SUMMARY
PSL I08 031-27600-8-PSL CHEMICAL ANALYSIS Mn Si P ' Cr Mo
.031 1.60 .68 .007 .017 17.20 12.12 2.40 MECHANICAL ANALYSIS HARONESS =UTS 0.2XYS %RA A C 64,63,65. 28 88". 8 56.0 57.1 80.0
ATTACHMENT 2 DATA
SUMMARY
PSL
.ID8 ., 031-32800-8-PSL CHEMICAL ANALYSIS C Si Mo
'.010,17.40 Ct'008
078 1.73 .53 ;
12.07 MECHANICAL ANALYSIS BARONESS UTS 0.2XYS %EL A C 46.5,46.5,47. 139 BHN 83.7 34.5 77.5 77.6
ATTACHMENT 2 DATA
SUMMARY
PSL ID'31-34500-0-PSL CHEMICAL ANALYSIS 4 I
C Mn Si Cr Mo
.062 1.53 .71 .009 .030 17.10 12.42 2.31 HECHANICAL ANALYSIS HARDNESS UTS 0.2XYS %EL %RA A 8 55,54,54. 88 95.2 58.0 53.7 76.0
QUALITYASSURANCE MANUAL Proc. No. QP 0.1 Rev.
CONTROL OF PROCUREMENT 18 ORIGINATED BY OPERATING ete POWER 4 LIGHT COMPANY PLANT PERSONNEL january 31'986 Pe9e 32 APPENDIX C DEFINITION OR PROCUREMENT C ii conditions exist:
i: ihi if' UALITYLEVELS:
'h II 1 <<\ ig The item is for use in or in conjunction with a safety related system and the item or service does not meet the definition of a commercial grade item.
~,
2. It is desired to,upgrade an item, or assure that only a supplier with an. approved nuclear QA Program is used.
h
3. Doubt exists as to the Quality Assurance Program requirements to be imposed.
1-2 Classification: This classification should be used when one ofi.the following conditions exist:
The item is for use in or. in conjunction with a. safety related system and meets the definition of a commercial grade item and documentation (e.g., mill test reports, certification of compliance, chemical or physical test reports, heat treat certification, reports of inspection, etc) is required.
2. The item is for use in or in conjunction with a safety related-system and meets the definition of a commercial grade item and the functional or material characteristics of the item cannot be verified upon 'receipt inspection or post t installation testing.
3.'tto is desired to upgrade an item meeting the definition of commercial grade item or
-3 ii conditions are met:
I ii i b 1 <<I assure that only a supplier approved by Quality Assurance is used for purchase.
'i: Tti ig
1. The item'is for use in or in conjunction with a safety related system and meets the definition of a commercial grade item and no documentation is required by design related documents. Documentation for elastomeric compounds (i.e., QCN 6S) may be obtained under QL-3.
2. The item is for use in or in conjunction with a safety related system and meets the.
-definition of a commercial grade item and the functional or material characteristics of the item can be verified upon receipt inspection or post.
installation testing.
The item is for use in or in conjunction with fire protection equipment or components that are subject to other QA Program requirements.
It is desired to upgrade the item to obtain a QC receiving inspection.
T7 1 -AJ QUALITYASSURANCE MANUAL Proc. No. QP O.l Rev.
CONTROL OF PROCUREMENT ORIGINATED BY OPERATING A POWER 8 LIGHT COMPANY PLANT PERSONNEL 3anuary 31, 1986 e9e 32 APPENDIX C DEFINITION OR PROCUREMENT UALITYLEVELS:
I conditions exist: "
"a The item is for use in or in conjunction with a safety related system and the item or service does not meet the definition of a commercial grade item.
V
2. 'It is desired to upgrade, an ite'm or assure that only a supplier'ith an approved I
E nuclear QA Program is used.
'.'3 I
~ Doubt exists as to the Quality Assurance Program requirements to be imposed.
ig conditions exist:
The item is for use in or in conjunction with a. safety related system and meets the definition of a commercial grade item and documentation (e.g., mill test reports, certification of compliance, chemical or physical test reports, heat treat certification, reports of inspection, etc) is required.
2. The item is<or use in or in conjunction with a safety related system and meets the definition of a commercial grade item and the functional or material characteristics of the item cannot be verified upon receipt inspection or post installation testing.
3. It is desired to upgrade an item meeting the definition of commercial grade item or 1M>>Y to assure that only a supplier approved by Quality Assurance is used for purchase.
conditions are met:
ig
l. The item is for use in or in conjunction with a safety related system and meets the definition of a commercial grade item and no documentation is required by design related documents. Documentation for elastomeric compounds (i.e., QCN 6S) may be obtained under QL-3.
2. The item is for use in or in conjunction with a safety related system and meets the definition of a commercial grade item and the functional or material characteristics of the item can be verified upon receipt inspection or post installation testing.
The item is for use in or in conjunction with fire protection equipment or components that-are subject to other QA Program requirements.
It is desired to upgrade the item to obtain a QC receiving inspection.
PI C. bin QUALITYASSURANCE MANUAL Proc. No. QP O.l Rev.
CONTROL OF PROCUREMENT ORIGINATED BY OPERATING Date FLORIDA POWER t LIGHT COMPANY PLANT PERSONNEL January 3 l, f9gI Page 33 Gf APPENDIX C (Cont'd)
Not L-1 2 3 Classification: This classification shall only be used for items or services that are not tclassified as, QL-l, QL-,2, or QL-3. "This may include a part of a safety related item, if that- part is determined to be not safety related based on design related documents.
I A commercial grade item is defined as an item that:
Ie
l. Is not subject to design or specification requirements that are unique'to facilities or
'activities licensed by the NRC, ~and '
e t
2. Is used in applications other than'acihties or activities licensed by the NRC, ~and t
3. Can be ordered from the manufacturer on the basis of specifications set forth in the manufacturer's published product description (e.g., a catalog).
Items classified as QL-1, QL-2, or QL-3 require a QC receipt inspection in addition to the normal stores department receiving inspection. QC inspections shall be accomplished in accordance with QP 7.1.
NOTE: For additional guidance on determining quality levels, refer to Appendix Bg.
E z
et ee o
I~
.C, M- 3 QUALITYASSURANCE MANUAL Proc. No. QP 0.1 Rev.
CONTROL OF PROCUREMENT ORIGINATED BY OPERATING POWER IL LIGHT COMPANY PLANT PERSONNEL January 31, 1986 Page Gf 3q APPENDIX D UALITY RE UIREMENTS (ALTERNATE TO S ADS)
Normally the following SQADs are referenced on procurement documents classified as QL-1 or QL-2:
Documentation QL-1 QL-2 Referenced by QCN Optional
'tems SQAD 1001,1002 SQAD 1006 Add SQAD 1005 SQAD 1000.
Services SQAD 1003,1002+ 'SQAD '1006 Add SQAD 1005 SQAD 1000j 1
+Include SQAD 1001 if materials are also provided aC QL-l.
+Include SQAD 1006 if materials are also provided as QL-2.
As an alternative to, referencing SQADs for QL-1 or QL-2, the following shall be specified if applicable to the item or service:
Requirements for the supplier to have a documented Quality Assurance Program that implements the applicable portions of 10CRF50, Appendix B, ANSI N05.2, ASME Section III, NCA sections, or AINSI daughter standards (this requirement not applicable to QL-2.
2. Right of access for inspection or audit by FPL or designee. This requirement should also include the identification of, or method for identification of witness and hold points, if applicable.
3. Specific requirements shall identify the documentation to be submitted, including Quality Assurance records for information, review, or approval.
The method for reporting and requirements for approving nonconformances shall be specified. IVonconformance reports shall include corrective action to be taken.
5. The requirement that the supplier shall include the appropriate Quality Assurance requirements in all lower tier purchases or supply a copy of the FPL purchase order to the subtier's.
FLOIMOA KWVER L UOHf COMPANY QL.-2 QUALITY REQUIRENENTS FOR
,CONÃERCIAL GRADE ITB5 AND SERYICES FOR NUCLEAR PLANT USE Ro ,THE ENCLOSED SPECIAL QA DOCUHENTS (SQADS) SHALL BE APPLIED To 'LL,PURCHASED ITEMS OR SERVICES ONLY IN THE FPL PURCHASE'RDER OR CONTRACT DOCUNENTS ~
ALL ITENS OR SERVICES MHERE SQAD 1006 HAS BEEN REFERENCED IN THE PURCHASE ORDER OR CONTRACT DOCUMENTS SHALL BE PROVIDED UNDER YOUR QUALITY PR06RN AS APPROVED BY, FPL.
IF YOU HAVE NORE THAN ONE QUALITY PR06RNi 'THE PROGRAH WHICH NEETS OR EXCEEDS THE NININUN QA REaUIRENENTS FOR THE ITENS OR SERVICES SHALL BE APPLIEDa 0 COMMERCIAL GRADE WHEN SQAD 1005 ITEllS OR SERVICES SHALL BE PROVIDED IS SPECIFIED IN THE PURCHASE ORDER e
~ .
COEOERCIOC OIIOOE IVIES OR SERVICES SRLLJIOI OE PROVISOS WHEN SQAD 1001 OR SQAD 1003 ARE SPECIFIEDs FPL QUALITY ASSURANCE PROCURENENT & RELIABILITY I 'V'I V
CONTENTS I
I ~ I SOAO 1066@ REvo 1 'UALITY REQU I RESENTS "
FOR CONNERC I AL 6RADE ITEMS AND SERVICES SQAD 1000, Rfv. 3 SURvEILLANcE REQUIRENENTs I I SSS 1005 'EV ~ 2 STANDARD OVALI TY CONTROL NOT I CES SOAD,1999, REvs.3 'REFERENcEs, DEF INITIoNsi ABBREYIATIQNs AND
'ORNS SUPPL'IER DEYIATIoN NoTIcE FoR@ 3526 REv. 1/80 VPt '4.l ~' "+.4 ~
SPECIAI QUAI XTT ASSUaaWCE DOCUMENT . SHAD 1006,.
Rev.
QUAINT REQUIREaanTS ZOR FLORtOA POWER d L~ ~~ COMMERCIhL GRADE ITEMS ADSERVICES Date
'j/(j1/84'age 1 of , 2 LO hPPBOVhL: referenced on the Request for Quote (RFQ) or PO.
Approyed by>
PURPOSELY Manager QA ervices Sales Offices and Distributorss
~
3.0 As the Primary SuppHer, a sales office, and when requested, distributors, shall. furnish This Special Quality Assurance Document to the appropriate FPL Purchasing Agent, (SQAD) establishes the minimum Quality the names and addresses of their sub-tier Assurance (QA) requirements that are to suppliers and manufacturers of items This be satisfied by Suppliers of commercial requirement shall apply whether items are .
'grade items. These requirements may be shipped directly from their sub-tier supplemented by other technical or, supplier or manufacturer (as, in the ease of specialized requirements pertinent to the , a salei office) or. when another facility of '
item or service. the., Primary Supplier acts as a sub-tier supplier.
3.0 APPLICABILITY'he Right of Accam requirements of tMs SQAD are mandatory for those SuppHers awarded During the Procurement process (from the
'ontracts or Purchase Orders (POs) that fnltial RFQ through final payment for the reference SQAD 1006. Although services renderec9, FPL, its agents or considered commercial grade, the items or ass~ shall have the right to,inspect and services referenced shall be provided under evaluate the Supplier's faeiH ties and a quality program as specified in Section activities. This right shall extend to sub-4.5 of this SQAD. tler suppHers and. will be coordinated through the Primary Supplier. QA The item or service for which this SQAD Is inspections, surveiHanees, tests or audits referenced is commercial grade. An item'r performed by FPL shall in no way relieve service is considered to be "commercial the Supplier of any responsibOities under grade" when< the PO.
l. It fs not subsect to design or specification requirements that are unique to facHities or activities The Supplier shall be responsible for licensed by the Nuclear Regulatory emring that aH sub-tier supp Hers Commission (NRC), AND implement an adequate QA Program, as appHcable. The Supplier shall either
2. It is used in applications other than maintain documentation of the evaluation faciHties and activities licensed by the and acceptance of sub-tier suppliers'A Nuclear Regulatory Commission, AND programs or use FPL QA approved suppliers only. When a sub-tier supplier is
3. It is to be ordered from the Supplier used, aH technical and quality on the basis of specifications set forth requirements imposed in the FPL PO in their published product description and/or supplement shaH be transmitted to such as a catalog. .the sub-tier supplier, whether the sub-tier ts specifieaHy identified in the In the event of a confHct between these PO/supplement or not.
SQAD requirements and those in the PO, the PO requirements take precedence. Exceptions.
3.3 AH correspondence related to the PO shaH If a bidder takes exception to any item in be directed to the FPL Purchasing Agent the specification, said exception shall be presented in writing under a caption
t +w e ~ ." ~ ' s. ~ 4 4' I SPECKLE QVALITYhsSURANCB DOCUMENT 'HAD 1006 QUhIZIT REQUlRHMENTS POR Rev. 1 COMMERCIALGRAQE GEMS Date 11~01 lOA POWER 4 OQHT COI5%NY AND SERmCZ ot paragraph titled, "EXCEPTIONS". The exceptions shall reference the speciffc items or paragraphs by number.
45 Quality Assurance Programs The Supplier shall assure that the item or provided fs controned under a 'ervice quality assurance program acceptable to FPL QA This program, as a minfmum, shall contain procedur est controfst processes, etc., necessary to assure FPL that the item or service being,'supplied meets industry standardst'PL PO requirements, and performance or technical requirements specftfed fn the suppUer's catalog.
Documentatfon requirements are specfffed on the PO, the FPL Suppliers Records/Documentation Checklist" (Form
$ 3524), or 'ther applfcable PO attachments.
41 Noaconformfng Itemsc Any devfation from the PO specfficatfons shall be reported. Theie devfatfons shall be submitted to FPL for review and acceptance on the FPL "SuppUer Deviation Notice" (Form 43528). The Supplier shall not ship the item to FPL until the Supplier Eevfatfon Notice has been dfsposftfoned and accepted by FPI>>
5 0 REFEREE DBFINIFIO RBVIATION AND FORMSt See SQAD 1999.
SURVEn uurCE Rev. 3 lualUHESIMS Date l1/0>/84 FLORIQA POWER a LIGHT COMPANY Page 1 oi 2 I
1.0 APPROVAL< a scheduled hold point The hold point shall not be performed and work shall not Approved by! proceed beyond that point until the FPL representative is present, unless FPL QAP waives the right of surveQlance.
QA vices 44 Notificsstioas
~ 2.0 PURP OSEc I 1. Notification of reaching a surveiHance I'anager This Special QuaHty Assurance Document (SQAD) establLhes minimum requirements point and the conditions covering these points are governed by sections for witness or hold points that are subject 4.1 and 4.2 of this SQAD.
to FPL surveUlance at the Supplier's faciHty. 2. Reco~ procedure drawings, etc.,
I necessary to pertorm the process to be 3.0 APPLICABHZPYs surveilled which require FPL approval, I
~ 'hould have been approved prior to The requirements of this SQAD shall be arrival ot the FPL surveillance mandatory for SuppJers when referenced representative. All such documents ML-h an FPL Purchase Order (PO). shall be readily available for review by the FPL surveiHance representative.
,4.0
3. Notification of an upcoming FPL shall identity surveillance surveiHance point to FPL QAP should, events/intervals as being "hold points" or as a minimum, contain the foHowing "witness points". These surveillance points inform ations shell be identified in the. FPL PO as followss a FPL PO Number
b. PO Supplement(s)
Witness Point (or Hold Point) c. PO Lhe item Description ot event/intervaL
Quantity of items to be surveilled and estimated length of time Examples necessary to complete
e. Expected shipping date Hold'Points t. Planned surveiHance date i Hydrostatic Test of Complete Valve. g. Additional FPL work in progress.
I Pl .'WTX'NESS POINTs 4. Notification shall be addressed to the I QA Supervising Engineer identified in F PL QA Procurement and ReHabiHty the FPL PO.
(QAPRR) shall be notified in writing or by phone by the SuppHer at least tive (5) tull Notes The satistactory completion of a working days prior to reaching a scheduled witness or hold point does not witness point. Work shall not be delayed if constitute acceptance of a
'he FPL representative has not arrived at the appointed time. SuppHer is required to show evidence ot notification to FPL QAPRR per section 4.3.3 and 4.3.4.
I 4.2 HOLD POiNTs FPL QA Procurement R Reliability shall be notified in writing or by phone by the SuppHer at least five (5) full working days prior to reaching
SPECIAL QUAXZITASSURANCE DOCURQQiT SHAD 1004 I
SURVEILLANCE Rev. 3 IIIII IIIMmIIS Date li/01/84 RIOA POWER a UGHT COMPANY pe9e 2 of 2 product, nor does it alleviate the responsibility of the Supplier to comply with PO andI specification requirements
"'4.4 'Pfaivers."
I All waivers for identified witnessor hold points shallt be obtained in writing from FPL's QA Procurement 4 ReliabGity Department. Verbal 'waivers may be obtained from qualified QA Procurement dc Relhbility Department personnel, ~,
however, all such waivers shall be followed
( by written confirmation and shall j be maintained with the SuplIHers records.
I
.I 4.5 FaihIre to Comply'ailure of the Supplier to comply with these requirements I, or,'otify FPL of witness or hold points )may result in rejection'f the'product or may require retesting or reinspection of the product in the pre'sence of an FPL repjesentative.
6: NatteatNmmanceu I Nonconformances, that are detected through surveillance shall be controlled in accordance with! the provisions of:,
esgbnshed Suppliek procedIn',~ or, should a Supplier p1hh FPii to evaluate a deviation from," a PO requirement,! a "Supplier .
Deviation Notice" (FPL Form ¹3528) shall be 'ubmitted to the responsible FPL Purchasing Agent identified in the PO.
5.0 REFERENC DEFINITIO ABBREVIATIONSAND FORK%
See SQAO 1999.
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SHAD 1005 Rev.
STANDARD qUmgT CONTROL NOTfCBS '" ZZgovg84 FLORIOA POWER a I.IGHT COMPANY age I " 10 10 APP RO VhLa 4.2 Documentation Quality Approved bys All documents submitted shall be of the following reproduction quality:
Manager QA ry ces a ak x ll Documents: Legible black and white copy suitable for ",electrostatic 2.0 PURPOSEs copier reproduction and microfilming. l This Special Quality Assurance Document b. Larger documents and drawings: (1)
(SQAD) estabiishes Standard Quality Direct reading - autopositive, (2)
Control Notices (QCNs) which convey to Vellum, (3) tracing paper type, (4)
Suppliers frequently used quality direct reading reproducible of no .
requirements. This does not preclude the lesser quality than autopositive able to use of other instructions that are imposed produce clear, sharp and legible prints by Purchase Order (PO) upon the product and micro-reproductions 'ach or service performed by the Supplier. reproducible drawing shall include a 4" margin on the right side of the sheet APPLICAHIIZITs for purchaser disposition information.,
All reproducibles must be rolled, not folded.
lt The requirements of this SQAD are SIgnature Restuire ments on Supplier mandatory for those Suppliers which are Certiflcatfons axl ~arts awarded POs which reference this SQAD.
Only those QCN(s) which are specifically All certificates and reports, shall have the, referenced in the PO or which are approprhte level of approval consistent',
referenced on FPL "Supplier with the quality level placed on the )
Records/Documentation Checklist" (Form purchased item. The date, and the title of
¹3524) willapply. the responsible individual shall appear on the document. Failure to comply with the, signature requirements will result In I refection of documentation provided. Finalt The QCNs shall apply when specified by payment Is contingent upon receipt of~
FPL PO; however, the PO, specification, acceptable documentatism. The following and Code requirements take precedence guidelines are to be used wh'en approving over these requirements in the event of a such documents: I conflict or omission. Conflicts or E atten on ot the report provided by the Supplier shall be signed by a qualified individual in their Quality Assurance organization.
Commercial Grade ( L-2)s We certificate Supplier Documentatka Submittalss or report provided by the Supplier shall be signed by an individual in their Quality Unless otherwise specified by the PO, the organization; a supervisor, officer, or other Supplier may use a format compatibIe with ~ individual whose title re fico ts their documentation system, provided all responsibility and cognizance for the applicable requirements of the PO and its Company's product.
references are met. The document shall reference the FPL PO number (and item 44 QCN Identification Systems number, if required to assure traceability).
Each QCN Is identified by a unique alpha-numeric code number. It Is this code
d W III% E1 r 4 ~ I SPanAL qUALmrr ASSURANCE OOCUMmV SHAD 1005 Rev.
Srmnmn qadi,rTT CONTROL NCYQCES 11/01/84 ORIOA POWFR a UGHT COMPANY Page ot 2
number which will be identified in the PO QCN 4P Contaminant Content and or contract and which will identify those Limitation QCN(s) which are appHcable to a particular PO or contract. Examples The QCN code number for a Mechanical Test Report is 4B. QCN -
2P . Seat Leak Test Valves QCN 4C ASME Code Data Reports 5.0 SThNDARD UALITTCONTROL QCN 4P Hydrostatic Test Report NOTICES CN s INDEX QCN 4U Performance - Mechanical 'I 5.1 5 5 Electrical QCN 3A ANSI B31.1 QCN 4N Performance - Electrical QCN 3B ANSI B31.7 QCN 6J Envi'ronmental QuaHficatfon.
QCN 3C ASME Section IH Statement QCN 3G FPL QC Site SurveiHance QCN 4E Certificate of Conformance 5.6 Welding QCN 4L Drawings
'CN 4M Packaging/Shipping/Storage/, QCN VA Welder QuaHficatfons HandHng QCN 7B Weld Repair Maps QCN 4T Certificate of CaHbration QCN VC Welding'Procedure QCN 4W Certificate ot Seismic QuaHfications QuaHf ication QCN VD Welding Material Certifications QCN 4Y Certificate of CompHance QCN VE Welding Procedure QCN 4Z Vendor's QC Release Report Specifications QCN 5E Temperature or Humidity Sensitive Materials QCN SP Repair or Rework Procedures QCN 6D Spechl Requirements QCN SG Certificate of Repair or Rework QCN 8B Technical or Instruction Manuals 6.0 . STANDARD UhLTFF CONTROL QCN 8S Shelf Life C CNs M NTS 5.2 Non-Destructive Examinations QCN 2B Magnetic Particle Report - ASME Section V QCN 2B Magnetic Particle Report QCN 2C Ultrasonic Examination Report Each item or material ordered for QCN 2D Liquid Penetrant Examination which this QCN is specified requires a Report "Magnetic Particle Test Report".
QCN 2E Visual Examination Report Examination procedures shall conform QCN '2G Eddy Current Examination with the requirements of the ASME B Report 8s PV Code, Section.V, Article 7 and QCN 4G Radiography - Piim and mandatory Addenda as specified in the Interpretation Report PO. Examination and reporting shall QCN 4H Radiography - Interpretation conform with the requirements of the Report Only , ASME B 8c PV Code (or other code) as specified in the PO. Each report shall 5.3 Material include the name of the reader, signature, and level of certification to QCN 4A Chemical Test Report the requirements of SNT-TC-1A.
QCN 4B Mechanical Test Report QCN 4D Certified Material Test Report QCN 2C Ultrasoaic Ezamfnation Report- ASME QCN 4J Heat Treatment Charts Section V QCN 4K Heat Treatment Certification Each item or material ordered for which this QCN is specified requires an "Ultrasonic Test Report".
Examination procedures shall conform O
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SrmsmO qvmrrr Rev.
CONTROL NOTICES '" iiloil84 FLORIDA POWEA a LIGHT COMPANY P898 3 of $0 with the requirements of the ASME B hydrostatfc test pressure duratfon and dc PV Code,Section V, Article 5 and amount of leakage per unit time. This mandatory Addenda as specified in the. certificate (which may be Included in PO. Examinatfon and reporting shall "Certfffcate of Hydrostatic Testfng")
conform with the requirements of'he shall indicate the name of the ASME B Ik PV Code (or other code) as individual performing the test, and specified in the PO. Each report shall signature. Seat leak testing include the name of the reader, procedures and acceptance criteria signature, and level of certification to shall conform with the requirements the requirements of SNT-TC-1A. of the Code as specffied fn the FPL PO or its references.
QCN 2D Liquid Penetrant Examfnatioa Report
- ASME Seetfoa V QCN 26 Eddy Current Examination Report-ASME Section V Each item or material ordered for which thfs QCN Is specified requires a Each item or material ordered for "Liquid Penetrant Test Report". whfeh this QCN is specified requires Examhation procedures shall conform an. "Eddy Current Test Report".
with the requirements of the ASME B Examination procedures shall ccnform 4 PV Code,Section V, Artfele 6 and with the requirements o! the ASME B mandatory Addenda as specified in the dt PV Code,Section V, Article 8 and PO. Examfnatfon and reporting shall mandatory addenda as speefffed in the conform with the requirements of the PO- Examfnatfon and reporting shall ASME B 8 PV Code (or other code) as conform wfth the requirements of the specified in the PO. Each report shall ASME B 4 PV Code (or other code) as fnclude the name of the reader, specfffed in the PO. Each report shall signature, and level of certification to fnclude the name of the reader, the requfrements of SNT-TC-1A. sfgnature and level of certification to the requirements of SNT-TC-1A.
QCN 2E Vfsual Examfnatfoa Repact - ASME Sectloa V QCN 3A Each item or material ordered for Each item ordered for whfeh this QCN whfeh this QCN is specified requires a Is specified, shall be manufactured, "Visual Examination Test 3teport". examined, tested> and certified in Examination procedures shall conform accordance wfth the ANSI B31.1 Code with the requirements of the ASME B and Addenda specified fn the FPL PO R PV Code, Seetfon V, Article,9 and and Its references.
mandatory Addenda as specified in the PO. Examination and reporting shall QCN 3B conform with the requfrements of this ASME B 4 PV Code (or other code) as Each item ordered for which thfs QCN specified in the PO. Each report shall Is specified, shall be manufactured, include the name of the reader, examined, tested and certified in signature, and level of certification to accordance with the ANSI B31.7 Code, the requirements of SNT-TC-1A. Addenda, and classification speciffed in the PPL PO and fts references-QCN 2P Seat Leak Test - Valves QCN 3C Each item or material ordered for which this QCN is specified requires a Each item ordered for which this QCN "Certification of Seat Leak Test". Is specified, shall be manufactured, This certificate shall indicate the examined, =-
tested and certified in
SPBCThL QUhIZIY k8SURANCB DOCUMENT SHAD 1005 WENDED QUAINT Rev.
CONTROL NOTICES '" iiloZIS4 AIOA PQWER d LIGHT COMPANY P898 Gf 4 ]0 accordance with the ASME Section IH QCN 4D Certified Material Test Report B 8c PV Code Edition, Addenda, and classification ~ecified in the FPL PO Each item ordered for which this QCN and its references. is specified shall require a Certified Material Test Report (CMTR),
QCN 3G FPL Quality Control Site Surveillance traceable by heat or code number to the item furnished, to accompany the Supplier services performed at the shipment The CMTR must be FPL site shall be subject to FPL provided by the material manufacturer Quality Control (QC) and or Quality certifying the item to codes and Assurance (QA) Depa-tment specifications including code date and surveillance. addenda specified in the FPL PO and its references The CNTR shall QCN 4A Chemical Test Report contain specific examination and test results required by codes "
and Each item ordered for which this QCN specifications referenced in the FPL is specified requires a "Certified PO and its references." Analysis, Actual Chemical Test Report" (Ladle examinati~ and, tests for ASME or Product as required by spec.) Section III materials shall be traceable to the lot, batch or heat of performed under an NCA 3800 (ASME) material or serial number of the item program approved by the for which it was generated.. This manufacturer providing the report shall include an analysis of the Certificate quantities of all elements required by e the material specification referenced CMTRs provided by the manufacturer in the FPL PO and its references. The for ASME Section III and ANSI B31.7.
report shall reference the PO number items shall specify the code, class and (and item number, if required to addenda to which the item is being assure traceabiiity). certified in addition to identifying the ASME Quality System Certificate QCN 4B Mechanical Test Report number or QA program. revision number and date under which the Each item ordered for which this QQN material is supplied.
is specified requires a Certified Actual Mechanical Test Report" Certificate of Conformance traceable to the lot> batch or heat of material or serial number of the item Each item ordered for which this QCN for which it was generated. This is specified requires a "Certificate of report shall include an analysis of the Conformance". This certificate shall hysical properties and heat treatment certify that the item conforms to the if applicable) as required by the FPL PO and tts references The date, material specification referenced in title, and signature of a responsible the FPL PO and its references. The individual fn the Supplier's QA report shall reference the PO number organization shall appear indicating (and item number, if required to acceptance of the certificate. The assure traceability). certificate(s) shall reference the PO number (and item number, if required QCN 4C to assure traceabiiity).
Each item ordered for which this QCN QCN 4F Hydrostatic Test Report (Pump is specified requires an appropriate Valve Sbeiit Pipe)
AS ME Code Data Report, properly executed, be supplied Each item or material ordered for which this QCN is specified requires a z
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QUAIiFLT MSURhHCB BGCUMENT'QAD 1005 Rev.
Sl'hNDABD QUALLEVT FLORIOA POWER a UGHT COMPANY CONTROL NOTICES 11/01/84 Page of 5 10 "Certificate of Hydrostatic Test". fnterpretatfon reports only shall This certificate shall indicate the accompany shipment. The hydrostatic test pressure, interpretation reports shall include temperature, test medium (analysis), disposition (accept or reject),
duration at pressure, the number and procedure number and technique revision of the procedure used and the used, a method of identifying and results of the test including leakage cross-reterencing each film rates (if allowed) and shall be in exposure to the interpretation accordance with the code specified in report and the item including serial the FPL PO and its references. This numbers where required by PO.
"Certification of Hydrostatic Test" Each report shall include the name:
may be included in the "Material Test of the reader, signature, and level Report" for material furnished. of certification to thy requhements of SNT-TC-1A. The
, QCN 46'adiography - FQm and fnterpretaUon Supplier is required to keep the Regxat radiographic fQm,. traceable to the interpretation report, in records
, Each item or material ordered for storage area. This area shall be which this QCN Is specified requires sufficiently designed to provide radiographic examination. Examina- adequate temperature and tion procedures shall conform with the humidity condiUons suitable for requirements o! the code specified in radiographic fQm and shall protect the FPL PO and its references. the fQm from deterioration Radiographic fQm and interpre- QCN 4J Heat ament Charts taUon reports shall accompany shipment, or at FPL's option, be . Each item or material ordered for submitted for review prior to which this QCN is specified requires a shipment The interpretaUon ocr Utied copy of the actual heat reports shall include disposition treatment chart(s). Each chart shall (accept or reject), procedure reference the FPL PO number, the number and technique used, a charging time, rate, temperature, method of identifying and cross- cooling time, quench time, as referencing each fQm exposure to applicable, and should include any the interpretation report end the other perUnent data on the process item including serial numbers when required to assure traceability or QCN 4K Heat Treatment CerUficaUon when required by PO.
Radiographic film shall be Each item or material ordered tor packaged to prevent damage both which this QCN is specified requires a in shipment and in storage. Each "Certificate of Heat Treatment". This report shall include the name of certification shall include a summary the reader, signature, and level of description ot the heat treatment time certitication to the requirements and temperature data. The certificate of SNT-TC-lA. shall reference the FPL PO number (and item numbec, it required to QCN 48 Radiography. - Interpretation Report assure traceability).
Only QCN 4L Drawings Each item or material ordered for which this QCN is specified requires Each item ordered for which this QCN radiographic examination. Examina- is specified requires outline end/or tion procedures shall contorm with the certified drawings. These drawings requirements ot the code specified in shall include the toQowing:
the FPL PO and its references.
8PECIhXi QUAINT k8SURANCE DOCUHZNT , SQAD 1005 Rcv.
SMNDARD QUALITY CONTROL NOTICES 11/01/84 ea paw@a ac~COV~V f'<<6 of 10 a Outline drawings a No mercury, lead, or other heavy metal, or low meltfng point The Supplier shall submit general elements 'were used in the arrangement or outline drawings processing of these materials.
that wfil be used and relied upon fn the preparation of engfneerfng b. 'No elements known to be harmful and fInal construction drawings. to stainless steel and nickel These drawings must show the allo~ such as leachable sulfides approximate weight and . all or chloride, were used in. the principle dimensions of the processing of these materials~
equipment including size and locatfon of mounting bolts and If any of the above elements are outsfde electr fcal and piping present in the material to be connections. delfvercd, a chemfcal test report (see I QCN 4A) certffying amounts (ppm) of
b. Certified drawings such elements shall be Included with the shfpment. Copies of the test The SuppUer shall submit a reports shall be transmitted to the certified as-built drawing when responsible FPL Purchasing Agent required by PO, Specification, or prfor to shipment to obtain FPL.
Code Engineering approval, unless otherwfse authorized by the FPL PO and its
c. Other drawings references.
The SuppUer shall submit QCN 4T Certificate of CaUbratfon ~
additional drawings as speciffed by the PO, Spccfffcatf~ or thefr Each item ordered for which this QCN
'eferences. .fs specified requires a Certificate of CaUb ration" be provfded. The QCN4M Pa ing/StorsgeiffandUng Certificate shall contain the foliowings Each item ordered for which thfs QCN fs specff led shall be packaged, shfpp~ a FPL PO number.
stored, and handled in accordance with ANSI N45.2.2 to the levels and classes b. Delivery 4 Work Authorization specified withfn the PPL PO and its number, if applicable.
references.
c. Name of the item calibrated QCN 4N Performance - Electrical
d. Model number of the item Each ite'm ordered for which this QCN calfbrated, ff applicable.
fs specf fied requires an Electrfcal Performance Report. This report shall e. Serial number or PPL materfal certify that testfng required by the tag number of the item FPL, PO and its references was caUbrated.
performed and the results are documented and acceptable. f. Accuracy of the item calibrated
'expressed in commonly used and QCN 4P Contaminant Content and Lfmftatfoa industry accepted terminology.
Each item or material ordered for g. Statement of traceabiUty to the whfch this QCN fs specified requires Natfonal Bureau of Standards that a ",Certfffcate of Conformance" (NBS) or other nat tonally be provided attesting to the following: recognized agency. (If other than Ol I OI
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QUALMYASSURANCE DOCUMENT SHAD 1005, SrANDARD qVALrrr Rev.
CONTROL NOTICES 11/01/84 FLORIOA POWER d UGHT COMPANY 10 the NBS, this agency shall be calibrated fs within the specified specified.) accuracy in all operating ranges.
h. If the item calibrated has a range If the item submitted for of opemtf~ a separate recalibration is found to have calibration data attachment'shall been out of calibration fn the "as be furnished, identified with tomxP condftion, this also shall be items "a" through "e" above and clearly fndicated on the shall show &t least five (5) points certificate.
of calibratfon of that operating range unless otherwise specified The document shall reference the FPL in the PO. The fIrst point shall be PO number (and ftem number, if specified as being the low end of required to assure traceability).
the range 'of operation and the fifth point specified as being the 'CN 4U Performance ~ Mechanical hfgh end of the range of operation. Each item ordered for which this QCN fs specified requires certified test if th item 'mac rated report and data that testing was multfple ranges of operatf~ the performed in accordance with the PO calibration data attachment (as and specification requirements and specified in "h" above) shall be that test results are satisfactory. The furnished for each, operating document shall reference the FPL PO f angelo number and item number to assure traceabiHty.
If the item calibrated fs a dfgital instrument'with multfple ranges, QCN iW CertifIcate of Seismic QuaHffcatfon the caHbration data attachment shall be furnished, fdentfffed with Each item ordered for which this QCN items "a" through "e" above, and fs referenced shall require the Supplier shall show one range calibrated to to provide a certfficatfon of seismic at lease five (5) points on that quaHffeation certifying that each item range. All other ranges shall be compHes with the seismic caHbrated in accordance with requirements for the nuclear power manufacturer's p'rocedures or as a phnt lfsted in the FPL PO. and its minimum to two (2) pofnts of references. Such certification may be calibration. The first point shall performed by either method Hsted be specified as being the low 'end below.
of the range of operatfon and the I second 'point specified as being the high end of the range of
a. Prevfous ~e Testing - If thfs method fs used, the certificate operation shall certify that the item(s) deHvered hereunder is identical to If the item was submitted for the item tested.
recaHbratfoa, unless otherwise speeif fed in the PO> the b. New Item Qualiffeation - If this caHbration data attachment shall method is used, a record of FPL state the as fold or "prior to appr oval of the sefsmic recalibration" readings and the qualfffcation test procedure shall "after caHbration" readings. accompany the eertffieate. Such (Both as specified fn "f", "h", "i", certiffcation must specify which and "f" above.) It shall contain a method was used in determining statement that the item seismic qualification Each IS os E
SPECIAL QUALIFYhSSURhNCB BGCUMBNT SHAD 1005 Rev.
te CONTROL NOTICES 11/01/84 lOA POWER a UGHT COMPANY certification shall state the test QCN 4Z Vendor's QC Release Report
=number, date of test, name and address of testing - agency and Each item ordered for which this QCN shall state the seismic Hmits Is specified. requires a statement (including vertical and horizontal signed and dated by' responsibly moments) for which the item was individual in the Supplier's QA found acceptable organization. The, statement 'hall certify that the responsible individual The document shall reference the FPL has reviewed all appHcable PO number (and Item number, if documentation for adequacy prior to required to assure traceabiHty). shipment The SuppUer shall retain all associated documentation at their QCN 4Y Certificate ot CompHance faciHty, subJect to, FPL'udit and request for submittal at a later date.
Each item ordered for which this QCN The retention period shall be forty (40)
Is specified shall require the years unless disposal Is authorized by Manufacturer to provide certification FPL QA that the item shipped compUes with all requirements of the FPL PO and its QCN 5B Temperature or Humidity Sensitive references The certification shall be Materials traceable to the item furnlshec4 'as well as the'drawings and specifications Each item or material ordered for to which the item conforms A which this QCN fs specified shall statement shall be included to the require the SuppHer to identify, in a effect that the Manufacturer (or certificate, the temperature or quaHffed sub-tier) has performed all humidity storage requirements for the the ffnal inspections and tests required item or materiaL Packaging shall be to verify conformance of the items plainly marked to Identify that the shipped. The date, title, and signature item or material contained Is of a responsible individual fn the "temperature or humidity sensitive Supp Her's QA organization shall materials".
appear indicating acceptance of the certificate. The document shaH QCN 5F Repair or Rework Procedures (a, b, or reference the'FPL PO number (and c must be specified) item number, if required to assure traceabiHty).- Each item ordered for which this QCN is specified shall require the Supplier Marking on small items or its to perform repair or rework according container (which cannot be marked to the appropriate requirement individually) shall be traceable to the specified below'.
certification. Certificates of Comp Hance provided by the FPL suppUes an aproved rework manufacturer for ASME Section GI or or repair procedure referenced in ANSI B31.7 materials must, In the PO.
addition, indicate a reference to specified code, class, addenda, b.. Supp Her rework or repair material specification, type, grade, procedure which has been and heat treating of the. material previously approved by FPL for furnished. The manufacturer must the work to be accomplished specify the ASME certificate number hereunder and referenced In the and expiration date under which the PO.
material was supplied NOTE~ If the Supplier rework or repair procedure has not been
SHAD 1005 Rev.
Srmnmn qvmrrr COMHkOL NOTICES 11/01/84 FLORIOA POWER a LIGHT CoMPANY P~9e af 10 g
previously 'pproved, these ,d. Maintenance, calibration and procedures must be submitted to . lubricatfon procedures.
PPL Purchasing and approved by P PL Engineering prior to e. InstaHatton and rigging commencement of work. instructions.
e. PPL subcontractor or Archi- f. Electrical power and input tect/Engineer rework or repair 'onf tguratfon."
procedure referenced in the PO.
g. General assembly, outline dc QCN 56 Certificate of Repair or Rewarfc , detailed drawings.
Each item ordered for which this QCN h. Detailed dimensional prints where fs specffted shall require the Supplier spare parts are not available.
to provide a "Certffieate of Repair or Rework" identifyfng the foHowfngc Complete parts list with part numbers and SuppUer's name and a A desertptfon of the parts number ffe purchased item.
replaced (fncludfng part numbers).
J. Suppliers shaH identify which
b. A descrfptfon of substitute parts parts are subject to 10 CPR 21 used for replacement (including corn and which are "Co'mmercial part numbers). Grade".
c. A description of any physfeal or QCN GD Special Requirements electr feel configure tfon changes.
Each item ordered for which this QCN Perfocmance of work for ftems b and c h specified has additional above shall not be aecompHshed prior requirements beyond those contained to receiving written authorization in other QCNs. These requirements from FPL Engineering. wtH be attached-to, ar Identiffed fn the PPL PO. A certificate certifying The document shall reference the FPL plfance to these special PO number (and item number, if requirements shaH be provided by FPL required to assure traceabilfty3. and attached to the FPL PO for completion by the Supplier.
QCN SB Technical or ]hstruetfon Manuals Each item ordered for which this QCN h specif fed requires instruction/technical manual to be
'n QCN BJ Environmental ment QuaHfication Each item ordered for whtch this QCN State-provided. Twenty (20) copies of these ~is specified shall be supplied with an manuals shall be hsued as a final issue Environmental Certification ar only no later than three (3) months Qualification Test Report certifying prfor to shfpment, unless otherwise that the item has been qualified to noted. These manuals shaH include: maintain its operability with tn the requirements specified in the FPL PO a Equfpment description including and its references.
types and modeh QCN SS Shelf Life
b. Description of principle design features, especially special Each item ordered for which this QCN features h specified requires the Supplier to provide documentation identifying
c. Operating procedures, Hmits, shelf ltfe limitations, including adjustments and setpoints.
v SPBCIhX QU)LLITYhBSURANCE DOCUIIBNT SHAD 1005 Rev.
STASSram qmrzrr CONTROX NGTLCBS 11/01/84 ORIOA POWEA a UGHT COMPANY Page 10 of 10 maximum shelf life based on storage supplementary essential Code welding
~ of the item in an environment per variables w ere met during the ANSI N45.2.2, Level A, at VOoP and qualification 'rocess. The 50-55% relative humidity. Shelf life qualification report shall include expiration dates shall be marked on qualification test results.
the packaging material or as required
,by the PO or its references. items QCN TD WeldIng Material Certificaticas shall have a minimum of 7096 of recommended shelf IIfe remaining Each item or material ordered for
,prior to being sh~
otherwise indicated by the PPL PO or unless which this QCN Is specified shall require the Manufacturer to conform its references. with the requirements specified In QCN 4X (Certified Material Test QCN Th, 9feMer Qssalifications Reports) o! this SQAD.
I QCN 'TE 1VeMIng Procedure Speeiflcatices
Each",item ordered foe which this QCN I Is specified shall require the welding supplier to provide evidence of each Each item ordered for which this QCN welders'ualification in the welding Is specified shall require the welding
'rocess employed on the item supplier to provide a welding furnished. QuILIIfication shall be in procedure specification (referencing a the form of a completed and certified procedure qualification) that provides welder, or a complete welding qualification report as defined in Code/specification to which the item operator description essen~ nonessentiaL and supple-of the mentary essential welding variables was manufactured, fabricated, or described in the Code/specification installed specified in the PPL PO and its references.
QCN VB NeM Repair Maps (on Material Recydring HeM Repair)
Each item ordered for which this QCN is specified shall require the SuppHer to provide a weld map Indicating the location and extent of welding performed in the repaired area The map or sketch shall, as a minimum, show a visible unique point of reference from which the repair area(s) can be located by PPL upon re'ceipt..
QCN VC Each item ordered for which this QCN is specified shall require the Supplier to provide a Procedure Qualification Report as defIned in the Code or specification referenced in the PPL PO and its references. The procedure qualification shall include certification that appropriate Code requirements and essential and O
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~PZCIAI. qUAr.rrr ~U~CE DOCUMENT SHAD 1999 Rev. 3 REPERENCESe DEPINITIONse ABBREVIATIOHSAND FORMS Pate li/01/84 FLOR 10A POWER 4 LlGHT COMPANY 1.0 APPROVAI AS' tk PV Code:
Approved by: Boiler and Pressure Vessel Code of the American Society of Mechanical Engineers Manager QA rvices SNT-TG-1h 2.0 PURPCK~ \ Recommended Practice Number SNT-TC-1A American Society for Nondestructive This Special Quality Assurance Document Testing.
(SQAD) provides references, definitions of terms, abbreviations and sample forms that 5.0 DEFINIHONSe are used by FPL in the performance of quaUty activities during procurement he-IBuGt Drawinge activities associated with nuclear'ower plants A design drawing that depicts the final condition actually achieved in an item after 3 0 APPLICABILI'PYe implementation of any changes or
'modiflotions This SQAD provides the, definitions of term~ meaning of abbreviations and Certiflcatimc sample forms appHcable to the Special Quality Assurance Documents The terms The action of determining, verifying and of'his SQAD are supplementary to the attesting in writing to the qualifications of provisions of the PO, and in case of personnel or materiaII t.e., written conflict, the provisions of the PO shall testimony of quaUfication.
prevaiL 'onflicts shall be brought promptly to the attention of the Certified Perseeeneie appropriate F PL Purchasing Agent in writing. Persons who are periodically certified by their respective employers as being qualified to perform assigned work.
Certification is substantiated by 10CFR21e documentation that verifies education or training, testing, evaluation and periodic Title 10 of the Code of Federal review to assure initial and continuing Regulations, Part 21 "Reporting of Defects proficiencies.
and Noncompliance".
Corrective hctiexee 10CFR50, hppeexHx Be Action taken to correct a nonconforming Title 10 of the Code of Federal condition with specific emphasis on Regulations, Part 50, Appendix B, "Quality prevention of recurrence.
Assurance Criteria for Nuclear Power Plants and Fuel Reprocessing Plants". Deflciencye I
ANSI B31.1e An observed condition that fs, or appears to be, adverse to quality or beyond a American National Standards Code for defined or approved, qualitative or Pressure Piping B31.1 "Power Piping". quantitative acceptance criterion.
ANSI N45.2e American National Standard N45.2 Reports issued for deficiencies which do "Quality Assurance Program Requirements not require an engineering evaluation or for Nuclear Power Plants". are corrected by standard procedures during the normal course of construction.
SPBCIAL QUkXZIYASSURANCB DOCUMENT SHAD 1999 Rev. 3 1HKKREN~ DBI?INITIONBj, ASBRBVIATIONSAND FOKIS Date 11/01/84 lOA POWER 5 LIGHT COMPANY Page 2 of 3 Dhtributors ,Nonconformance Reports An organization that h franchised by one Reports hsued for dfserepaneies or or more manufacturers to act as a deviations whfch require an engineering sales/service agency In an establtshed evaluatfon or controlled release of territory. A Dhtributor has warehouse and discrepant material for Hmited use.
,dhtributfon capabilities In addition to the sales/service Objective Evidences organization.'ocument I
Concurrenees Any statement of fact, informattorc or corn record, either quantitative or qualitative, A formal indication of agreement with the pertaining to the quality of an item or provisions and conclusfons presented in a .service based on observations, document. measurements or'ests which can be veriffed.
Document Reviews Primary Suppliers 1
'I A documented evaluation to determtne degree of plfance with regulatory, The SuppHer with whom the PO h place*
corporate or other predetermined requirements. Purchasing Agents Fabricator s The FPL representative designed to aet in FPL's behalf on a specffie procurement.
An organization that produces, assembles, modiffes or fabricates a product which, QuaMeattons upon Its completfon, conforms to the speciffeations and design criteria that were The char acterhties or abfHtfes gained furnished by the purchaser. through training or experience or both as measured against establhhed requirements HoM Points such as standarch oc tests that qualify an individual to perform a required function.
A step fn a procedure, shop traveler checklist, etc., requiring FPL inspection, QuaHty Assurance Programs test, or process verification. Work shall not be performed nor proceed beyond that The poHcies and procedures for quaHty until the. FPL representative or his 'oint related activities in documented form to designee fs present, or unless waived by a meet specified requirements, and the qualified QAPRR representative. fmplementatfon of those policies and procedures.
Manufacturers QuaHty Documents One who constructs any class of component, part, or appurtenance, to meet Any written or pictorial informatfon prescribed design requirements (N45.2.10- describing, defining, or specifying quaHty V3). r equie ments, procedures, activities oc Nonconformance s results'equest for Quotattoas A deficiency in characteristic, documentation, oc procedure which renders An invitatfon to a SuppHer to submit to the quality of an item unacceptable or FPL, prices, terms and condittons for a indeterminate. Examples of noncon- contemplated purchase.
formanees Includes physical defects, tes't failures, incorrect oc inadequate documentation, or deviations from prescribed processing, inspection oc test C
0 procedures.
Z CV E
O 4
hBSURkHCE IMCUMMFl'HAD1999 Rev. 3 MPERENC~ DEI?INITIONSs ABBaZVraTIONS mn POEMS Date 11/01/84 FLORIOA POWER d LIGHT COMPANY Page 3 of 3 Sales Offices 'LO ABBREVIATIONSs A sales organization, usually regionally ANSls American National Standards locat~ whose primary purpose ls to Institute promote the sale of products and service to accounts of customers It processes paper ASLs FPL Quality Assurance Depart-only, providing no warehousing or physical ment - Approved SuppHers List distribution of the products it sells.
ASMEs Am'erican Society o!
Service Orgassizatioa: Mechanical Engineers An organization. which performs a ASME service(s) at the request of the purchaser. Bd(PV Purchased services may be performed at CODEs American Society of the service organization's faciUty, the Mechanical Engineers Boiler 4 purchaser's faciHty, a third faciUty, or at a Pressure Vessel Code
, combination of faciUties in accordance h with requirements as specified in the PO or CMTRs Certified Material Test Repor t Contract. The end result Is the accomplishment of a task rather than the DRs Deficiency Report production of materials, components, parts, assembUes or systems. FPLs Florida Power dc Light Company Institute of Electrical and Any supplier who provides Items or Electronic Engineers services to the primary supplier Including other facIUties/locations within the NCRs Nonconformance Report primary suppUer's company.
NDEs Nondestructive Examination Substantial Safety Hazards NRCs Nuclear Regulatory Commis-A loss of safety function to the extent that sion there is a major reduction in the degree of protectiori provided to pubHc healt1i and Pos Purchase Order or Purchase safety for any facility or activity Ucensed Document or Contract under appUcable Parts of Title 10, Code Regulations. oi'ederal QAs QuaUty Assurance SuppUers QADs QuaUty Assurance Department Any Individual or organization under QAPs Quality Assurance Procurement contract for furnishing items or services "SuppUer" encompasses the terms Vendor, QCs QuaUty Control Seller, Contractor, Sub-Contractor, Fabricator, Cohsultang and lower tier QCNs Quality Control Notice levels RFQs Request for Quote Witness Point:
SQADs Special QuaUty Assurance A step In a procedure, shop traveler, Document checklist, etc. requiring FPL Inspection, test, or process verification. Work shall not be delayed if an FPL representative is not present at the appointed time.
SDN NO.
QJPPLIER DEVIATIONNOTICE Form 3525 (No~toe)gad) Rev, 1104 LORIDA POWER S LIGHT COMPANY Page of CONTRACT/PO NUMBER FLORIDA POWER 8t LIGHT COMPANY Purchasing Agent FRCXH:
Attention:
~
DRAWING SKETCH OR DATA ATTACHED SERIAL NO.
VEB DRAWING NO. 4a REVISION C3 NO PIKCK NO.
SPECIFICATION NO. 41 REVISION NAME OF PART ITEM DKVIATIONAND RECOMMKNOED DISPOSITION (Must Indude actual cnaracterlsltcs and spedflcatlon tolerances)
WHAT CORRECTIVK ACTION HAS BKEN TAKEN TO PRKVKNT RECURRENCK OF OKVIATIONt U5K 5KCONO PAGK FOR CONTINUATION.
PARED BY TITLE L OKPARTMKN FOR Rgl. USE ONLY PURCHASING ~ $ )GNATURK ANO OATK REVIEW OF FORM CONTENT ANO CORRKCTNESS APPROVKO DISPOSITION ANO BASIS ROUTING 51GNATURK DATE ACCEPT Te COMMKNTSg YES NO RPA ORIGINATOR YES NO QUALITYCONTROL YES NO ENGINEER (JPK)
SUPERVISOR (JPE)
S NO STORES SUPERVISOR YES NO QA REVIKWKR ~ CHANGE IS RKCOMMKNDEOASg P aa PERMANENT, T < TKMPORARY (THIS ORDER ONLY)
~ a = << ~ ~ ~ ~ ~ " - a aa e <<. ~ ~
. a. a e << " . e a<<<< -a~a<<o e g: ~ <<<<v'
INSTRUCTIONS FOR ROUTING OF SDNs The following instructions are to be used as a guideline in determining the routing of the SDN.
For specific instructions refer to QP 7.8:
1. 'uality Control; If the deviation is for an order originated by an operating plant.
2, JPE; If the deviation potentially involves a change from materials, design, specification or function.
3. Stores Supervisor;, If the change is permanent and affects future reorders of a series 2115 M&S hard card item.
4. Quality Assurance; In all cases.
NOTE: If the deviation is rejected by any of the departments in routing, the SDN shall be immediately returned to the originator. Where'the RPA originator or res'ponsible department'representative cannot obtain SDN disposition or receives a rejected response, he shall sign and return the SDN to the purchasing agent for notification of the supplier.
5. Upon completion of the required routing, the SDN shall be returned to the purchasing agent for Issuance of a P.O. Supplement.
6. The completed SDN, whether accepted or rejected, shall be filed in the purchase order package by purchasing.
V 'I Ill ,~ o % 1
ATTACHMENT 5 Safety Evaluation for Sample XDg 028-25277-2-PSL 030-61820-7-PSL 030-92120-1-PSL GRM.010 'T2
EVALUATIONFOR IDS 030&18207-PSL The 1/2 inch nut was determined to have a carbon content of 0.362% as opposed to 0.40% required for SA194 Grade 2H. We hardness of the nut was found to be within the code allowable limits.
A reduction in carbon of 0.04% does not result in any great effect on strength or ductility. In fact the hardness value, which may be correlated to tensile strength, shows the hardness and therefore strength to be high within the
. permissible range. A minor decrease in impact properties may result. However, nuts typically do not experience impact loads.
I Based on the above, Engineering recommends that the 1/2 inch nuts of this heat lot be i
used as is.
t k
EVALUATION FOR ID 028-252772-PSL 1
The 5/8" stud was determined to have a 484 reduction of area
,(R/A) value after tensile testing as 'opposed to 504 R/A required by the code. All other tensile properties: yield strength (Sy),
tensile strength (Su), and percent elongation (4E), exceeded the code required minimum values. 'hemical analysis showed 'the composition of the material to be within the code i allowable'imits.
Ductility is ll N determined in the tension test by either the 4E or the R/A and a significant reducti'on in ductilityl~
either value, in comparison to "normal" values asmaymeasured be ,of a by concern as an, indicator of the possibility, of 'atastr'ophic failure with small stress excursions beyond the yield Either method of determination of ductility is, sensitivestrength. to factors including, but not limited'o, specimen preparation many and test methods employed. Considering t'e statistical variation normally associated with ductility measurement, the 2%,difference between the test value and the required value for R/A is not significant. Since the ductility, as measured by R/A, for the stud does not show a significant,',deviation,'rom the !code acceptable value, catastrophic failure as a result of minor over-stressing in excess of yield is precluded',. Furthermore, the value for the 4E which exceeded the code required value (and was consistent with that reported on th'e materiallcertification from Cardinal Products Corp.) indicates that thej overall! ductility meets the code minimum value. I I I Based on the above, Engineering recommends that the 5/8" studs of this heat lot be used as is.
for ID 028-92120-1-PSL I'valuation The 1/2"-13 nut was identified as being out of specification as a result of the'review of the Test Laboratory Data. The Hardness did not match the specifications which are Rockwell A=66, 65, 66 Rockwell C=32*
ASTM A194B8 and ASME SA 194B8 show an acceptable hardness range to be 60 to 105RB. Using Table 6 of ASTM E140, Standard Hardness Conversion Tables for Metals, by interpolation a value of RB=105 is approximately R~ =64.5. The hardness values obtained for the nut (66, 65,* 66) lze within the normally expected range of error for an RB value of 105. Therefore the nut lies at approximately the top value acceptable for this specification.
Based on the above, Engineering recommends that the 1/2"-13 nuts of this heat lot be used as is.
GRM.010.FT2
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ML17221A597

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