ML112370648

From kanterella
Jump to navigation Jump to search
Forwards Addl Info Re Facility Compliance w/10CFR50,App I, Per 760903 Request.W/Eight Oversize Drawings
ML112370648
Person / Time
Site: Duane Arnold NextEra Energy icon.png
Issue date: 12/09/1976
From: Leslie Liu
IES Utilities, (Formerly Iowa Electric Light & Power Co)
To: Lear G
Office of Nuclear Reactor Regulation
Shared Package
ML112370647 List:
References
IEC-76-1933, NUDOCS 8805130035
Download: ML112370648 (34)
v • d • e


Text

OWA ELECTRIc LIGHT AND POWER COMPANY General Office CEDAR RAPIDS. IOWA LEE LIU VICE PRESIDENT - ENGINEERING December 9, 1976

.IE-76-1933 Mr. George Lear, Chief Operating Reactors Branch 3 Division of Operating Reactors Nuclear Regulatory Commission Washington, D.C. 20555

Dear Mr. Lear:

Your letter of September 3, 1976 requested additional information for evaluating Duane Arnold Energy Center compliance with Appendix I to 10CFR50. The purpose of this letter is to transmit our response to that request for information.

Three originals and 37 copies of this submittal are transmitted herewith. This submittal, consisting of this letter and the attachment hereto, is true and accurate to the best of my knowledge and belief.

Iowa Electriq Light and Power Company By:_______________

Led Liu Vice President, Engineering LL/RFS/ms Attachment cc:

R. Salmon D. Arnold R. Lowenstein L. Root J. Shea (NRC)

J. Keppler (NRC)

File A-107

'T Subscribed and sworn to before me on this 9Pf day of December, 1976.

Notary Public in and for Uhe State of Iowa.

z %--r 12851 8805130035 880429 PDR ADOCK 05000331 P

PDR

RESPONSES TO ADDITIONAL INFORMATION REQUESTED FOR DUANE ARNOLD ENERGY CENTER

TABLE OF CONTENTS Question 1 Question 2 Question 3 Appendices A.

Source Terms by Radionuclide B.

P&ID's for Liquid Radwaste C.

P&ID's for Gaseous Radwaste

1.
2.
3.

4.

Pg.

1-1 2-1 3-1

1. Provide the information requested in Chapter 4 of NUREG-0016 "Calculation of Release of Radioactive Materials in Gaseous and Liquid Effluents from Boiling Water Reactors (BWR-GALE Code)"

April 1976.

(formerly Appendix D of Regulatory Guide l.CC).

Refer to question No. 1 in Enclosure 2 of our letter of February 17, 1976.

Responses to Information Requested in Chapter 4 of NUREG-0016 Request

Response

4.1 General

1) Maximum core thermal power 1658 MWt
2) Tritium released from each reactor in a) Liquid effluents 20 Ci/yr*

b) Gaseous effluents 21 Ci/yr*

4.2 Nuclear Steam Supply System

1) Total steam flow rate 7,147,000 lb/hr
2) Mass of reactor coolant in reactor vessel at full power 289,000 lb 4.3 Reactor Coolant Cleanup System
1) Average flow rate 70,000 lb/hr
2) Demineralizer a) Type Powdex b) Size 26 ft3
3) Regeneration frequency NA
4) Regenerant a) Volume NA b) Activity NA
  • Note:

Based on GALE calculations 1-1

Request 4.4 Condensate Demineralizers

1) Average flow
2) Demineralizer type
3) Demineralizers a) Number b) Size
4) Regeneration frequency
5) Ultrasonic resin cleaning a) Is it used?

b) Volume associated with use

6) Regenerant a) Volume b) Activity 4.5 Liquid Waste Processing Systems la.

Flo System Sources (ga High Purity Equipment Drains:

Drywell Containment, Reactor Bldg.,

Fuel Pool Radwaste Bldg.

.Turbine Bldg.

Response

14,500 gpm 7.25 x 106 lb/hr Powdex 5

234 ft3 NA No NA NA NA w Rate*

l/day) 3400 PCA*

1.0 3720 1060 2960 0.01 0.01 0.01

  • Note:

Based on NUREG-0016 1-2

4.5 la.

System Continued Sources Flow Rate*

(gal/day)

Resin Rinse Cleanup Phase Separator Decant Condensate Demineralizer Backwash Low Purity Floor Drains:

Drywell Containment, Reactor Bldg.,Fuel Pool Radwaste Bldg.

Turbine Bldg.

Chemical Lab Drains Chem Lab.

5000 640 8100 700 2000 1000 2000 500 100 PCA*

0.002 0.002 Negligible 1.0 0.01 0.01 0.01 0.02 0.02 lb.

System High Purity Low Purity Chemical Collection Time (days) 0.16 0.7 2.7 Processing Time (days) 0.03 0.03 0.6 Discharge Time (days) 0 0

0 Equipment High Purity Collection Tanks Filter lonex Sample Tanks

  • Note:

Based on NUREG-0016 Number 1

1 1

2 Capacity or Process Rate 10,000 gal.

2 110 gpm (120 ft )

110 gpm (35 ft3 10,000 gal 1-3 Ic.

System

4.5 Ic. Continuec System Low Purity Chemical l.d System High Purity Low Purity Equipment Collection Tank Filter lonex Sample Tank Collection Tank Filter lonex Sample Tank Process Step Collection Tank Filter Ionex Sample Tanks Collection Tank Filter Ionex Sample Tank Number 1

1 1

I1 1

1 1

1 Capacity or Process Rate 10,000 gal 110 gpm (120 ft 2 110 gpm (35 ft3 10,000 gal 4,000 gal 2 gpm 2 gpm (35 ft3 4,000 gal Decontamination Factors*

Iodine Cesium Others 1

1 1

1 1

1 100 10 100 1

1 1

1 1

1 1

1 1

100 2

100 1

1 1

  • Note:

Based on NUREG-0016 1-4

Id. Continued Process Step 4.5 Systen Chemic System High Purity Low Purity Chemical NA See Appendix A See Appendix B Decontamination Factors*

Iodine Cesium Others 1

1 1

1 1

1 100 2

100 1

1 1

Fraction Discharge 0.01 0.1 1.0 Request Respon 4.6 Main Condenser and Turbine Gland Seal Air Removal Systems

1) The holdup time for offgases from the main condenser air ejector prior to processing by the offgas treatment system 0.5 hr
2) Offgas treatment system a)

Type (se b) Air inleakage per condenser shell 18.5 s c) Number of condenser shells 2

se e next page) cfm

1-5 Collection Tank Filter Ionex Sample Tank al le.

if.

1g.

2.

4.6

2. Continued

Noncondensible radioactive offgas is continuously removed from the main condenser by the air ejector during plant operation.

This is the major source and is larger than all other sources combined.' The air ejector offgas will normally contain activation gases, principally N-16, 0-19, and N-13.

The N-16 and 0-19 isotopes have short half-lives and quickly decay. The 10-minute half-life N-13 isotope is present in small amounts which are further reduced by decay. The air ejector offgas also contains the radioactive noble gas parents of biologically significant Sr-89, Sr-90, Ba-140, and Cs-137 isotopes. The concentration of these noble gases depends upon the usually extremely small amount of tramp uranium in the coolant and on the cladding surfaces, and the number and size of fuel cladding leaks.

Radioactive particulate daughters are retained on the HEPA filters and on the charcoal.

The offgas is discharged to the environs via the plant stack. The activity of the gas entering and leaving the offgas treatment system is continuously monitored. Thus, the system performance is-known to the operator at all times.

Mechanical Vacuum Pump Off gas During unit startup, air is removed from the main condenser by a mechanical vacuum pump. The mechanical vacuum pump exhaust is 1-6

4.6

2. Continued Continued discharged to the plant stack. The mechanical vacuum pump will normally be in service only during startup at a time when little or no radioactive gas is present. It will be isolated upon the receipt of a high radiation signal from the main steam line radiation monitoring system.

Request

Response

d) Iodine source term from condenser i) 1-131 ii) 1-133

3) Charcoal Delay System a) Mass of Charcoal b) Operating Temperature c) Dew point temperature d) Dynamic adsorption coefficient for Xe e) Dynamic adsorption coefficient for Kr
4) Cryogenic Distillation System a) Fraction of gases partitioned b) Holdup in system c) Storage following distillation d) Expected system leakage rate 5 Ci/yr*

5 Ci/yr*

37 tons 770F 45 0 F 330 cc/g 18.5 cc/g NA NA NA NA

  • Note: Based on GALE Assumptions 1-7

Request 4.6 Continued

5) Gland seal steam a) Flow rate b) Steam source
6) Gland seal condenser a) Vented gas holdup time b) Iodine partition factor c) Fraction of iodine released through system vent d) Gland seal off-gas system
7) See Appendix C

Response

7,147 lb/hr Primary steam 0.029 hrs 100 1.0

      • Gland Seal Condenser Offgas The gland seal condenser exhauster discharges into a separate holdup piping system. A holdup of approximately two minutes is provided to permit decay of the short lived radioactive gases present. These are principally N-13, N-16, N-17, and 0-19.

The release rate of radioactive gas is less than 0.1% of that from the air ejector offgas system. The gland seal exhaust gas flows past the elevated release point radiation monitors prior to release so its contribution to the release rate is included in the measured total.

1-8

4.7 Ventilation and Exhaust Systems 1, 2)

Decontamination Factors*

Building Equipment Iodine Particulates Containment HEPA and Charcoal 10 100 Turbine None 1

1 Radwaste None 1

1 Reactor None 1

1

3) See Appendix A for release rates. The radioactive particulate size distribution information does not exist for Duane Arnold. The gaseous radwaste treatment system meets the requirements of Regulatory Guide 1.112 and satisfies the criteria according to the BWR GALE Code.
4) Duane Arnold Source Parameters RX Building Location is 420 06' 02" N 910 46' 36" W Centered on N-S, E-W directions.

Area of roof = 140' x 140' Height = 896' 5-3/16"-757"6" Turbine Building Located East of and adjoining RX Building Area of roof = 257' x 137' Height = 833'10" -

757' 6"

  • Note:

Based on NUREG-0016 1-9

4.7

4) Continued Vent Stacks (3)

Located at NE corner of RX Building Diameter = 6' Height -

911' 10-5/8" -

757'6" Flow Rate -

63,000 cfm Exit Velocity = 63 x 103 = 37.14 ft/sec 60-M R2 Off Gas Stack Located 180' East and 560' South of RX Building Diameter = 2' Height = 1083'6" -

755'6" Flow rate = 4300 cfm Exit Velocity = 4300 22.81 ft/sec 60 Tr R2 Gaseous effluent temperature information is not measured at Duane Arnold, however, because of the distance between the offgas treatment system and the release point at the stack it is assumed to reach the ambient temperature at time of release.

Offgas flow is measured at Duane Arnold via RTD's.

5) Containment Building a) Purge frequency:

4/yr b) Purge duration:

8 hr c) Continuous purge rate:

NA 1-10

2.

The annual production date of agricultural products for the 50 mile radius as submitted was extrapolated from Linn and Benton Counties. Justify the use of this data in lieu of providing the data by sectors in the manner indicated in Sections 2.1.3.1 and 2.1.3.2-of Regulatory Guide 4.2, Rev 1 as requested.

The annual production data of agricultural products was extrapolated from data for Linn and Benton Counties, because

1. Linn and Benton Counties include most of the land within 20 miles of the plant.
2. Data from other counties was not available.
3. The production was assumed to be uniform within 50 miles of the plant.
4. If the production rate more than 20 miles from the plant was actually five times that of Linn and Benton Counties, the total population dose would increase about 60%.

This would not make any additional equipment cost-beneficial.

The following information is in support of point 4 above.

Milk production was based on data for the area within 50 miles of the plant, thus only -meat, fruits and vegetables were extrapolated.

Linn and Benton Counties have a total area of 1435 square miles or 18 percent of the area within 50 miles of the plant. For this analysis these counties will be represented by the area within 20 miles of the plant (1257 square miles or 16 percent of the area within 50 miles of the plant).

2-1

The cost-benefit analysis was based on the assumption that the agricultural production rate was uniform over the entire area within 50 miles of the plant. If, in fact, the production rate outside 20 miles is greater than that inside 20 miles, what is the effect on the total population dose?

Table 2 shows the effect of higher production rates outside 20 miles of the plant on crop and meat doses. For example:

If the production rate outside 20 miles were five times that inside 20 miles, the total production would be 4.36 times that used in the cost-benefit analysis.

The production weighted dispersion parameters would be smaller however since the parameters for the farther distances would be more heavily weighted. The product of relative tot'al production and the dispersion parameters would be:

a) 1.83E-08 for the stack X/Q b) 4.95E-11 for the stack relative deposition c). 1.02E-07 for the vent X/Q d) 5.86E-11 for the vent relative deposition.

Taking the ratio of these numbers to the similar numbers for the uniform production assumption gives the relative doses for crops and meat via each release point and isotope type.

Thus, 2-2

a) C-14 and H-3 doses from the stack would increase by a factor of 3.08.

b) Iodine and particulate doses from the stack would increase by a factor of 2.17.

c) C-14 and H-3 doses from the vent would increase by a factor of 2.97.

d) Iodine and particulate doses from the vent would increase by a factor of 2.02.

Table 2 was derived from Table 1 by weighting the dispersion parameters by the relative production rate in each region.

The table below shows the fraction of the total crop and meat dose which is attributable to each dispersion parameter:

Stack X/Q 0.05 Stack Relative Deposition 0.08 Vent X/Q

<0.01 Vent Relative Deposition 0.87 When these dose fractions are multiplied by the relative doses from Table 2, the following table results:

2-3

Relative Production Rate Outside 20 Miles 1.5 1.5

2.
3.
5.

10.

Relative Dose 1.00 1.14 1.28 1.54 2.09 3.45 When these relative doses are applied to the meat and crop doses of the Base Case, Table 3 results. This table shows that the population dose increases by 59 percent when the production rate outside 20 miles is five times greater than the production rate inside 20 miles.

Table 4 shows that no equipment is closer than a factor of 2.6 to becoming cost-beneficial. Therefore, since the crop production does not vary widely within 50 miles of the plant, extrapolating the Linn and Benton County data to 50 miles did not effect the cost-benefit analysis.

2-4

Duane Arnold Table 1

Determination of Meteorological Parameters for All Food Pathways (Grazing Season Values) page 1 of 3 Direction N

NNE NE ENE E

Distance 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total Sector Fraction 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.02 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 Stack X/Q Specific Deposition sec/m 3 1/m2 1.65E-07 6.25E-08 2.0 1E-08 1.08E-08

7. 19E-09 5.30E-09 1.20E-08 9.47E-08
4. 15E-08 1.35E-08
7. 23E-09 4.84E-09 3.58E-09 7.90E-09 6.75E-08
3. 26E-08

.1.

04E-08 5.48E-09 3.66E-09 2.70E-09 5.99E-09 7.15E-08 2.07E-08 7.32E-09 4.15E-09 2.84E-09

2. 13E-09 4.61E-09 9.06E-08 2.08E-08 7.33E-09 4.16E-09 2.85E-09 3.14E-09 4.81E-09 2.07E-09 2.39E-10 6.47E-11
3. 19E-11 2.06E-11 1.37E-11 5.27E-11 1.57E-09 1.68E-10 4.32E-11 2.08E-11 1.33E-11 8.88E-12 3.70E-11 1.03E-09 1.38E-10 4.02E-11 1.72E-11 9.89E-12.
6. 19E-12 2.77E-11 6.07E-10 5.55E-11 1.28E-111 6.06E-12 4.05E-12 2.90E-12 1.27E-11 8.41E-10 7.60E-11 1.74E-11 7.87E-12 5.04E-12 3.55E-12
1. 70E-11

.Vent X/Q Specific Depositio sec/m 3 1/m2 1.06E-06 2.24E-09 3.87E-07 4.54E-10 1.14E-07 9.82E-11 5.73E-08 3.63E-11 3.78E-08 1.84E-11 2.78E-08 1.14E-11 6.79E-08 6.43E-11 4.91E-07 2.79E-07 8.36E-08

4. 23E-08 2.81E-08 2.07E-08 4.71E-08 3.35E-07 2.09E-07 6.23E-08 3.13E-08 2.08E-08 1.53E -08 3.47E-08 4.91E-07
1. 19E-07 3.70E-08 1.91E-08 1.27E-08 9.44E-09 2.37E-08 4.82E-07 7.81E-08
2. 39E-08
1. 23E-08 8.17E-09 6.03E-09 1.69E-08 1.53E-09 2.75E-10 6.01E-11 2.22E-11
1. 13E-11 6.97E-12 4.09E-11 9.93E-10 1.73E-10 3.62E-11 1.33E-11 6.77E-12 4.19E-12 2.55E-11 7.91E-10
1. 15E-10 2.79E-11 1.05E-11 5.44E-12 3.32E-12 1.95E-11 9.34E-10
1. 14E-10 2.77E-11 1.05E-11 5.46E-12 3.34E-12 2.09E-11 2-5
May, 1976

Duane Arnold Table 1

Determination of Meteorological Parameters for All Food Pathways (Grazing Season Values) page 2 of 3 Direction ESE SE SSE S

SSW Distance 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total Sector Fraction 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03.

0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.02 0.20 0.28 0.36 Stack X/Q Specific Deposition sec/m 3 1/m2 7.02E-08 2.32E-08 8.46E-09 4.86E-09 3.34E-09 2.52E-09

5. 23E-09 5.80E-08 2.51E-08 8.93E-09
5. 1OE-09 3.49E-09 2.62E-09 5.43E-09 5.06E-08 2.76E-08
1. OOE-08 5.83E-09 4.02E-09 3.03E-09 5.92E-09 3.78E-08 1.94E-08
7. 14E-09
4. 19E-09 2.90E-09
2. 19E-09 4.26E-09 3.58E-08
2. 15E-08
7. 30E-09 4.03E-09 2.73E-09 2.03E-09 4.18E-09 7.08E-10 6.52E-11 1.53E-11 7.24E - 12 4.74E-12
3. 26E-12 1.48E-11 1.02E-.09 9.74E-11 2.21E-11.

'9.93E-12 6.35E-12 4.47E-12

2. 11E-11
1. 20E-09 1.20E-10 2.71E-11
1. 21E-11 7.64E-12
5. 38E-12 2.53E-11 7.34E-10
7. 67E-11 1.72E-11 7.40E-12 4.50E-12
3. 19E-12 1.56E-11 4.89E-10 5.24E-11
1. 17E-11 5.40E-12 3.65E-12 2.63E-12 1.09E-11 Vent X/Q Specific Depositio sec/m 3 1/m2 3.29E-07 6.20E-08 1.85E-08 9.36E-09 6.18E-09 4.53E-09 1.26E-08 2.22E-07 6.53E-08 1.96E-08 1.00E-08 6.59E-09 4.83E-09 1.21E-08 1.70E-07 6.29E-08 1.91E-08 9.79E-09 6.46E-09 4.73E-09
1. 13E-08 1.46E-07 5.84E-08 1.81E-08 9.42E-09 6.25E-09 4.59E-09 1.07E-08 2.01E-07 1.42E-07 4.27E-08 2.17E-08
1. 44E-08 1.06E-08 2.36E-08 9.35E-10
1. 12E-.10 2.44E-11 9.04E-12 4.62E-12 2.85E-12 1.98E-11
1. 16E-09 1.55E-10 3.64E-11
1. 38E-11 7.21E-12 4.44E-12 2.70E-11 1.24E-09 1.63E-10 3.84E-11 1.46E-11 7.65E-12 4.71E-12 2.87E-11 7.68E-10
1. IE-10 2.98E-11
1. 16E-11 6.26E-12 3.82E-'12 2.00E-11 6.57E-10 1.43E-10 3.46E-11 1.30E-11 6.68E-12 4.07E-12 2.09E-11 2-6
May, 1976'

Duane Arnold Table 1 Determination of Meteorological Parameters for All Food Pathways (Grazing Season Values) page 3 of 3 Direction Distance Sector Fraction Stack X/Q Specific Deposition sec/m 3 1/m2 Vent X/Q Specific Depositc sec/m 3 I/m2 SW WSW W

WNW NW NNW 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5.

5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total 1-5 5-10 10-20 20-30 30-40 40-50 Total verall Total 0.01 0.03 0.12 0.20 0.25 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36 0.01 0.03 0.12 0.20 0.28 0.36

4. 14E-08 2.07E-08
7. I1E-09 3.97E-09 2.69E-09
2. 00E-09
4. 16E-09 4.24E-08 2.09E-08 7.O1E-09 3.85E-09 2.60E-09 1.92E-09 4.08E-09 4.53E-08 1.48E-08 4.78E-09 2.58E-09 1.72E-09 1.26E-09 2.92E-09 8.78E-08 3.OOE-08 9.51E-09 5.02E-09 3.34E-09 2.45E-09 5.74E-09 1.28E-07 3.93E-08 1.23E-08 6.46E-09 4.28E-09
3. 14E-09 7.56E-09
1. 31E-07 5.72E-08 1.78E-08 9.25E-09 6.14E-09 4.52E-09 1.04E-08 5.94E-09 4.79E-10 5.12E-11 1.09E-1l 4.65E-12 3.02E-12 2.18E-12 1.02E-11 4.53E-10 4.81E-11 1.06E-11 4.81E-12 3.24E-12 2.31E-12 9.96E-12

.5.57E-10 5.68E-11

1. 22E-ll 5.17E-12 3.26E-12 2.31E-12
1. 15E-11 8.46E-10 1.23E-10 3.62E-11 1.49E-11 8.37E-12 5.12E -12 2.37E-11 1.11E-09 1.70E-10 5.17E-11 2.16E-11 1.23E-11 7.50E-12 3.29E-11
1. 17E-09 2.44E-10 7.64E-11 3.01E-11 1.62E-11 9.75E-12 4.23E-11 2.28E-11 2.82E-07 2.49E-07 7.80E-08 4.05E-08 2.71E-08 2.0 1E-08
4. 26E-08
2. 14E-07 3.29E-07 1.05E-07 5.46E-08 3.67E-08 2.74E-08 5.57E-08 3.28E-07 2.23E-07 7.23E-08 3.83E-08 2.57E-08 1.92E-08 4.04E-08 5.93E-07 2.29E-07 6.78E-08 3.40E-08 2.25E-08 1.65E-08 4.00E-08, 9.40E-07 2.54E-07 7.45E-08 3.73E-08 2.46E-08 1.80E-08 4.68E-08 1.07E-06 3.49E-07 1.02E-07
5. 10E-08 3.36E-08 2.47E-08 6.19E-08 3.43E-08 7.20E-10
1. 70E -10 4.52E-11 1.71E-11.

8.85E-12 5.32E-12 2.55E-11 6.62E-10 1.45E-10 3.70E-11 1.39E-11 7.19E-12 4.34E-12 2.18E-11 7.53E-10 1.53E-10

4. 18E-11 1.59E-11 8.33E-12 5.OOE-12 2.44E-11 1.06E-09 1.82E-10 3.84E-11 1.42E-11 7.18E-12 4.45E-12 2.71E-11
1. 15E-09 2.30E-10 4.84E-11 1.78E-11 9.05E-12 5.60E-12 3.23E-11 1.48E-09 3.37E-10 6.95E-11 2.55E-11 1.30E-11 8.04E-12 4.49E-11 2.90E-11 2-7 n~ay, Lvia

Table 2 Relative Production Rate Outside 20 miles 1.

1.5

2.
3.

5-10.

Relative Production Rate Total

1.

1.42 1.84 2.68 4.36 8.56 Relative Production Rate Times Dispersion Factor Stack X/Q 5.94E-9

7. 49E-9 9.03E-9
1. 21E-8.

1.83E-8 3.38E-8 Stack 6 2.28E-11 2.62E-11 2.95E-11 3.62E-11 4.95E-11 8.29E-11 Vent X/Q 3.43E-8

4. 27E-8
5. 11E-8 6.79E-8 1.02E-7 1.86E-7 Vent 6 2.90E-11 3.27E-11 3.64E-11 4.38E-11 5.86E-11 9.57E-11 Ratio Stack X/Q 1.00 1.26 1.52 2.04 3.08 5.69 Vent 6

X/Q 1.00 1.15 1.29 1.59 2.17 3.64 1.00 1.24 1.49 1.98 2.97 5.42 6

1.00 1.13 1.26 1.51 2.02 3.30

Table 3 Relative Production Rate Outside 20 miles 1

1.5 2

3 5

10 Crop and Meat Dose (man-rem) 47.9 54.6 61.3 73.7 100.0 165.1 Total 1980 Population Dose (man-rem) 88.6 95.3 102.0 114.4 140.7 205.8 Increase in Population Dose over Uniform Crop Distribution M%

3 8

15 29 59 132 2-9

ne Arnold

May, 1976 Table 4 Ratios for Alternate Cases

.Annual A -Doses from Base

-from Prey Case man-rem man-rem Annual A Costs from Base from Prey Case dollars dollars Cost-Benefit Ratios from Base from Prey Case

$/man-rem

$/man-rem Gland Seal D-1 Double holdup time D-2 Add HEPA & charcoal SJAE E-1 Operate at OF dewpont E-2 Add 2 more beds E-3 Remove 2 beds 1.65E-02 2.35E 00 2.96E 00 1.20E 00

-i.46E 0 0 a Drywell F-2 Remove charcoal

-2.39E+01 F-3 Remove HEPA & charcoal-2.45E+0l Turbine Bldg G-1 Add HEPA G-2 Add HEPA & charcoal G-3 Add clean steam Auxiliary Bldg H-1 Add HEPA H-3 Add HEPA & charcoal Radwaste Bldg I-1 Add charcoal I-2 Remove HEPA 1.04E-01 2.69E+01 2.65E+01 6.25E-01 2.45E+01 7.02E 00

-3.44E 00 6.OOE-01 2.68E+01 2.39E+01

>5,000

.14,600 155,300 45,800

-451 800b,

.- 9,300

-18,100 59,400 120,700 7150,00.0 76,200 153,100 18,100

-17,300

-8,800 61,300 76,900

>3.0E+05 6.2E+03 5.2E+04 3.8E+04 3.1E+04 3.9E+02 7.4E+02 5.7E+05 4.5E+03 75.7E+03 1.2E+05

6. 2E+03 2.6E+03 5.OE+03 a Negative dose changes are increases in dose b Negative costs are decreases in costs Case Cs-Bnefi~t Purpose I.

1.5E+04 2.2E+03 3.2E+03 rogt-Benefit i

3. Provide information on grazing season (give dates), feeding regimes for cattle (such as grazing practices, green chop feeding, corn and grass sileage feeding and hay feeding),

pasture grass density (Kg/m2 ) and yield statistics (Kg/

2) for harvested forage crops for beef and dairy cattle feeding.

The following information is provided on the grazing season and feeding regimes for cattle. Because there is considerable variability in the production of forages and the feeding and grazing programs for cattle, the data must be considered as estimates for average conditions:

Calendar Dates for Grazing Season and Feeding Pattern Forage Grass pastures Alfalfa Alfalfa Red Clover Corn stalks Green Chop Silage Hay Range Apr. 20-Dec. 1 Apr. 15-May 10 Oct. 20-Dec. 1 Apr. 15-May 10 Oct. 1-Apr. 1 May 1-Oct. 1 All year feeding practice by some All year feeding practice by some Intensive Period May 15-Nov. 1 Apr. 30 -

May 10 November May 1-Oct. 1 Oct. 1-Jan.

1 May 20-Sept. 20 Dec. 15-May 15 Dec. 15-May 15 Portion of Yr 42-50%

42-50%

12.5%

25-42%

25-33%

33%

42%

42%

3-1

3. Continued Pasture Grass Density. This is difficult to assess since the density varies throughout the year, and the pasture grass is not normally harvested and stored. However, using the values which are common to hay harvesting, which should add some conservatisms, it is estimated that the pasture grass density is 0.4 kg/m2 of dry matter.

Annual Yield of Forage Crops.

This yield is based upon the average harvest which is estimated as 1.2 kg/m2 of dry matter.

3-2

APPENDIX A SOURCE TERMS BY RADIONUCLIDE

05/17/7b 17.30.02 PAGE 3

DUANE ARNOLD

)77.

BASE CASE GASEOUS RELEASE RATE SCURIES PER YEARa LOOLANT CONC.

CONIAINMENT TURBINE AUXILIARY RADWASTE GLAND AIR MECH VAC NUCLIDE XMILROCURIES/Ga BLDG.

BLDG.

BLDG.

BLDG.

SEAL EJECTOR PUMP TOTAL KR-83M 1.100E-03 0.0 0.0 0.0 0.0 2.SE 01 2.4E 01 0.0 4.9E 01 KR-8-5M 1.900E-03 3.0E 00 6.8E 01 3.0E 00 0.0 4.3E 01 2.3E 03 0.0 2.4E 03 Di KR--85 6.000E-06 0.0 0.0 0.0 0.0 0.0 1.4E 02 0.0 1.4E 02 KR--87 6.b00E-03 3.E 00 1.3E 02 3.0E 00 0.0 1.5E 02 6.UE 00 0.0 2.9E 02 KR--88 6.600E-03 3.E 00 2.3E 02 3.OE 00 0.0 1.SE 02 1.5E 03 0.0 1.9E 03 7

KR-89 4.100E-02 0.0 0.0 0.0.

0.0 6.4E. 02 0.0 0.0 6.4E 02 71 XE131M 4.700E-0b 0.0 0.0 0.0 0.0 0.0 4.8E 01 0.0 4.8E 01 XE133M 9.000E-05 0.0 0.0 0.0 0.0 2.0E 00

.3.3E 01 0.0 3.5E 01 XE-133 2.bDOE-03 b.6 01 2.5E 02 6.6E 01 1.OE 01 S.9E 01 1.OE 04 2.3E 03 1.3E 04 XE13SM 8.400E-04 4.6E 01 6.SE 02 4.6E 01 0.0 B1.E 01 0.0 0.0 7.6E 02 XE-135 7.200E-03 3.4E 01 6.3E 02 3.4E 01 4.5E 01 1.6E 02 0.0 3.SE 02 1.3E 03 E-137 4.700E-02 0.0.

D.0

-0.0 0.0 7.8E 02 0.0

.0.0 7.8E 02 XE-138 2.800E-02 7.0E 00 1.4E 03 7.0E 00 0.0 S.9E 02 0.0 0.0 2.0E 03 TOTAL NOBLE GASES 2.3E 04 TI 1--131 4.912E-03 1.7E-02 1.9E-01 1.7E-01 S.OE-02 2.2E-02 0.0 3.E-02 4.8E-01 I--133 1.13bE-02

b. BE-02 7.tE-01 b.8E-01 1.6E-0 8.8-02 0.0 0.0 1.8E 00 C---14 0.0 0.0 0.0

.0.0 0.0 9.SE 00 0.0 9.5E 00 AR--41

2. 5E 01

.0.0

.0.0 0.0

.. 0.0 0.0 0.0 2.5E 0l 0.0 1.1E 01 0.0 0.0 0.0 1.1E 01 0.0 2.1E 01 0.0 APPEARING IN THE TABLE INDICATES RELEASE IS LESS THAN 1.0 CI/YR FOR NOBLE GAS, 0.0001 CI/YR FOR I

L 5/7/

~17.30.02 PAGE '4 DUANE ARNOLD BASE CASE AIRBORNE PARTICULATE RELEASE RATE

%CURIES PER YEAR",

CONTAINMENT TURBINE AUXILIARY' R ADWASTE_-

MEffH ^VAC.

NUCLIDE BLDG.

BLDG.

BLDG.

BLDG.

PUMP TOTAL Ck--Sil 3.OE-06 1.3E-02 3.DE-04 9.[OE-05 0.0 1.3E-02 Ji. MN--54,.3O-5 6O-04

.3U-3.

3. DE-4

-. 0.0.........3.

9E03..........

FE--S1

'I.OE-06' 5.OE-04 1h0E-04

1. 5E-04 0.0 1.1E-03 L-.

C0---58 BE 6O-706....

_6. E-0 4 I..OE-04

.5E -D10 5.

. 00......13-3.~

i CO--60 1.OE-0J4 2.UE-03 1.02-02 9.DE-'4 0.0 1.3E-02 L_.

ZN--65 2-GE-0 5 2 *0E -0 4.

. 2OE -0 3..

SE-05

a.........

2.2E-03,..

SR--89 9.fUE-07 6.DE-03 9.OE-05

4. SE-06 0.0 6.1E-03 SR--9U S. 3E -U8 2.OE -0S5-S.GEr06.

3O-6

.. ~002a-5.

ZR--95 4.OE-06 1.0E-0LI 4.OE-04 S.OE-0?

0.0 S.DE-D'd SB-124 2.DE-06 3,E-0LI

.2,OE-04 5.DEI-fJ?

0..,-.0.

S.0L.. -0LI C-134 4.BE -GS 3.OE-04 4.DE-03 4.5E-05 3E-06 LI.

0~3 LS-136 3.OE-06 590E-05..

3.E-04 4.SE-D6_

ME-06.

3.6E-04.

CS-i13?

S.SE-OS 6.OE-04 S. SE-03 9I.0E-OS 1.OE-OS6.5E0 bA-146

~

.4. DE-06 1.1E0

4. DE-04

.02-06

.20

.ED LE -141 1.02-L16 6.02-04 1.0E-04 2.6E-OS 0.0 7.3E04 r7--------------------------------------

1---------

05/17/76 DUANE ARNOLD BASE CASE CONCENTRATION ANNUAL IN PRIMARY ---------

NUCLIDE HALF-LIFE COOLANT HIGH PURITY tDAYSO 4MICRU CI/MLU tCURIESu CORROSIuN AND ACTIVATION PRODUCTS NA 24 6.2SE-01 7.65E-03 0.00335 P 32 1.43E 01 1.83E-04 0.00009 Ck 51 2.78E 0l 4.S8E-03 0.00220 IN '4 3.0E 02 S.SDE-05 0.00003 1'N 56 1.07E-01 3.86E-02 u.009ss FE 55 9.SuE fie 9.16E-04 0.00044 FE S9 4.50E 01 2.7SE-OS 0.00001 CO £8 7.1VE 01 1.83E-114 0.00009

,0 60 1.12E 03 3.6?E-04 0.00018 NI 6 1.07E-01 2.31E-04 0.0000b CU 64 S.3E-01 2.6E-02 0.01087 ZN 65 2.49E 02 1.83E-04 0.00009 ZN 69M 5.7SE-01 1.74E-03 10.00173 ZN 69

.9E-0a 0.0 00061 W187 9.LE-01 2.66E-04 0.00012 1P239 2.35E 00 6.32E-03 Os0025 FISSION LR 8 1 OR 8 RB 81 SR 81

'R 9U SR 91 Y 9114 y Ill SR 92 Y 92 Y -13 ZR 95 NB '15 INB 98 NO 9 9 TC 94M TC101 RU0103 R"H103m

.TC104 RU105 1H11s TE129M TE129m 1 E 19 TE131m j1L131 1131 TE 132 1133 1 E139 (25114 PRODUCTS

1. 0I0E-O-1 2.21E-02 1.07E-02 5.20E 01 1.0E 04 4.603E-01
3. 4?E-0K 5.88E 01 1.13E-01
1. 47E-01 4.2HE-01 6.56L 01 3.50E 01
3. S4E-02 2.79E 00 2.SOE-01 9.72E-03 13.96E 01 1.25E-0U 1.85E-01 S.2LE-094 1.SOE 00 3.40E 01
1. 711E-0 1.25E 00 1.74E-02 8.0SE 00 3.25E 00 9.58L-n2 8.75E-01 3.07E-02 7.9E 02 2.64E-03 3.78E-03 3.27JE-03 9.LE-OS S.50E-0b
3. 41E-u3 U.0 3.66E-OS 7.7SE-DB 4.76E-03
3. 42E-03 6.41E-06 6.41E-0b6 2.82E-0i 1.81E-03 1.65E-02 5.96 E-02 1.83E-0s 0.0 S.114E-02 1.62E-03 0.0 0.0 3.66E-05

.. U 8.9LE-0S 0.0 4.91E-03 9.07E-6 2.6 3E-02 1.4E-02 S.59E-02 2.75E-US 0.00063 0.o001 l 0.00022 0.0000 4 0.00000

0. 00136 0.00071 0.00002
0. 0 0198
0. 002i8 0.00138 0.00000 0.00000 0.00023
0. 0 01 85
0. 00611 0.00030 0.00001 0.00001 0.00055
0. 000 52 0.00052

[.00003 0.00002 0.0001L 0.00004 0.0000 1 0.00234 0.0(1000

0. 0 060 S
0. 0.0 8 S 5 0.00480 0.00013 17.36.42 LIQUID EFFLUENTS RELEASES TO DISCHARGE CANAL LOW PURITY 4CURIESo 0.00541 0.00018 0.00464 0.00006 0.00713 0.0009 4 0.00003 0.00019 0.00038
0. 00004 0.01680 0.00019
0. 00116 0.00119 0.00021 0.00580 0.000 S 0.00007 0.000 53 0.00009 0.00001
0. 00 193 0.00118
0. 00 005
0. 00151 0.00287 0.00 199 0.00001 0.00001 0.00112 0.00 169 0.00777 0.00014 0.00002 0,00002 0.00027 0.000S2 0.00052 0.00012
0. 00004 0.00002
0. 00007 0,00001 0.00187 0.00001 0.00426 0,01186 0.00245 0.00141 PAGE 3

ADJUSTED.

OTERGENT.....

TOTAL CHEMICAL TOTAL LWS TOTAL WASTES

%LURIESn %CURIESU

%CI/YRu CIYRu

%CI/YRa 0.00000 0.00876 0.01527 0.0 a.a1s0 0.00000 0.00027 0.00047 0.0 0.0004?

0.00001 0.00685 0.01194 0.0 0.01200 0.00(100 0.00008 0.00014 0.0 0.00014 0.00000 0.01668 0.02907 0.0 0.029o0 0.00000 0.00138 0.00241 0.0 0.00240 0.00000 0.00004 0.00007 0.0 0.00607 0.00000 0.00028 0.00048 0.0 h FJ0048 0.00000 0.00055 0.00096 0.0 0.00048 0.00000 0.0010 0.00017 0.0

.00010 0.00000 0.0277 0.00823 0.0 0.04810 0.00000 0.00033 0.00048 0.0 0.00048 0.00000 0.0018 0.00330 0.0 0..1500 0.0000 0.00180 0.0031 0.0 0.0010 0.000(11 0.000332 0.00036 01.0 0.00038 0.00000 0.00875.

0.00130 0.0.....0.00150 0.00000 0.00033 0.00028 0.0 0.000 0.00000 0.00001 0.0[001 0.0 0.00001 0.00000n 0.00029 0.00170 0.0 0.001370 0.00000.0.0014 0.0032 D 0.

0 0.0030 0.00000 0.0000?

0.00001 0.0 0.0001 0.00000 0.00349 0.00609 0.0 0.00570 0.000010 0.0059 0.0039 0 0 0.00920 0.00000 0.0033?

0.00f88 0.0 0.00019 0.00000 0.00001 0.002 9

0.0 0.0000 0.00000 0.00001 0.00006 0.0 0.0002 0 onorio'.0 00007,__._

0.000(0 0.0000 0.00001 0.0 0.00008 0.0(0000 0.002501 0.00002 0.0 0.O002..

0.00000 0.6039 0.02021 0.0 0.0800 0.00000 002S4.0044 0

0.0

0. 00078 0.00000 0.00003 0.002 00 0 0.O24 0.0000.

0.00043 0.00004 0...0 0.00058 0.00001 0.00087 0.00142 0.0 1.0010 0.00000 0.00108 0.00182 0.0 0.0010 0.00000 0.00082 0.0013 0.0 0.00140 0.00000 0.00075 0.00102 0.0 0.00130 0.00000 0.00005 0.00012 0.0 0.0001 0.00000 0.00003 0.00006 0.0 0.00000 0.00000 0.0001 0.0007 0.0 0.000 0.00001 0.00002 0.0000 0.0 0.0030 0.0000?

0.00017 0.000120 0.0 0.0002 0.00000

  • 0.00399 O00040 0.0

..... 0.00b0 0.000000 0.0072b 0.00270 0.0 0.0610 0.00000 0.00001 0.00002 0.0 0.00002 0.00000 0.01031 0.0179 0.0 0.01800 0.00008 0.0235

.0006 0.0

.0004100 0.00000 0.00725 0.01264 0.10 0.01300 0.00000 0.0014 0.00268 0.0 0.00270 V ~.

0

,'I 4.

E 4

05/17/76 17.36.42 PAGE DUANE ARNOLD LIQUID EFFLUENTS %CONTINUEDa BASE CASE CONCEN[RAIION ANNUAL RELEASES TO DISCHARGE CANAL IN PRIMARY----------------------------------------ADJUSTED NUCLIDE HALF-LIFE COOLANT HIGH PURITY LOW PURITY CHEMICAL TOTAL IWS TOTAL

%0AYSn u

MICRO CI/MLa ECUR1ESa 4CURIESn CURIESO CURIESQ

%CI/YRo 1i1s 2.?"E-0 1 1.88E-02 0.00692 0.00846 o.0001 0.01539 0.02682 CS13b 1.30E 01 1.82E-05 0.00009 0.00092 0.00000 0.00100 0.00175 CS157 1.lf1E 04 b.4HE-05 0.00031 0.00329 0.00000 0.003S9 0.00626 bA137M 1.?7E-U 0.0 U.00021 0.00307 0.00000 0.00336 0.00S86 CS1-:8 2.24E-O 6.67E-03 0.0025 0.00621 0.00000 6.66875 0.015p5 BAl3'1 S.76 E-02 7.30-03 0.00109 0.00062 0.0000 0.00171 0.00297 6A140 1.28E 01 i.66E-04 0.00018 0.0003 0.00010 0.00054 0.00095 LA140 1.LE 00 0.0 0.00001 0.0000c 0.00000 0.00006 0.00011 8A141 1.25E-02 6.67E-031 0.00007 0.00003

.000 0.00010 0.00018 LA141 1.LOE-01 0.0.

0.00018 0.00016 0.000.

0,00034-0000 CE141 3.24E 01 2.75E-05 0.00001 0003 0.00000 0.00004 0.000 8 BAL42 7.64E-03 3.95E-03 0.00001 0.00000 0.0 0.00001 0.00002 LAl12 6.39E-02 3.68E-03 0.00070 0.00041 0.00000 0.00111 0.00193 CL13 1.3LE DO 2.68E-05 0,00001 0.[0002 BA000 0.00004 0.00006 PK14 1.3?E 01 3.L6E-05 0.00002 0.00004 0.0000 0.00005 0.00010 ALL OTHERS 1.91E-03 0.00001 0.00003 0.00000 0.00004 0.0000?

TOT AL

%EXCEPT TRITIUMn 4.aL-U1

. 0.08374 0.11794 0.000200 0.20188 0.00bb TRITIUM RELEASE 20 LURIES PER YEAR

~--

~

DETERGENT 10TAL WASTES

%CI/YRP

%CI/YRu 0.0 0.02700 0.0 0.00170 0.0 0.00630 0.0 0.00590 0.0 0.01500 0.0 0.00300 0.0 0.00095 0.0 0.00011 0.0 0.00018 0.0 0.00059 0.0 0.00008 0.0 0.00002 0.0 0.00110 0.0 0.0000 0.0 0.0000 0.0 0.00007 00 3SD0.35000

05/27/76L DUANE ARNOLD COMP[IANCE BASE CASE B 12.51.00 LIQUID EFFLUENTS CONCENTRATION ANNUAL RELEASES TO DISCHARGE CANAL IN PRIMARY ADJUSTED NUCLIDE HALF-LIFE COOLANT HIGH PURITY LOW PURITY CHEMICAL TOTAL LWS TOTAL

,DAYSD TMICRO CI/MLv ECURIESn TCURIESn ECURIESn ECURIESn tCl/YRa CORROSION AND ACTIVATION PRODUCTS NA 24 L.25E-011 7.85E-03 0.00335 0.00541 0.00021 0.00197 0.0154 P 32 1.13E 01 1.83E-04 0.00001 0.00018 0.00003 0.00030 0.0005 CR 51 2.78E 01 4.S8E-03 0.00220 0.00b44 0.00072 0.0075L 0.0130 MN 511 3.03E 0-S.SDE-05 0.00003 0.00006 0.00001 0.00009 0.0001 MN 56 1.07E-01 3.86E-02 0.00955 0.00713 0.00001 0.01669 0.0287 FL 55 9.S0E OP 9.36E-04 0.00044 0.00094 0.00015 0.00153 0.0026 FE 59 4.50E 01 2.75E-05 0.00001 0.00003 0.00000 0.00005 0.0000 Cc 58 7.13E 01 1.83L-04 0.00009 0.00019 0.00003 0.00030 0.000S CO '0 1.9?E 03 3.67E-04 0.00018 0.00038 0.00006 0.00061 0.0010 NI 65 1.07E-P1 2.31E-04 0.00006 0.00004 0.00000 0.00010 0.0001 CU 61 5.33E-01 2.60E-02 0.01087 0.01680 0.00055 0.02821 0.0485 ZN 65 2.45E 02 1.83E-04 0.00009 0.000119 0.00003 0.00031 0.0005 ZN bIM 5.75E-ol 1.74E-03 0.00073 01D.001-16 0.00004 0.00193 0.0033 IN 69 3.6LE-G2 0.0 0.00061 0.00119 0.00004 0.00185 0.0031 W187 9.96E-01 2.L6E-04 0.00012 0.00021 0.00001 0.00034 0.0005 NP?39 2.3SF 00 6.3tE-03 0.00295 D.00580 0.00061 0.00935 0.0111 PRODUCTS 1.00E-01 2.21E-02 1.D7E-02 5.2OF 01 1.03E 04 4.03E-01 3.47E-02 5.88E 01 1.13F-o 1.47L-01.

4.25E-01l

.6.501 (I

3.50E 01 2.S4F-02 9.72t-03 3.961u v1 3.96 E-V2 11.251-01 1.8SE-UL 5.21E-04 1.sF 00 3.400E 01 I. 7'lE-02 1.25E on 1.7iE-P2 8.051 00 3.2'E 001

9. 581-02 8.71E-01 3.6?-02 7.49E D?

2.64E-03 3.78E-03 3.27E-03 9.16E-05 5.5 PE-0b 3.41E-03 0.0 3.61-05

7. 7 SE-03 4.76E-03 3.42E-03 L. 41E-0b1 6.41E-OL 2.82E-03
1. 81:E-03 1.6E-02 5.91E-02 1.83E-05 0.0 5.34E-02 1.6 2E-03 0.0 0.0 3.6bE-05 0.0 8.4EL-05 0.0 4.911.1-03 9.07E-0b 2.6?f-0 1.94-02 5.5lE-02 2.7 5.E-05 0.000b3 0.00014 0.00022 0.00004 0.00000 0.00136 0.00071 0.00002 0.00198 0.00238 0.00138 0.00000 0.00000 0.00023 0.00085 0.00611 0.00030
0. 000 1 0.00001 0.000525 0.00052 0.00052 0.00003 0.00002 0.00001 0.00004 0.00001
0. 00 234 0.00000 0.00605 0.00855 0.00480 0.00013 0.00015 0.00007 0.00053 0.00009 0.00001 0.00193 0.00118 0.00005 0.001.51 0.00287 0.00199 0.00001 0.00001 0.00012 0.00169 0.00777 0.000 14 0.00002 0.00002 0.00027 0.00052 0.0 0(1s2 0.00012 0.00004 0.00002 0.00007 0.00001 0.00487 0.00001 0.0042b 0.01486 0.00'45
0. 001111 0.00000 0.00000 0.00000 0.00001 0.00000 0.00004
0. 00003 0.000011 0.00000 0.00002 0.0000S 0.00000 0.00000 0.00000
0. 0001 9 0.00025
0. 00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.0000 2 0.010001 0.00001 0.00000 0.0006 9
0. 00000 0.00000 0.00082 0.00000 0.000233 0.00108 0.00021.

0.00075 0.0001.5 0.00001 0.00334 0.00192 0.00008 0.003 49 0.00527 0. 003112 0.00001 0.00001 0.00035 0.00273 0.01413 0.00044 0.*00003 0 00003 0.00082 0.00105 0.00105 0.00017 0.00006 0.00004 0.00012 0.00002 0.007 91 0.00001 0.01032 0.021124 0.0072 S 0.00177 0.00186 0.0003b 0.00128 0.00027 0.00002 0.00574 0.00330 0.00013 0.00601 0.00908 0.00 589 0.00002 0.0000?

0.00060 0.00b469 0.02433 0.00M076 0:0000 0.00140 0.00181 0.00181

0. 00 029 0.00010 0.0000b.

0.00021 0.00004 0.01361 0.00 002 0.01776 0.04172

0. 01299 0.00304 DETERGENT TOTAL WASTES EC1/YRa

%CI/YRi

'I 0.0 2

0.0 2

0.0 3

0.0 3

0.0 8

0.0 8

0.0 2

0.0 5

0.0 7

0.0 3

0.0 3

0.0 3

0.0 8

0.0 a

0.0 0

0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.01500 0.00051 0.01300 0.0001b 0.02900 0.00260 0.00008 0.00052 0.00110 0.0001.7 0.04900 0.00053 0.00330 0.00320 0.00059 0.01600 0.00190 0.00036

0. 00130 0.00027 0.00002 0.00570 0.00330 0.00013 0.00600 0.00910 0.00590 0.00002 0.00002 0.00060 0.00470 0.02400 0.00076 0.00005 0.0010 0.00140 0.00180 0.1 0180 0.00029 0.0 0010 0.00006 0.00021 0.00004 0.01,400 0.00002 0.01800
0. 04200 0.01200 0.00300 F IS S I ON BR 83 RB 84 SR 89 SR 90 SR
91.

Y 91.M Y 91.

SR 92 Y 92 Y 93 ZR 95 NP 9S NE 98 MO 99 TC 99M T C 1 01

'RHI03M TCL104 RUlUS5 RHIOSM RH10S TELO9M T E 131.

9 TE 1.

31 T EL31-M TEL31 11.31 TEl 2 11.32 11.33

11. 3 C S3 14 2f

.2 2'

2(

21 x1 3

3; 3:

1' 3t 31 41 4(

1 PAGE 3

05/27/76 12.51.00 PAGE 4

fDUANE ARNOLD LIQUID EFFLUENTS ICONTINUEDu COMPLIANCE BASE CASE B CONCENTRATION

-ANNUAL RELEASES TO DISCHARGE CANAL IN PRIMARY -------------------------------------------

ADJUSTED DETERGENT TOTAL NUCLIDE HALF-LIFE COOLANT HIGH PURITY LOW PURITY CHEMICAL TOTAL LWS TOTAL WASTES EDAYSo

%MICRO CI/MLn SCURIESn

%CURIESn XCURIESn XCURIESm XCI/YRu

%CI/YRa

%CI/YRa II

2. E-01 1.88E-02 0.00692 0.008b46 0.00010 0.01548 0.02665 0.0
0. 2700 CS ll.

E 01 1.82E-05

.00.000.9 00012 0.00014 0.00114 0.00196 0.0

0. 0200 CS137 1.10E 04 6.42E-05 0.00031 0.00329 0.00053 0.00413 0.00710 0.0 0.00710 BA137 1.77E-03 0.0 0.00029 0.00307 0.00050 0.00386 0.00664 0.0 0.006b0 CS138 2.24E-02 6.67E-03 0.00254
0. 00b21 0.00000 0.00875 0.01506 0.0 0.01500 BA139 5.76E-02 7.30E-03 0.00109 0.000b2 0.00000 0.00171 0.00294 0.0 0.00290 BA14O 1.28E 01 3.L6E-04 0.00018 0.00037 0.00005 0.000b0 0.00103 0.0 0.00100 LA140 1.b7E 00 0.0 0.00001 0.00005 0.00003 0.00009 0.00016 0.0 0.0001b BA141 1.25E-02 6.67E-03 0.00007 0.00003 0.00000 0.00010 0.00018

.0.0 0.00018 LA141 1.b2E-01 0.0 0.00018 0.00016 0.00000 0.00034 0.00058 0.0 0.00058 CE141 3.24E 01 2.75E-05 0.00001 0.00003 0.00000 0.00005 0.00008 0.0 0.00008 BA142 7.bIIE-03 3.95E-03 0.00001 0.00000 0.0 0.00001 0.00002 0.0 0.00002 LA142 6.39E-02 3.68E-03 0.00070 0.000111 0.00000 0.00111 0.00191 0.0 0.00190 CE143 1.38E 00 2.68E-05 0.00001 0.0n002 0.00000 0.00004 0.00006 0.0 0.00006 PRI43 1.37E 01 3.66E-0S 0.00002 0.00004 0.00001 0.00006 0.00010 0.0 0.00010 ALL OTHERS 1.98E-03 0.00001 0.00003 0.00000 0.00004 0.00007 0.0 0.00007 TOTAL

%EXCEPT!rTRITIUM 4.08E-01 0.08374 0.11794 0.00627 0.20796 0.35796 0.0 0.36000 TRITIUM RELEASE 20 CURIES PER YEAR

APPENDIX B PIPING AND INSTRUMENTATION DRAWINGS for LIQUID RADWASTE

OVERSIZE DOCUMENT PAGE PULLED SEE APERTURE CARDS NUMBER OF OVERSIZE PAGES FILMED ON APERTURE CARDS APERTURE CARD/HARD COPY AVAILABLE FROM RECORD SERVICES BRANCH FTS 492-8989

Retrieved from "https://kanterella.com/w/index.php?title=ML112370648&oldid=5273970"