NG-82-2653, Stress Corrosion Cracking Evaluation Program,Duane Arnold Energy Ctr
| ML20067C979 | |
| Person / Time | |
|---|---|
| Site: | Duane Arnold  |
| Issue date: | 04/23/1980 |
| From: | Martin J, Riccardella P, Sullivan M NUTECH ENGINEERS, INC. |
| To: | |
| Shared Package | |
| ML19268D482 | List: |
| References | |
| IOW-20-004, IOW-20-4, NG-82-2653, NUDOCS 8212100303 | |
| Download: ML20067C979 (75) | |
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f- NG-82-2653 J December 1, 1982
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_O v Attachment 3 J
STRESS CORROSION CRACKING EVALUATION PROGRAM
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i DUANE ARNOLD ENERGY CENTER r
L Prepared for:
Iowa Electric Light & Power Company
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' Prepared by:
NNTECH San Jose, California
. Prepared by: Reviewed and rov by:
Lq 1 1, 0&f L 4. 772 ; i, uw A
[. N M[rtin, P.E. P5 C. Riccahdella, P.E.
I l' M
- M. D. Sullivan l Issued by: -
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- b. Date: April 2? 1980
. W. Axline, P.E.
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a ABSTRACT
_ An intergranular stress corrosion cracking (IGSCC) survey of the i
austenitic stainless steel piping in the recirculation system and
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RHR system of the Duane Arnold Energy Center has been completed. The primary objective of the survey was to assist Iowa Electric Light & Power in its inservice inspection program 7 by identifying the weld joints which are most susceptible to IGSCC. In the survey, material properties and fabrication data q from the plant records were compiled for each joint. The Stress O Rule Index (SRI), a method of evaluating the sustained stress level at the inside surface weld HAZ, was calculated for each i
joint. The materials data and SRI were then used to rank each weld joint according to its ' relative susceptibility to IGSCC. An IGSCC Susceptibility Matrix was developed as a means of ranking the weld joints. Through this matrix each weld joint is
~1 categorized into one of three regions. Region I represents u combinations of SRI and material chemistry which have thus far n proven to be immune to IGSCC. Regions II and III represent j combinations more susceptible to IGSCC.
,. In addition to the ranking, all weld joints were categorized as conforming, -nonconforming, or service-sensitive according to the guidelines given in NUREG-0313, Revision 0, the Nuclear Regulatory Commission document related to IGSCC of BWR piping.
i-- The following summary highlights the results of the survey.
- 1. Of a total of 117 welds >10 inches in diameter, 19
! welds were found to meet the requirements for con-
,] forming material as defined in NUREG-0313. Of the remaining 98 nonconforming welds , 4 were identified l as having a high resistance to IGSCC because the base materials contained a carbon content between 0.0357.
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and 0.050% or because they are believed to have been
-. fabricated using an inside surface water spray
_ cooling technique.
- 2. None of the large diameter pipec (>10 inches diameter) were in service-sensitive lines.
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- 3. All of the 26, 4 inch diameter welds were found to n contain base material defined as nonconforming by
' NUREG-0313, and 18 of these were located in service-
.. sensitive lines. Two of these 18 welds have high
'_i resistance to IGSCC because the carbon content of
,, base material was between 0.035% and 0.050%.
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categorized in Region I of the IGSCC Susceptibility Matrix, representing the least susceptible welds.
'l The remainder of the weld joints were evenly divided
"' between Regions II and III.
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W TABLE OF CONTENTS g( g
.Pm ABSTRACT.....................................................i L TABLE OF CONTENTS......................................... 111
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1.0 INTRODUCTION
AND PROGRAM OBJECTIVE.................... 1 L' 2.0 REVIEW OF PLANT REC 0RDS............................... 2 1 3.0 REVIEW OF METALLURGICAL VARIABLES..................... 3
'J Figure 3-1 Carbon Content Versus Time to............. 8
,r Failure in Type-304 Stainless Steel i
a Pipe Tests Table 3-2 Summary of Metallurgical . . . . . . . . . . . . . . . . . 9
' O. Evaluation Results
,\;J 4.0 STRESS RULE EVALUATION............................... 10 ln
',] 5.0 IDENTIFICATION OF LOW FAILURE PROBABILITY JOINTS..... 11 q Figure 5-1 IGSCC Susceptibility Matrix.............. 13 LI APPENDIX A SCC Evaluation Tables f i U APPENDIX B Stress Rule Index Evaluation Summary
- ' APPENDIX C ISI Isometric Drawings a
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1.0 INTRODUCTION
AND PROGRAM OBJECTIVE As a result of the stress corrosion cracking incidents in welded
., austenitic stainless steel primary coolant piping in Boiling
, Water Reactors (BWRs) in recent years, Iowa Electric Light and Power instituted a program with NUTECH to evaluate the stress corrosion cracking propensity of stainless steel welds in the I recirculation and residual heat removal (RHR) systems at the Duane Arnold Energy Center (DAEC). The objective of the program p is to perform a review of plant fabrication records, a metallur-
,L gical review of these records to evaluate factors important to p intergranular stress corrosion cracking (IGSCC) in the BWR
'b environment, and a Stress Rule evaluation to assist in identi-fying those joints which are potentially susceptible to IGSCC.
b9 The ultimate program aim is to provide input to the DAEC Inservice Inspection Program so that the proper attention can be 3 focused on those joints which are most susceptible to IGSCC. The identification of potentially susceptible pipe locations will qf- also enable Iowa Electric to prepare for potential incidents by LA providing a repair or replacement plan to address the problem where it may exist. Additionally, this program will assist in y addressing, in a more meaningful way, the concerns of the Nuclear Regulatory Commission published in NUREG-0313 and NUREG-0531
[' regarding materials selection and processing guidelines for BWRs.
The program is divided into the following four major task's:
r '"ask 1. Review of Plant Records
- Task 2. Review of Metallurgical Variables
., Task 3. Stress Rule Evaluation b Task 4. Identification of Low Failure Probability Joints The following sections provide a brief description of the work performed under each of the above mentioned tasks.
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2.0 REVIEW OF PLANT RECORDS J The cbjective of this task activity was to obtain and review all
,g plant records required to complete the detailed evaluations L described in Tasks 2 and 3. These records included piping fabrication and isometric drawings, stress reports, material n -
certifications, fabrication procedures, and records regarding repairs and replacements.
7 An extremely complete and well-compiled set of fabrication
,- records for the entire recirculation system were supplied to
.. NUTECH by Mr. K. V. Harrington of Iowa Electric, greatly
,, facilitating this task activity.
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7 3.0 REVIEW OF METALLURGICAL VARIABLES
_ The objective of this task was tc identify, for each stainless
, steel joint in the recirculation and RHR systems, the material j chemistry, significant fabrication practices that may have an effect on the joint's susceptibility to IGSCC, and determine the NUREG-0313 status. A detailed compilation of this information is L
presented in the Strees Corrosion Cracking Evaluation Tables 7 included as Appendix A to this report.
V p 3.1 Material Chemistry Certified material test reports were located for each component of the subject piping systems. The material specification and a the associated carbon content are identified in SCC Evaluation Tables, Appendix A.
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V Unstabilized wrought austenitic stainless steel with a carbon "p content less than 0.035% has been demonstrated to be highly il d resistant to stress corrosion cracking and is acceptable to the q NRC for installation in BWR piping systems, as stated in
- j NUREG-0313. Welds between materials with a carbon content in the 0.035% to 0.050% range are identified in the SCC Evaluation Tables as having high resistance to IGSCC. While no NRC credit can be taken for these welds relative to NUREG-0313 guidelines, we feel it is appropriate, based on field failure data and the
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v EPRI sponsored pipe test and laboratory test data, to identify
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v these joints as highly resistant to IGSCC.
test data presented in Figure 3-1 The General Electric illustrates that at these carbon levels Type 304 stainless steel is highly resistant to
!. IGSCC.
Ferritic steels and cast stainless steels have also been demon-strated to be highly resistant to IGSCC and are acceptable 9
materials for installation in BWR piping systems. Inconel (Alloy 600), not addressed specifically in NUREG-0313, is considered as
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'J a conforming material in this evaluation. In the uncreviced condition this material has provided satisfactory performance in L the BWR environment.
. 3.2 Significant Fabrication Practices A review of the fabrication procedures revealed that the large diameter shop welds may have been fabricated using an inside surface water spray cooling technique. The pipe fabricator, C Southwest Fabricating and Welding Co., commonly uses the sprey U cool technique to maintain interpass temperature when welding p stainless steel pipe having a wall thickness greater than 0.75 t, in.(1) The main purpose for employing this technique was to control interpass temperature, however, the technique is similar
'ly to that currently being studied as a fabrication remedy for stress corrosion cracking mitigation.
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,d This technique, also called heat sink welding (HSW), is used to i produce axial compressive residual stress on the inside pipe
^ surface in the weld heat affected zone. The first two layers are deposited by the gas tungsten are process in the normal manner.
Iv The remainder of the weld is made while the inside surface is being cooled by either a water spray or by filling the pipe with
!qj flowing wat.er.
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It has been documented in General Electric Company's pipe tests on small diameter piping that as much as an order of magnitude
[ performance improvement may be possible for heat sink welded
- j oints . (2) A separate program, supported by the Electric Power r
i, v (1) Robert Pearson, Soutnwest Fabricating and Welding Co.,
,.3 Private Communication (2) R. Hughes, Qualification of Solution Heat Treatment, Corrosion Resistant Cladding and Heat Sink Welding.
7 Seminar on Countermeasures for BWR Pipe Cracking, im January 22-24, 1980.
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'j Research Institute, is currently underway to evaluate the residual stress benefit for large diameter piping fabricated using this process.
] Although no NRC credit can currently be taken for heat sink welded joints in relation to the augmented ISI requirements of r'
NUREG-0313, these welds are specifically highlighted in the SCC U Evaluation Tables because of their potentially high resistance to e IGSCC. It should also be noted that, although the shop welding O proceoure used in fabricating the Duane Arnold spools requires interpass temperature control, and allows water spray cooling, specific documentation describing the detailed process and verifying its use oc each of the shop welds has aot been located. Follow-up discussions with the pipe fabricator will be necessary to provide adequate assurance that the water spray cooling technique was, in fact, employed for each shop weld.
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3.3 NUREG-0313 Evaluation Q '
An etaluation of the metallurgical data compiled for each joint was conducted with respect to the NRC technical positions f established in NUREG-0313, " Technical Report on Material Selection and Processing Guidelines for BWR Coolant Pressure
'[ Boundary Piping," published in July 1977.
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The SCC Evaluation Tables identify the NUREG-0313 status of each
'V joint based on the following criteria.
Conforming -
joints for which each of the adjoining parent materials are one of the following highly resistant materials; n
ferritic steels, " Nuclear Grade" or L-Grade Type 304 or 316 l austenitic stainicss steel (<0.0357. Carbon) , or cast etainless
steels. Regular grades of 304 or 316 stainless steel are not U
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considered conforming unless the as-installed piping, including the weld, is in the solution annealed condition, c Nonconforming - all joints not meeting the above criteria. These joints are subject to augment.ed inservice inspection requirements as identified in NUREG-0313.
U Service Sensitive -
nonconforming joints in lines designated by
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the NRC as having experienced cracking of a generic nature, or that are considered to be particularly susceptible to cracking r because of a combination of high local stress material condition,
<- and high oxygen content in lines which have relatively stagnant, intermittent, or low flow coolant. Included in this category of
([ piping runs are: core spray lines, recirculation bypass lines, CRD hydraulic return lines, isolation condenser lines, and idh shutdown heat exchanger lines.
inspection is required for these lines.
A higher degree of augmented l pA b A revision of NUREG-0313, currently issued for review and comment, proposes to add recirculation riser piping and internal J)
L) attachment welds to the service sensitive category.
]j 3.4 Summary l The overall metallurgical review consisted of an examination of
'] 136 joints in the recirculation system and 7 joints in the residual heat removal system. Of the 143 total-joints, 19 were t evaluated as conforming, 106 were nonconforming, and 18 were both 4 nonconforming and in service sensitive lines.
F L Of a total of 117 welds greater than or equal to 10 inches in r diameter, 19 welds were found to meet the requirements for
[ conforming material as defined in NUREG-0313. Of the remaining 98 nonconfcrming welds, 34 were identified as having a high r'
- resistance to IGSCC because the base materials contained a carbon content between 0.0357. and 0.0507. or because they are believed to J IOW-20-004 6 1ia nutech
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have been fabricated using an inside surface water cooling technique.
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' r. All of the 26, 4-inch diameter welds were found to contain base
[ material defined as nonconforming by NUREG-0313, and 18 of these were located in service sensitive lines. Two of these 18 welds
, were designated as having a high resistance to IGSCC because the carbon content of the base material 'was between 0.035% and
,P 0.0507..
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^ Table 3-2 provides a tabular summary of the metallurgical
,- evaluation results.
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LING TOTAL CONFORMING WATER SPRAY WELDS WITil CONFORFIING G SERVICE SYST,EM DIA WELDS WELDS COOLED * .035 <%C <.050 WELDS SENSITIVE RECIRCULATION 22 23 2 10 15 21 0 SUCTION RECIRCULATION 22 16 0 6 1 16 0 DISCilARGE RECIRCULATION 16 8 0 8 0 8 0 RING IIEADER RECIRCULATION 10 64 16 0 0 48 0
,o RISERS RECIRCULATION 4 18 0 0 2 0 18 BYPASS RECIRCULATION 4 7 0 0 0 7 0 BRANCil CONNECTIONS RESIDUAL IIEAT 20 0 0 4 0 4 0 REMOVAL 18 2 1 0 0 1 0 4 1 0 0 0 1 0 TOTAL 143 19 24** 18** 106 18 3 *The use of water spray cooling not yet fully verified.
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- Each column includes six joints that satis fy both criteria (i.e., . 0 3 5 < *, C < . 0 5 0 a n d shop water spray cooled.)
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- V 4.0 STRESS RULE EVALUATION
!e formed for each joint being studied. The Stress Rule Index is O determined in the following manner. The axial stress components 1
! resulting from sustained loading conditions (i.e. pressure, l deadweight, and stecdy state thermal expansion) are derived from i the elemental force and moment tables of the original Duane
'[ Arnold piping stress analysis. These are combined with residual !
stress estimates and input to the General Electric Company developed Stress Rule Index equation shown below.
f P, + Pb Q + F (Resid)
+ "
S S + .002E
{ y y m .
Where P, = Primary Membrane Stress
= Primary Bending Stress i{ .
Pb S
y
= Code Yield Strength Q = Sustained Secondary Stress l F = Sustained Peak Stress E = Elastic Modulus
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,J Resid = Weld Residual Stress ,
l }7 For non-creviced welds , General Electric Company has . determined that if the index is less than unity, susceptibility to stress
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corrosion cracking is taitigated; for crevices, a value somewhat lower than unity may be more suitable. To this date, IGSCC
,{ events have not been observed in joints exhibiting a SRI less than 1.2.
f, b The SRI evaluation was facilitated by the use of a NUTECH
_ computer program (SCORE) which calculates the SRI given the
, appropriate forces and moments from the piping stress report.
The SRI for each joint is given in the SCC Evaluation Tables.
h Detailed results of the SRI evaluation are included in Appendix B.
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,v 5.0 IDENTIFICATION OF LOW FAILURE PROBABILITY JOINTS Three main considerations must be taken into account in deter-
- , mining the susceptibility of a joint to intergranular stress corrosion; material properties, stress, and environment. In this l report, we have quantitatively addressed two of these three
- { factors. For both material properties and stress, there exists sufficient analysis, laboratory data, and field experience to provide a basis for determining relative susceptibility. The environmental factor has only been addressed in that stagnant, p low flow lines (service sensitive) are considered more C susceptible to IGSCC. The degree to which one of these three
, ingredients must be present for IGSCC to occur is variable, 3 making it extremely difficult to combine what is known about each of these factors to define en absolute scale of susceptibility.
l There are also other known variables that effect the suscepti-
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bility of sensitized austentic stainless steel to IGSCC. These other variables, which must be factored into a final determina-d tion of susceptibility, include such effects as cold work, counterbore grinding crevices, temperature, pH, etc. EPRI is i] currently sponsoring research that may lead to more refined techniques for quantifying the susceptibility of various piping joints.
li To provide a rudimentary means of ranking each weld, the IGSCC Susceptibility Matrix was developed. It displays the relative G susceptibility of each weld based on the information that haa L '
been compiled in this study regarding material properties and stress conditions. Figure 5-1 shows the placement of the
[. recirculation and RHR system welds in the matrix based on the stress rule index calculated for that joint and the highest j carbon content of the base material on either side of the weld.
O The IGSCC Susceptibility Matrix is divided into three regions labeled I, II, and III. Region I contains welds that are either i
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conforming from a material standpoint (less than 0.0357, carbon as 3 defined in NUREG-0313) or have a stress rule index less than
,I susceptible to IGSCC.
v Region II defines an intermediate zone encompassing welds which i"
{ exhibit considerable margin to failure, relative to Region III q welds, but are somewhat more susceptible than Region I welds.
lO Finally, Region III represents the most susceptible welds, those having the smallest margin to failure.
lbL Other variables, as discussed earlier, can enter in to increase
- or decrease the susceptibility to IGSCC. Two of the more impor-tant factors to be considered for Duane Arnold are the effects of I shop water spray cooling and whether specific welds are in lC service sensitive piping. Welds that are believed to have been m shop water spray cooled are underlined in the matrix. These ld welds are potentially highly resistant to IGSCC because of favorable residual stress distribution. If this is verified and actual measurements determine the extent to which these stresses are reduced, the stress rule index may be significantly lowered,
, }" thus shifting the position of the underlined welds to the left.
j The other important factor to consider is whether welds are in l
service sensitive piping. Welds which are both nonconfoming and in service sensitive piping are identified in the matrix with an q asterisk. These welds are potentially more susceptible to IGSCC b than other welds of the same matrix position.
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cJ 0 STRESS RULE INDEX r, 0 - 1.20 ,
1.21 - 1.50 ,
1.51 - 2.00 ,2.01 +
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UtA J4 R)tA-J 5 RRA J7 RCA J18 ptB J5 i
RRD J7 RitA J10 DtA-J2 l
RRG J7 R>tB J11 DtB J9 c- , RRC-J7 R)!B J2 RRF.J7 RCB J21 RRB J7 h 9 RRJi J7 RRC-J7 k
~1 9 d
RCA J27 RCA I)4 RBB J18 RRA/H J5 (8 welds) o 3BA M* RBE-J78 RBA-J6*
c R34-J7*
RRE J4 RBB-J12* REA J8* RBB-J6*
C RCB'J30 REB J8*
Ci I i
- 3 RHC-F2 RHD-F2 RRF-J4 RRC-J4 RHC J1 RHD-J1 RRG-J4 RRH J4
, RAD-J4 RRA.J4 RCB J37 RRB J4 REGION III 9
f [j O 9 (HIGH SUSCEPTIBILITY)
RCA-J7 RCB-J27 RCA J12 ptA - J 5 RCB J24 RBA-J98
<l RCB-J31 ;ICIJTI 'mX 77 RHB.Ji RBB.J98
- .:.: 10CX-~JIS RCB-J41 RCA J21 KiXUT* U"d"*J6
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Z
@ RCA J24 RCA-J28 R>tB J1 IICI ~J317 RBA J3* DTT",TT C o. RCA J38 U"J 7T2 RCA-J32 RCB.J6 RSB J2*
U EG~7I'~ IICI UTT RCB J7 RBB J 3*
' 1 KU~~JT3 1ECTUI3 Z RRA/H-J4A (8 welds) af tA-J6 RCB-J35 c
U,U ) h W J3 (E welds)
{- .
RCA-J4 RCB-J24 RCA J22 RCA-J3 RBA-J108 RCA J6 RCA-J5 KCTUTI V e.y RBA.J128 RCB-J25 RCB J3 RBB-J10*
O RCB J9 RCB.J4 -
KCTUT8 RCB.J5 f e RCB-115 RCB J15
(~h REGION II 9 (MODERATE SUSCEPTIBILITY) ig I
" RHB-F3 RCA-F2 l . an RCB F2
,8,' m RRA/H F2A (8 welds)
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- REGION I v
(LOW SUSCEPTIBILITY) i r i i
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4 e IN SERYiCE SENSITIVE LINES I -
xxx SHOP WATEM $ PRAY COOLED 1
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l FIGURE 5-1 l J IGSCC SUSCEPTIBILITY MATRIX m
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APPENDIX A
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I SCC EVALUATION TABLES r,-
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i0 A I"C7ac STRESS CORROSION CRACKING EVALUATION COM DUANE ARNOLD ENERGY CENTER LINE NO. SYSTEM MVl51011 - DATE PAGE RCA RECIRCULATION SUCTION - LOOP A 0 ti/lu80 Al i mums SHOP MAT CA.JON SfATUS STM53 ea mi r FI D T
EC ICA 19 T,REA g(h g EMI gg 00 0 WELD aa Ng g RECIRC. StKTION IM CLD SA-508 CL.2 ... g ...
N0ZZE (NIA) IIM ALII)Y STEL RCA-F2 22 N0Z-SL SW X 1.01 SAFE-D4D 1mC0) SA-336 Gt F8 7 ftS7S 0.023 (NIA)
LOWER SC RCA-J3 22 SE-P FW e. 1.03 111 011 RESISTANCE TO ICSCC PIPE (5-1) Rt.W A358 CL.1 FIGI 1 2P2470-4A 0.045 A240 T304 LOWER SC 6 SIDP WARR SPRAY OX) LED RCA-J4 22 P-E SW a. 1.30 11101 RESISTANG TO IGSCC 4
ELBOW (90*LR) 2 300223 0.049 0
LOWER SC 6 910P WATER SPRAY COOLED RCA-J5 22 E-P SW tp+ 1.32 mm creverurr m verer-PIPE (5-2) 2P2470-4A 3.045
[0T304 1 RCA-J6 22 P-P FW & 0.90 gg, y gg PIPE (6-1) 1 2P2470-1A 3.045 0 T3M RCA-J7 22 P-P SW h 0.87 SIIDP WATER dPRAY COOLED PIPE (6-2) 1 300069-1B 3.050 0 4 RCA-J12 22 P-E SW h 1.30 ll0P WATER SPRAY 000 TID A W3MW ELBOW (90*LR) 2 300223 1.049 LOhT.R IC TD CA511NG RCA-J B 22 E-V IW h 1.33 llI01 RESISTANCE TD ICSCC VALVei CAST A351-65 GR CF-8 7 40298 0.05 91 FERRITE
(>D-F023A)
C] C C~3 C C~ 2 CO C] w O C7C~)-(*"S ~~ C bd C.3 C3 C3 0.LJ %(3) e 2 iO5'."icTu STRESS CORROSION CRACKING EVALUATION
'$d,AY,I" DUANE ARNOLD ENERGY CENTER EINE NO. SYSTEM REVISION - DATE PAGE RCA ECIR01ATim SUCTim - LOOP A (Cm'T) 0 11 / 1 1 / 8.0 A2
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munes SHOP CARSON KTATUS STRESS HE AT
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""'""' "#5EAlls' ',agl- =0L 75"' ,
S gc ,l=,a
"""5 RCA-JIS 22 V-P FW X 0.%
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- 300069-1B 0.050 PIPE (4-1) 0 M 1 RCA-J21 22 P-E SW & 1,43 Sil0P WATER SPRAY OD0 LID
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wA 3 WP304W-l%7 y K51142-3 0.048 ELBOW (90*SR) y h IDfd!! 1C TO CASTING RCA-J22 22 E-Pp FW h 1.63 :ttet nrsisTANrT Tn irsn'
" II I 19 0 C bT A351 GR. CF8M 7
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PIPE (5-2) A 0 N 1 2P2470-4A 0.045 SIEOL 5-2 ALSO SIMi ON 10. Al FfA-JSA 4 BPC SW (
WLUOLL'r TORGED A182-F304 6 812680 0.060 22" X 4" (4%E)
PIPE (4-1) A2f0 04 1 300069-1B 0.050 SF00L AlSO SIIDWN (N 10. A2 RCA 118 4 ggt sw ( l.32 A182-b9 4 41167 0.070 lil11NTMl!W. TION FIANE AIS2 *v9 15LIND l'IN#I , , 4 41167 0. 0 /0 V h
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io). 57.e STRESS CORROSION CRACKING EVALUATION ~
p DUANE ARNOLD ENERGY CENTtiR
__ I SYSTEM REVIStC4 DATL FAEi LINE NO l '
RCA ECIRDtATim DISOARrf - iHP A 0 11/11/80 A3
$NOP 18 EAT CAR 00ll sfATUS STRESS 1 EA g M "
SR N) 1 FI D SPEC ICA I N g g 0 0 X WELD nN NN 3 V5 F r 51510 er 0.06 g CAST A351 CF8M 7 14% FERRITE 50448 0.05 ,
RCA-J24 22 Ip-P IU X 0.98
^ *I 300071 1B 0.058 PIPE (7-1) A 0 M 1 !
RCA-J28 22 P-V IV X 0.97 CAST A351-65 m. CF8 7 44266 0.04 18% FERRI 1E 031A1 RCA-J30 22 V-E FW X 1.27 A #3 " 2 600324-1A 0.055 ELBOW (90*1R)
.'tCA-J32 22 E-P SW 0+ 1.26 SiOP WATIR SPRAY 000 TID
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- 300075-1B 0.058 j PIPE (9-1) A 0 04 1 RCA-J38 22 P-P SW ,
K 0.89 PIPE (9-1) 1 300075-1B 0.058 FIDW RESTRICITR WELDW 10 PIPE I.D.
A 0T 4 ,
RCA-J41 22 P-T SW G. 1.25 90P WATFR SPRAY OCDLED RTI1UCING TEE RGW A403-WP304W 20" ORLET EX11tLIDED PRIOR 1D 2 6003241 0.055 IDT TREADENT 22"X22X20 FRN A240 RCA-J43 22 T-Cr FW X I 33 '
REDUCING CAOSS RGWd4hhr304W 2 582533-1 0.040 i T DENT 22X22X16X16 MN A240-69 RIA-J6 22 Cr-Cp SW & 1.22 910P WATER SPRAY COOLED A W-304-67 3 600225-1A 3.058 hEID CAP g
co aaaa a a oa aaaaaai G9ao e
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-l ia*;"5C CORROSION CRACKING EVALUATION !
STRESS MPAN DUANE ARNOLD ENERGY CENTER b I
LINE NO. SYSTEM REVISION - DATE PAGE !
0 4/11/80 A5 RMA ECIROJLATION Rife IIADER - LOOP A l NUREG l
- HEAT CARBON STATUS STRESS NT E
gC CA10N TEEAT- CONTENT SS NC C RULE COMMENTS f NU 8 R FI D ER IN) P WELD MENT (%) Eg g0 v5 F l
F NN)EX [
A '
WEID CAP p 3g 3 K51404-4D :).050 0
ICM-J1 16 C gikir SW S. 0. % 910P WATER SPRAY 000!ID 1 600120-1B 3.059 i T litr ITNT 4 11 06 T 4 .
MIA-JS 16 ILir-Cr SW B+ 1.42 910P WA1T.R SPRAY (I)0 LID RE11 ICING CROSS R6W A403 WP-304W AISO S110HN ON PC. A3
' 2 582533-1 J..040 22X22X16X16 FRN A240-69 Mn-J7 16 Cr-IL!r SW @+ 1.37 910P WATER SPRAY 000 LID RIS m M E m m m i m m RING IIEADER R6W A358 CL.1 Fint 1 60Cl20-1B 1.059 IIEAT 1TIEA17Uir (74-n A?40-67 TTO&
2 n-Jll 16 ILir-Cp SW a. 0. % 90P WA1T.R SPRAY COOLID wA 3 K51404-4D .).050 WELD CAP fg3g [3N-67 ;
i I
I
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i0l'It c alc STRESS CORROSION CRACKING EVALUATION
"'"'co,*, " '" DUANE ARNOLD ENERGY CENTER SYSTEM REVist0N - DATE PAGE LINE NO.
EClic1AT10N RISERS - UIP A (N2E) A6
. RRE 0 4/11/80 l NUAEG ser nu cAno0N s#Ss s m ss 288Sn
"^
Ni E [j F
c0MPONENT "sr c A 0N T,RE,AT g g NENT s ME X
4s F F 1 600120-1B 0.059 ALSO SHOMN 04 PC. AS 12' 2) FRt i A 0 304 R M-J10 10 IUr-A SW X 1.40 AIRPIER IVRCLD A182-F304 6 52624 0.070 RRE-J7 10 A-P FW X 1.11 PIPE (12-2) SES A376-TP304 5 2P3687 0.051 RRE-J5 10 P-E SW X 1.56 A
3 37845-1A 0.061 ELBOW (90*LR) p [304W-67 RRE-J4 10 E-P SW X 1.39 PIPE (12-1) SILS A376-17304 5 2P3399 0.055 RRE-J4A 10 P-P FW X 0.98 FORTION OF SPOOL l'2-1 WAS QTr OLTr PIPE (12-1) SfLS A376-TP304 5 2P3399 0.055 APO RENEIDED IN 1978 RRE-J3 10 p.P IW X 1.23 SAFE-WD 10RGID SA-336 GR. F8 7 M53S 0.030 EXTTNSION RRE-F2A 10 P-SE FW X 1.02 SRS SB-166 INQNEL 7 NX8927 0.07 SAFE-Ee REPIXD IN 1978
)
RRE-F2 10 SE-N0Z FW X 1.03 RfCIRC INIET FORGED SA-508 CL.2 "~ M ""
NO77I t' IDW AIInY STITI.
[. .] C C C C C C C_~3 C C C C C C C FQ [
N .-
iOE*It C ac STRESS CORROSION CRACKING EVALUATION Cour DUANE ARNOLD ENERGY CENTER EINE h0. SYSTEM REVISION - DATE PAGE WCIROJLATI(N RISERS - lHP A (N2F) A7 RRF 0 ft/11/80 NuAEG SHOP MEAT CARSON STATUS STRESS 1, ,'la.
'^
Pi i Wr! ,g j ca"ra*"' "s7E5'CJO* 1,alg d'Ja =l,"' sg jg I g ca"*"'5 h5 F 1 600120-1B 0.059 m N m N. AS IU R 24-2) N A2 0 304 R L\-J8 10 ILir-A SW X 2.05 AIMiiER 10RGED A182-F304 6 52624 L).070 RRF-J7 10 A-P FW X 1.20 PIPE (13-2) SILS A376-W304 5 2P3271 0.061 HRF-J5 10 P-E SW X 1.70 A 3 304W-67 3 37845-1A l).061 ELBOW (90*LR) 4 RRF-J4 10 E-P SW X 1.41 PIPE (13-1) SILS A376 TP304 5 2P3687 ).051 RRF-J4A 10 P-P FW x 0.98 l
IX)RTION OF SIYX)L 13-1 WAS OIT OLIT
[: PIPE (13-1) 9tLS A376 W304 5 2P3687 :).051 AND RIME 1K.D IN 1978 l
RRF-J3 10. P-P iw X 1.23
- 3 IORGII) SA-336 CR. F8 7 M53S 0.030 RRF- F2A 10 P-SE IV X 1.02
" U 99.S SB-166 INCONI:L 7 tiX8927 0.07 SAFE-END RLPIK ED IN 1978
'fN2 :
RRF-F2 10 Sli-N0Z FW X 1.03 RECIRC INLIT 10 RED SA-508 CL.2 "' "~
NO2ZLl! Im ALIDY STIIL
.; C ] C C C C C C C C C C C C C C C b~$
0 0 -
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'6"I '
COMPANY DUANE ARNOLD ENERGY CENTER LINE NO. SYSTEM REVISION - DATE PAGE RRG ECIRWLATIm RISES - LOCP A (N2G) 0 11/11/80 A8 NUREG SHOP HE AT CARBON 5 AIUS STRESS
" I "
N 8R IN) PE FI D WELD SPEC CAION T,R ,AT- ER ff RN l0 0 X Ng g i 1 600120-1B 0. 0W E S N m A5 1 11 24-1) 4 T 04 MIA-J4 10 Ikir-A SW X 1.51 AIMPIIR IDRGLD A182-F304 6 52624 0.070 RIC-J7 10 A-P IW X 1.22 PIPE (14-2) SMLS A376-TP304 5 2P3271 0.061 RRG-J5 10 P-E SW X 1.68 A 3 304W-67 37845-1A ELBOW (90*LR) 3 0.061 RRG-J4 10 E-P SW X 1.53 PIPE (14-1) 96.S A376-5 5 2P3637 L).051 RRG-J4A 10 P-P IW X 0.98 l
PIPE (14-1) 90.S A376 5 2P3687 ].051 IVRTION OF Sit 0L 14-1 WAS Off ElR
( AND REWEl.DED IN 1978 RRG-J3 10 P-P IW X 1.23
NA --
N0ZZLE IDW ALIDY S11El.
C [ l O
O C C C C C I ~1 C O
C Il C Cl C C C eC C iOE*it C R C STRESS CORROSION CRACKING EVALUATION COMPANY DUANE ARNOLD ENERGY CENTER LINE NO. SYSTEM REVISION - DATE PAGE RRH RECIRCULATION RISERS - LOOP A (N2H) 0 11/11/80 A9 IsunEG IW HE AT CARSON SfAi$$ STRESS T TREAT ENT n eR inl' fl 0 EC A 10 ER g 00 I wtLV n ny y A 0 304 1 600120-1B 0.059 ALSO Sil0lti (N IE. AS 1 24-1) F1 iCn-J2 10 ILir-A SW X 1.90 AMPII!R FORGED A182-F304 6 S?624 0.070 RRil-J7 10 A-P FW X 1.14 PIPC (15-2) SMLS A376-TP304 5 2P3687 0.051 RR!I-J5 10 P-E SW X 1.55 A .W -67 ELBOW 3 37845-1A 0.061 Rrdi-J4 10 E-P SW X 1.57 PIPE (10-1) SES A376-1?304 5 2P3687 0.051 Ridi-J4A 10 P- P FW X 0.98 PIPE (15-1) S LS A376-TP304 5 2P3687 0.051 LD N 178 RRil-J3 10 P-P iW i .T 1.23 SAfli-IND IURGED M-336 Gl. F8 7 MS3S 0.030 i I:X11NS10N RIUI-F2A 10 P-ff IM x 1.02 0
l G.S Sb-166 INGNil 7 NX9923 0.06 Wii-END REPLACED IN 1978 fN 11 Ridi-F2 10 Sli-N0Z IW X 1.03 RIIIRC INIJ.T RWID SA-508 CL.2 IAM AI.lDY S11.EI, "- NA --
N0ZZlJi
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id7it c nic STRESS CORROSION CRACKING EVALUATION L5"' ' " '"
c0MPANY DUANE ARNOLD ENERGY CENTER SYSTEM nEVis10N - DATE PAGE LINE NO.
RECIRCULATION BYPASS LINE - LOOP A A10 RBA 1 14/11/80 NunEG 5"0' utAi canson sNlus sinfss
' " "* NE"' ss =c c non comufnis NEin n!!0 C8"' * "T "s^rYc5l'c'dIO IatAT- NEin fin'i YNE m0 == m ::
W5
- F
,a ax F
2 WELD 0LET FORCLD A182-F304 6 0.060 ALSO SilotN (N PG. A4 RM-J1 4 WOL-P FW X X J.22 PIPE SILS A376-TP304 5 2P3535 0.053 RM-J2 4 P-E SW X X 1.40 A
ELBOW (90*LR) gA376 3 1
0.047 RM-J3 4 E-P SW X X 1.50 PIPE SGS A376-17304 5 2P3371 0.057 RM-J6 4 P-T IM X A I.03 SR.S A403-WP304W-67 37368 E 3 0.060 FRtN A312 CFRP RM-J7 4 T-FL SW X X 1.16 I RGED A182-F316 4 E1460 1.060 0 3G)
BLIND FIANGE 10RGED A182-F316 4 E1460 1.060 g 98.S A403-WP304W-67 3 37368 FIOl A312 CFRP 1.060 tl.S0 SignWN ON PC. A4 RM-J8 4 T-P IW t X 1.94 PIPE 99.S A376-TP304 5 2P3371 1.057 RM-J9 4 P-E SW X X 1_75
((j LJ C CD EJ CJ CJ n L_ J I J CD n CJ O C] L_J O_ C] []
%) w i07i C7a.C STRESS CORROSION CRACKING EVALUATION
'5"',**'"
co ,, DUANE ARNOLD ENERGY CENTER SYSTEM REvlsl0N - SATE PAGE LINE NO.
. RBA RECIRCULATION BYPASS LINE - LOOP A (CON'T) 0 11/11/80 All Nunes snor ug a, cansaN sf!lus stress 8R INI FI D SPEC CA10N 1 EAT- gn INI ff Ob b X Ct "f f ELBOW (90*LR) g I)f g0 W3m-67 3 0.047 IINER SC 10 CASTING RBA-J10 4 E-V W e. X 1.52 111G1 RESISTA?LT TO IGST VAIXE CNiT A351-65 CR. CF8 7 41706 0.08 81 l'ERRilli (m-F032Al RBA-J12 4 V-WOL W X X 1.31 8
WEll101ET IORGED A182-F304 6 E
0.060 ALSO SDN W I'G. A4
C I El C C C C C C ] C C C C C C C_ C
/
NJ) -
iOTitCEC STRESS CORROSION CRACKING EVALUATION
- "I I" DUANE ARNOLD ENERGY CENTER COMPANY SYSTEM REVISION - DATE PAGE EINE NO.
RCB RECIRCULATION SULTION - LOOP B 0 11/11/80 A12 NUREG SHOP HE AT CARBON STAT S STRESS N BR IN) P Il D WELD P "I I SPEC CA 10N TREAT- N BER ENT f!
RN NN 0 x g
RECIRC. SilCTION IURCED SA-508 CL.2 ~~~ '~
N0!2LE (N1B) 11W ALIDY SIEEL RCB-F2 X 0.97 22 NO2-SE SW SAFE-IND IURGED SA-336 GR. F8 7 :37S 0.023 LOWER SC RCB-J3 22 SE-P Iw e+ 1.01 IIIGil RESISTANCE TO IGSCC Clo l M 2P2470-4A 0.045 PIPE (1-1) 0 304
\ l LOWER SC 6 Sil0P WATLR SPRAY (110LI.D RCD-J4 22 P-E SW l d+ 1.35 111Q1 RESISTANCE 10 IGCCC
^ 2 300223 0.049 ELBOW (90'LR) 40 LOWTR 1C 6 S10P WATER SPRAY 000LLD RCB-J5 22 E-P SW 4 1.24 111Q1 RESIRIANCE 1D IGSCC Clol N 2P2470-1A 0.045
( PIPE (1-2) 0 3M 1 RCB-J6 P-T IV X 1.24 f 22 j 18" OlHIEF EXITd.lDED PRIOR 1U RIIUCING 111E TGW A403-WP304W 2 6003241 0.055 22"X22"X18" I:101 A240-69 lH%T 1RIAU126 RCB-J7 22 T-P SW A 1.32 SIDP WA1T.R SPRAY COOLED PIPE (1-2) 1 2P2470-1A 0.045 0 3M
!OWER SC G SIDP WATER SPRAY 000 LID RCB-J9 22 P-P SW ++ 0.89 11101 RESISTANCE TD IGSCC PIPE (2-1) f0 304 1 2Wie 0.M 0 lDWIR \C ICB-JIS 22 P-E IM 4+ 1.31 ll!GI RESISTANCE TD IGSCC
^ 300223 0.049 T Li(W(90*l.R) f 9g 2 RCll.ll6 22 1.-V lY 4* 1.32 in tower m restr
O : O O O O O O w t J n O O O L_.3 O O I7 O E ..O O O' -
IOU"iUc'"aic STRESS CORROSION CRACKING EVALUATION
N ER ff l0 0 X WELD gn un g
- 023B)
CAST A351-65 GR. (T8 7 39839 0.06 Ill IIRR11E IN ER 1C TO CASTI!C RCB-J18 22 V-P IW 9 0.96 111G1 RI51 STANCE TD IGSCC
" I PIPE (3-1) 0 04 1 2P2470-4A 0.045 tiWtR 1C tb biUP WATER SPRAY (DOLED RCB-J24 22 P-E SW 4+ 1.38 ,,,g,og,qr m m i m
^ 3 K51142-3 0.048 ELBOW (90*SR) 2 IN ER tC TO CASTING RCB-J25 22 E-Pp IW 4+ 1.57 11101 RESISTANCE TO ICSer IWIP CAST A351 GR. CF8Ft 7 14% FERRITE 0'
0.070 W 08 4 41167 DE00NTAMINATION FIANGE BLIND FI).* G C[.DA182-69 4 41167 0.070
E_a U._..: L ) O O i i E) r3 T Il. O O O c7 r~ 7 C_] O- O Ci.]
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iO A7t C a C STRESS CORROSION CRACKING EVALUATION COMPANY DUANE ARNOLD ENERGY CENTER LINE NO. SYSTEM REVISION - DATE PAGE RECIRCULATION DISCilARGE - LOOP B A14 RCB 0 4/11/80 Nunes SHOP CAR 30N SfATUS STRESS llE AT M I aR N) Pf fl D OMMNT SPEC CA I iREA g(g N SER , ff lh h E
X WELD gN Nu g g CAST A351 CF8M 7 y.yor 14% FERRITE RCB-J27 22 Pp-P IV X 0.97 PIPE (8-1) 0 T3 4 1 300075-1C 0.058 RCB-J31 22 P-V FW X 0.96 CAST A351-65 GR. CF8 7 44691 0.04 15% FERR11E
( F 31B)
RCB-J33 22 V-E IN X 1.24 A 3 W304W ELil0W(90*LR) q 2 600324-1A 0.055 RCB-J35 22 E-P SW e+ 1.22 SilDP WA1ER SlHAY QXXID PIPE (10-1) 0 iOl 1 3000J5-lC 0.058 RCB-J41 22 e'- P SW X 0.90 PIPE (10-1) N 0 504 1 300075-lC 0.058 FIDW RESTRICIER WELDED 10 PIPE I.D.
RCB-J44 22 P-T SW e. 1.43 Sil0P WATER SPRAY UDifD REI11CING 1EE RGW A403-WP304W 20" OltrtIT EXTRLIDW IRIOR 10 22X22X20 l' int A240-69 2 6825331 0.040 llEAT 11 TEA 1)RNr LOWl:R IC 00N11NT - 111Q1 RCB-J46 22 T-Cr FW e+ 1.33 RESISTANCE 10 ICSCC RElllCING CROSS RGW A403-WP304W 16" GTTLI'IS EX110DED PRIOR 1D
, 22X22X16X16 Fl4N A240-69 2 6825331 0.040 IDMT 1RIADENI l
IclB-J7 22 Cr-Cp SW e. 1.22 $110P WATER SPRAY COOLED A 6 WEl.D CAP p 4h 304 3 600225-1A 0.058 i
l l
m, s...:. -- ---
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iO!'.*itic7.ie STRESS CORROSION CRACKING EVALUATION i
L'8"',,,"'
c " DUANE ARNOLD ENERGY CENTER SYSTEM REVisl0N - DATE PAGE LINE NO' RCB RECIRCULATION DISCHARGE - LOOP B (CON'T) 0 11/11/80 A15 NUPEG sw0r , , , cAn On s,8lhis stress II RER m) fi D WELD T "(g)hTBON T IA g EMI
!f Ra G0 b a
X Ng 22" PIPE (8-1) [. 1 300075-1C 0.058 ALSO SIONN m PG. A14 RCB-J30 4 BPC SW X 1.08 UM R)RGED AIB2-F304 6 812680 BRANOI OMTLTim IOR 4" RECIRC.
22"X4" ga%g 0.060 DISOIARGE VALVE BYPASS LINE
^ 300075-1C 0.058 U.50 SIDWN m PG. A14 22" PIPE (10-1) 0 I- 4 1
RCB-J37 4 BPC SW X 1.25 IORGED A182-F304 6 812683 NI NUIN N 4" EE-22"X4" 0.060 lilSOIARGE VALVE BYPASS LINE (4%D l
t I
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O FR L.;] O F' l U~J i._J P1 O L._.J EQ O O O O O O e- -
iOS'A*" tC Yaic STRESS CORROSION CRACKING EVALUATION co *, 7'" DUANE ARNOLD ENERGY CENTER EINE NO. SYSTEM REVISION - DATE PAGE RECIRCULATION RING HEADER - LOOP B ij 11/11/80
^
RMB Nunts I# HEAT CAR 8ON STAT S STRESS TREAT- g CDNTENT SS NC C RULE COMMENTS 8R IN) Fi D $ C ICA 10 MINI MX WitD WI g A 3 W3MW-67 WEID CAP 4
3 K51404-4D 0.050 MB-J1 16 Cp-lur SW 9+ 0. % 90P WA1TR SPRAY COOLED RING RGW A358 CL.1 RISER (11TLLTS EX11u1DED PRIOR 10 1- 600120-1B 0.059 IIEAT REABRM IIEADER (11-1) IR N A240-67 T304 IBB-J6 16 lur-Cr SW 9 1.45 90P WATER SPRAY 000 LED RElllClilG C10SS - R4W A403-WP304W '
AISO SDM ON PG. B14 2 6825331 O*040 22X22X16X16 1101 A240-69 l 14B-J8 16 Cr-lur SW 9* 1.35 90P WATTR (; PRAY rmt Fn RING R4W A358 CL.1 RISER ClTIlf13 EXTRUDID PRIOR TD Fiol A240-67 T304 1 600120-1B 0.059 IIEAT READEM
, IG-ADER (11-2) l j RB-JI2 16 lur-Cp SW 9+ 0.% 90P WA1TR SPRAY 0001ED A W3MW-67 WELD CAP 3 K51404-4D 0.050
w.1 C Il [I [ _] C C C R I - [] C C C C C L -L C C o)\.
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iOO"it C ac STRESS CORROSION CRACKING EVALUATION UGHT 6 N ER COMPANY DUANE ARNOLD ENERGY CENTER SYSTEM REVISION - DATE PAGi LINE NO.
RRA RECIRCULATI0fi RISERS - LOOP B (N2A) 0 11/11/80 A17 NUREG
$NOP HE AT CAASON STA US STRESS U T eR ( N)' FI O SPEC cA 60N MEN N OO O X Wild gN Ng g 0 7 T304 1 600120-1B 0.059 SMt.11-2 m M N N. A16 i 11-2)
RIB-J11 10 tur-A SW X 1.95 ADAPIT.R IVRGED A182-F304 6 52624 0.070 RRA-J7 10 A-P IM X 1.16 PIPE (16-2) SMLS A376 - TP304 5 2P3687 0.051 RRA-J5 10 P.E SW X 1,57 A 03 E0W67 3 37845-1A 0.061 ELBOW (90*LR) 9 RRA-J4 10 E-P Sw X 1.63 PIPE (16-1) 92.S A376-TP304 5 2P3399 0.055 RRA-J4A 10 P-P IM X 0.98 PORTION OF SIVOL 16-1 MAS QTT CLIT PIPE (16-1) SILS A376-TP304 5 2P3399 0.055 M4D REPLACED IN 1978 PRA-J3 10 P-P iW X 1.23 ,_
ON IURCI SA-336 CR. F8 7 M53S 0.030 RRA-F2A 10 P-SE IW X 1.02 D
91LS SB-166 INCmEL 7 NX9923 0.06 SAFE-D4D REPIACED IN 1978 RRA-F2 10 SE-N02 TW X 1.03 RECIRC. INIIT IVRGl'.D SA-508 CL.2 N0ZZLE 11W ALIDY STIIL ---
NA ---
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iOOATC7RIC STRESS CORROSION CRACKING EVALUATION L'G"' * *E" DUANE ARNOLD ENERGY CENTER COMPANY SYSTEM REV!$10N - DATE PAGE LINE NO.
RRB RECIRCULATION RISERS - LOOP B (N2B) 0 11/11/80 A18 Nunts SHOP NE Al CAR 8ON STATUS stile $$
WitD DIA. WELD OR MATERIAL TYPE 6 H I CONTENT $$ NC C llutt COMMEIIT3 COMPONENT TREAT.
IIUMBER 11N) TYPE flELO SPECIFICATION EE 00 0 MENT (%) INDEX WEta RN Ng y 1 600120-1B 0.059 SIVOL 11-2 ALSO Sil0NN ON PG. A16 1 11-2) 11 0 7 T304 RIB-J9 10 Itir-A SW X 2.19 AIRFIT.R IVRGED A182-F304 6 52624 0.070 r
RRB-J7 10 A-P FW X 1.25 PIPE (17-2) SGS A376 - TP304 5 2P3687 0.051 It'tB-J S 10 P-E SW X 1.75 A 03 304W-67 37845-1A 0.061 ELBOW (90*LR) y 4 3 RRB-J4 10 E-P SW X 1.59 PIPE (17-1) SILS A376 - TP304 5 2P3399 0.055 RRB-J4A 10 P-P FW X 0.98 0.055 2 1 hAS Off Otfr PIPE (17-1) SMLS A376 - TP304 5 2P3399 AN I # '1 RRB-J3 10 P-P FW X 1.23 FORGED SA-336 GR. F8 7 1153S 0.030 RRB-F2A 10 P-SE Iw I 1.02 IE 90S SB-166 INCINEL 7 NX9923 0.06 SAFE-IND REPIXED IN 1978 RRB-F2 10 SE-N0Z IM X_ l.03 RFCIRC. IN11T IOltGID SA-508 CL.2 .--
NA N0Z211 IDW Al.lDY Sl'lIL
C C C [] #
C C I~~7 C C C ~~'
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- I. _0[ ] %
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STRESS CORROSION CRACKING EVALUATION 1
iOO"I"CIR,C A
DUANE ARNOLD ENERGY CENTER N COMPAN REVISION - DATE PAGE llNE NO. SYSTEM RECIRCULATION RISERS - LOOP B (N20) AB RRC 0 4/11/80 1 NUREG SHOP HE AT CAA80N STATUS STRESS I COMMENTS TREAT- M ENT SS N RULE 8R INi FI D SPEC CA 10 Nh8ER INDEX MENT (%) ,, ,, ,
WELD vs F F 1 600120-1B 0.059 SPOOL 11-1 AlSO SIKM4 ON PG. Alb i 11-1) N 20 7 T'.04 X 2.10 icB-J5 10 lur-A SW ADAPTER FORGED A182-F304 6 52624 0.070 IM X 1.24 RRC-J7 10 A-P PIPE (18-2) SILS A376 "IP304 5 2P3687 0.051 RRC-J 5 10 P-E SW X 1.73 A WP304W-67 0.061
, ELBOW (90*LR) 3 37845-1A
. i9 E-P SW X 1.40 RRC-J4 l_
PIPE (18-1) SILS A376-TP304j 5 2P3399 0.055 RRC-J4A 10 P-P IM X 0.98 I "A3 M #
PIPE (18-1) SILS A376-TP304 5 2P3399 0.055 g 10 P-P IM X 1.23 RRC-J3 IORGED SA-336 CR. F8 7 H53S 0.030 3
l0 P-SE IW X 1.02 RHC-F2A IE 9tLS SB-166 INO[NLL SAFE-IND REPl>CED IN 1978 7 NX9923 0.06 RilC- k 2 to S' N0Z IW X 1.03 RECIRC. INLET FORGID SA-508 CL.2 ... g ...
N0ZZLE IDW ALIDY STLEL
fJ C C 5 i U R LJ i3 C C C C C C C l'~l C C@C O ~ 9-iOTEtCIe STRESS CORROSION CRACKING EVALUATION
('gypg', DUANE ARNOLD ENERGY CENTER LINE NO. SYSTEM REVISION - D ATE PAGE RRD RECIRCULATION RISERS - LOOP B (N2D) 0 11/11/80 A20 ermtG SHOP HEAL CARBON SfAY!S STRESS N NT
- " AT ENT "
NU B R IN) FI O $tEC CA 10 1,REA ER 0 x H "7 i
0 hT304 1 600120-1B 0.059 SM 11-1 M M W N. A16 i 11-1) 1 10tB-J2 10 ILir-A SW X 1.83 -
AIRITER IVRGED A182-F304 6 52624 0.070 RFD-J7 10 A-P IW X 1.13 ilPE (19-2) SMLS A376-TP304 5 2P3687 0.051 RRD-J5 10 P-E SW X 1,58 A 3 4 3 37845-1A 0.061 I LBOW(90*LR) g 0 RRD-J4 10 E-P SW X 1.44 PIPF (19-1) 9tLS A376-TP304 5 2P3399 0.055 RRD-J4A 10 P-P IM X 0.98 PIPE (19-1) 91LS A376-TP304 5 2P3399 0.055 , WELDF 1 8 RRD-J3 IO P-P IM X 1.23
- 110RGED SA-336 GR. F8 7 MS3S 0.030 0N RRD- F2 A 10 P-SE l'W X 1.02 D NX9923 Wii-IND REPIKED IN 1978 911S SB-166 INC(NEL 7 0.06 RRD- l'2 to SE-N0Z Iw X 1.03 '
RI~flRC. INLIT l M Gl'D SA-508 CL.2 N0ZZIli IDW ALIDY STIIL ---
NA ---
L .a O l_^ ! Q O '7 L !_ 1 i._ J O M C C C__3 F 9 C C.~3 r i E _;
O O e-iOETC ,1C STRESS CORROSION CRACKING EVALUATION L5"d,6 ['" , DUANE ARNOLD ENERGY CENTER llNE NO. SYSTEM REVISION - DATE PAGE RBB RECIRCULATION BYPASS LINE - LOOP B 0 11/11/80 A21 i IIUREG SHOP CAR 80N $ TAT S STIIE$$
MEAT Wil0 DIA. WELO OR MATERIAL TYPE 6 N FIELO COMP 000ENT SPECIFICATION TREAT.
IIUMSER (ENTENT SS NC C RULE COMMENTS NUMBER (lN) TYPE EE O0 0 wet 0 MM g Ne0EX gN NN N
- h. FOIKID A182-F304 6 0.060 h AISO SDN CN PG. A15 RBB-J1 4 MX.-P FW X X 1.23 PIPE 9ES A376-TP304 5 2P3371 0.057 RBB-J2 4 P-E SW X X 1.39 SILS A403-WP304W-67 20257 E W 90* W F101 A312 3 CFR0 0.047 RBB-J3 4 E-P SW X X 1.50 PIPE 953 A376-TP304 5 2P3371 0.057 RBB-J6 4 P-T FW X X 1.86 96S A403-WP304W-67 37368 RE Fint A312 3 0. %0 CFRP RBB-J7 4 T-FL SW X X 1.29 0
DA -F31b 4 E1460 0.060 IING) _
BLIND IUNCE FORGED A182-F316 4 E1460 0.060
' ^ ^
TLE 3 0.060 ,\150 S10hN ON PG. A14 A
! RBit-J8 4 T-P IW X X 1.99 l PIPE SRS A376-TP304 5 2P3371 0.057 l
Itllll J!8 4 P-l. SW X X l.73
E~J CZ2_ L_.J nQ CJ O C-] w Q (9 C3 C"3 C.3 CI.] b CC3_ CJ iOE*ItC7= STRESS CORROSION CRACKING EVALUATION co,,,, DUANE ARNOLD ENERGY CENTER EINE NO. SYSTEM REVISION - DATE PAGE RBB RECIRCULATION BYPASS LINE - LOOP B (CON'T) 0 fl/11/80 A22 NUREG 5"0P mal CARBON $ $ $TRES$
{g NENT SS REE ""$
NEOsSR ! uni Er{ r! C8""'"'
"EEC$$CA0N T,Rf,AT g
, X SILS A403-WP304W-67 20257 ELBOW (90*LR) 3 0.047 rRN A376 CFR0 RBB-J10 4 E-V Fw & X 1.52 ER T G j ;g,3,,, cast A35i-65 cR. cr. 7 41706 0.08 .s rERaiit RBB-J12 4 V-MX. IW X X 1.25 6 80 IWLED A182-r304 6p 0.060 AIJ50 SilDW ON PG. A15
,,b
C Il C C C [.--i C C C C h2 I I C C C C LJ i d'ATC7AiC STRESS CORROSION CRACKING EVALUATION comp [g DUANE ARNOLD ENERGY CENTER LINE NO. SYSTEM REVISION - DATE PAGE i
l RilB RESIDUAL IIEAT REMOVAL - LOOP B 0 11/11/80 B1 NUREG SHOP HEAT CARBON SfATUS STRESS WELD DIA. WELO OR MATERIAL TYM 6 HEAT COMMENTS COMP 00eENT SPEClflCATION TREAT- CDNTENT $$ NC C RULE l leUMBER (lN) TYPE FIELO EE 00 0 MENT (%) NIDEX
, Q1 "7 f l 1T.E ALSO SithN ON PG. A12 4
22"x22"x18" 1T.E 0 2 6003241 0.055 "B" RECIRC StXXICN LINE 11 RB-J1 18 T-P IW X 1.18 PIPE (P1) RGW A358 1P304 CL. 1 4 328258 0.033 RlB-F3 18 P-P SW X 0.82 SFILS A333 GR. 6 PIPE (P2) mg
--- NA ---
l PIPE (P1) RGW A358 1P304 CL. 1 7 328258 0.033 R B-J2 4 BPC SW ,
y l CONNL ON !LR 4" (P-WOL) WEll10LLT 18"x4'- FORGII) A182 F304 7 110G 0.05 ,g
! .] ~ Q C C C C C C C L3 C M C C . C'l C.0;I~' O[l e ' _]
iOE"It CIRC STRESS CORROSION CRACKING EVALUATION "I
CouPAN DUANE ARNOLD ENERGY CENTER EINE No. SYSTEM REVISION - CATE PAGE RHC RESIDUAL HEAT REtiOVAL - LOOP A (20A) 0 4/11/80 B2 NURf6 SHOP HEAT CARBON STATUS STRESS
+_
L.] l C C U C C '
C C C C C M C C_'Q C ul >O O - -
EATC7RC STRESS CORROSION CRACKING EVALUATION DUANE ARNOLD ENERGY CENTER C
SYSTEM REVISION - DATE PAGE EINE NO.
RHD RESIDUAL HEAT REMOVAL - LOOP B (20B) ,
0 11/11/80 B3 NuREs
WELD N 22"x22"x20" 1TE EXTRUDED A403 - WP304W 2 6825331 0.040 T..TE AISO SE1NN (N IG. LINE A14 Fini A240 B" RECIRC DISO WtGE h1&J1 20 T-P FW X 1.29 PIPE (P1) Rf.W A358 1?304 CL. 1 7 318435 0.060 f4 & F2 20 P-P SW X 0.84 SilS A333 CR. 6 --- NA ---
PIPE (P2) mg
- l. '
r 1
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L;'
-i i' APPENDIX B t_a l
l
, i r STRESS RULE INDEX EVALUATION SUmtARY L
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. KEY FOR SIRE 55 kwtE th0L X EVALUATION - SunnAky .
.e eeeeee e eee eee e e ee **e o o e e e e e eev o o oos e *
- e e e e e eeo* * **** ** ** **o* ***** *
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t til ISI held Number atLD ID Pipe Fabricator's Weld Number utLD TYPE Components Adjoining Weld PSPs Silt Pipe Diameter (in.)
N00E NO NSC Stress Analysis Mode Number COMP TYPE Component Type Used in Determining NS-3600 Piping Stress Indices
= ..._ _
______.... ...__. = . . ..
81 / 82 hl C1 / C2 h NS-3600 Piping Stress Indices I
K1 / K2 SitPNESB Pressure Stress Intensity (psi) 53 IDul Dead Weight Stress Intensity (psi)
SIITHEkl Thermal stress Intensity (psi)
PM e P8 Primary Stress Intensity (psi)
PM*PoeoeF Primar'/ plus Secondary alus Peak Stress Intensity (psi)
O e F Secondary plus Peak Stress Intensity (psi)
RESI ST Wald Residual Stress (psi)
YlELD ST Code Minimum YleLd Strength of Piping Material at 550*F (psi) 70 0. ELA. Young's Modulus of Piping Material (psi)
Sul PRI Stress Rule Index - Primary Stress Component
%Nis5EC Stress Rule Inden - Secondary Stress Component SWI ICIAL OveralL Stress Rule Index
[] C] C C LC O C C d C C C Il C C C I l. C C3 1
O O -
, eseeee.cooooooooooseeeeeeeeeeeeee****eoosecococoooooseeeeooseseeoooo***eooe**oosoeeeeooooooooose***eoosseseeooooooooseeoosseeeeee i 5C0R E e o NUTECH -- VERSION 1.0.0 -- PAGE 29 e o DuaNE ARNOLD REC!RCULATION PIPING, LOOP A 18 04/01/80 o oooooseeeeeeooooseeeeeeeeooe**eooooooooooooooooooseeooooooooooooeseeeeooo****eeeeeeeeeosoooooseeeeeooseeoeooooeeeeeeeeeeeeeeeeeee o STRESS WutE IN0ER EVALt'ATION - SumM ARY e se es.',o e e e e e e e e e e e o++ v oo s e e e e e o o o o o o o o o o o o o o o o o o o s e c e s e e e s e o *
- e o o o o o o o * * * * * *
- e s e e o o o o o o s e e e e e e e o o o o o o o o o o o o o o o s e e e e e e o e o s ee o o oo o o i
l I5I RCA-J3 RCA-J4 RCA-JS RCA-J6 ACA-JF At WELO ID RS-N-Al-A RS-L Al-S A2 RS-N-AZ-C j dELD TYPE SE-P 'P-E E-P P-P P-P
, rtPE SIZE 22.00 22.00 22.00 22.00 22.00 i
NONE NO 10A ISA 20A A2 SNA2C COMP TYPE TRAN5 EL80WLR EL80WLR PIPE PIPE 81 / 82 .50/1.00 1.00/3.52 1.00/3.52 .50/1.00 .50/1.00 C1 / C2 1.37/1.50 1.23/4.70 1.23/4.70 1.10/1.00 1.10/1.00 K1/K2 1.20/1 80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 5ttPRE58 12388.70 12388.70 12388.70 12388.70 12388.70 5I (DW3 716.42 140 12 344.64 215.70 0.00 Sl(THER) 1145.68 1038.97 699.63 S43.29 0.00 PM e PS 6910.78 12892.15 13602.37 6410.06 6194.35 PMePeeceF 2$432.10 28324.31 27184.80 17719.27 16353.09 0 e F 18521.33 15442.16 13582.43 11309.22 10158.74 RESI ST 28000.00 28000.00 25000.00 28000.00 28000.00 YIELD ST 18800.00 18800.00 18800.00 18800.00 18800.00 M00. ELA. 25666000.00 2S666000.00 25666000.00 25666000.00 25666000.00 SRI.PRI .3676 .6852 .7235 .3410 .3295 SNI.5fC .6633 .6194 .5929 .S605 .5441
____...._____ _ . . ._____..___.....__ . ==_...__.... ...-- .____.... .
5el total s.0309 1.1047 1.3164 .9015 .8736
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- e e o e e e e i N 4 e o e e me m er e 4 ee e e -e e m P.e O O O l e e N e e o N4 e % % % e O M se e e O O O 1 P. e e e e e "D 1 O E O e O m e 6' P= 0 m O e O 4 e o e e e e $E O O ly O e N N e N P= e e 4 en F' 1 e
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- 4 O O e P* N m O e e O O O 1 m 4 1 ?
e e e 1 8 e o e o e e e e e e e e 1 N e '
O e ee o em a se .* e m O ce e P= O O O 4 e N e e e =* 4 3 % % % e a e e m o O O O 4 a e e ed o e ** I O 5 O O O m e e e .e o e O e e e r' e e
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- e 9 se se se e e O =* N se O O O m N O 4 e e. e he e =e 1 % % % e P= c P. O m O O O O m 4 1 ?
- e O e 4e 9 O e i O P= O m me e m =e P= O e O 1 e e I e
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,l e U == W e w e 9 j e eg*Qe i I e e ag== e 2 e N O O O O e Pm Pm O O O O O 1.s e w u e ==
- e P= e P= c as m P. e O O O N e i e e > u,, e o e e o e e e e e o e e e P 7 $ e e m er 1 m e .e e =e P=
- e O O O O e P= 4 m o I er es e w e. -s .J % % % e e o e m O O O P. e I e 9 e I e3* 9 c. E O m o m e e O ** 4 O e o I e e i e i
e c e er e i O O O N N N e 4 N e e e l l .e e .J e e 4 > e 4 e o e e se me N me N es e l
~l e oeee um i N O s .* 4 i e reee ac 4 w es a w e i e orawe N 8 e 4 e as * $ $ ,
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e I e e e 1 1 O O O ~ ~ ~ e -e e e 4 9 o e e 4 0 m e 4 e o e e =e =e N -e N se 4 $
i o e e ue i N e .J =e ce =* 4 e e e Wg & N m W @ l O 4 e $ N O e e e 0 0 tm o e e t i $
1; ' e o e 4 $
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i teeeeeeeeeeeeeeooseeee****ooooseeee**o**eeeeeeeoseeee******Jeeeeeeeeeeeeeeoceeeeeeeee***eoooooosecoeoecesseeeeeeeeeeeeeoeooseseos e 5C0R E
- e NUTECH -- VER$10N 1.0.0 -- PAGE 31
- O OUaNE ARNOLD RECIRCULATION FIPING, LOOP A E 8 04/01/80
- eeeeeeee ee eee eee e ee eeeeee e eeee e ee e e ee e ee eee ee ee e e e e e eee eeeeeee ee ee eeee eee eeee eeeeeeee ee e eeee eeeee ee e eeeeeeeeeeee eeeeeeee eeeeeeeee 3 e STRES5 RULE IhDEX EVALUATION -
SUMMARY
e
- eseee.co.eeee.eee.eooeeeeeeeeeeeeeeeee**eeeeeeooeeeeeeeeooes**eceeeeeeeeeeesseeeeeeeeeeeeeeeeeeeee.ooeeeeeeeeeeeeeeeeeeeeeeeeeeee t
\
I5I RCA-J22 RCA-J24 RCA-J27 RCA-J28 RCA-J30 WELD 10 A5 A6 RD-A-Al-A A7 A8
)
i 81 / 82 1 00/4.62 .50/1.00 1.00/2.35 .50/1.00 1.00/3.18 C1 / C2 1.46/6.15 1.36/1.48 1.50/3 13 1.36/1.48 1.23/4.24 K1 / K2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 SitPRE55 12388.70 12748.55 3987.40 12748.55 12748.55 l 51 (DWI 1061.17 294.64 179.63 94.27 227.62
, SIITHERI 526.47 436.32 2766.79 365.14 505.85 i
PM e PB 17286.24 6668.91 4409.40 6468.55 13472.75 1
i PMeP8*0eF 39299.10 22814.02 23790.24 22088.29 24459.25 l
' Oe F 22012.85 16t45 10 19380.84 19619.74 10956.46 RESI ST 28000.00 28000.00 39000.00 28000.00 28000.00 YIELD ST 18800.00 18800.00 18800.00 18000.00 18800.00 M00. ELA. 25666000.00 25666000.00 2S666000.00 25666000.00 25666000.00 SRIePRI .9195 .3547 .2345 . 3 4 '+ 1 .7166 5RI 5EC .7131 .6295 .8324 .6220 .5559 SRI TOTAL 1.6326 .9842 t.0670 .9660 1.2725
O E. En a a r' L_J L.J Q Q Cn a a rn a a O a .
a
(
, ....e.eeeeeeeooseee..ee.oooo.oeseco**eee.o.eeeeesesee...oo eeeeeessee..oo.co..oo...ee.ee.co..**.e.o.o.oo..o.oo..ooe..oecocesecoe
. 5coR E .
9 NUTECH --
WEASION 1.0.0 -- PAGE 32
- I e QUAhi AdNOLD RFCIRCULATION PIPINGeLOOP A E d 04/01/80 e eeeeeeeeeeeeeeoceeeeeeeeeeooooooseeeeee***eo***eeeeeeeeeooooooooooooooootse***eceoeoooooooe.coosecesseeeeooooooooooseeeeeoososeee j e ST4E55 RULE INDER EVALUATION - SUNNARY ,
e seeeeeeeeeeeeeeeoeoooooseeeeoseoeceseeee***eseeeeeeeeoeooooooooseoooeseeeee***eoooooe***eoseeeeeeseeeeoeoooooosecocoeeeeeeeeevoes 151 RCA-J32 RCA-J34 RSA-J1 RSA-J2 R8A-J3 l WELD 10 20-N-A2-4 RD-N-A2-8 A14 RD-N-48-A RD-N-A8-8 MELD TYPE E-P BPC WCL-P P-E E-P PIPE SIZE 22.00 6.00 4.00 4.00 4.00 i
j N00E NO 120A 125A A18 130A 135A COMP TYPE EL80WLR TEE PIPE EL80WLR EL80WLR 1
.. .._____ = . . . _ _ - . . . . _ _ . _ _ _ _ _ . _ _ _ _ . . _ ..
1 81 / 82 1.00,3.18 1. 00/2.35 .50/1.00 1.00/2.43 1.00/2.43 C1 / C2 1.23/4.24 1.50/3.13 1.10/1.00 ,1.27/3 24 1.27/3.24 K1 / K2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 j
SIIPRESI 12748.55 3987.40 8031.90 8031.90 8031,90 SI (OWS 208.79 1115.00 591.19 76.24 155.46
'! SiliHERI 444.8F 2860.54 9106.68 3049.46 4088.63 P9
- PB 13412.8F 6606.90 4607.14 8217.26 8409.89 PMeP8eQeF 23849.85 29S93.08 20058.27 30437.64 36963.89
~
l 4e F 10436.99 22986.19 23451.13 22220.38 28554.00 l
RESI ST 24000.00 39000.00 45000.00 45000.00 45000.00 YIELD ST 18800.00 18600.00 18d00.00 18800.00 18000.00 a00. FLA.
- 2S666000.00 25466000.00 25666000.00 25666000.00 25666000.00 Skt.PRI .713S .3514 .2451 .43F1 .4473 Sul.5FC .S441 1839 .9740 .9585 1.0488
___.________ . . . - - - __-__.=_= . _ _ _ . . . . . _ _ _ _ _
bl IdIAL 1. 2 f.14 1./343 1.2211 1.3956 1.4961 i
C (R f7 d C U l) C C .I LJ Q O M C C Q >
- ........................e.............................................................................................e........e.
- 5C0R E o
- EUTECH -- VERSION 1.0.0 -- PAGE 33 e
- DUAhE ARNOLD RECIWCULATION PIPING, LOOP AE8 04/01/80 *
\ eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee l
- STRESS AuLE INDEN EVALUATION - $UMMARY ,
eeeeee e e e.e e e s se e ee ee e e e e e o s e e e e ee e e s ** e eoo o o o o o o es e e e e e ee e e e ee e e e eee o o o o o o o o o s ee ee e e o s o se e **
- e e * * ** e *
- e o oe oe oo o o oo ooooe oeee eooo o 1
J
' I58 RSA-J6 RSA-JS RSA-JF RSA-J9 R8A-J10 l WELD ID A19 A20 AD-N-A9-A RD-N-A10-A A21 i WELD TYPE P-T T-P T-FL P-E E-V PIPE SIZE 4.00 4.00 4.00 4.00 4.00 NDDE NO 140A 140A 1904 150A 155A I
COMP TYPE TEE TEE TEE EL80WLR EL80WLR d
81 / 82 1.00/1.69 1.00/1.69 1.00/1.69 1 00/2.43 1.00/2.43 j C1 / C2 1 50/2.26 1.50/2.26 1.50/2.26 1.27/3.24 1.27/3.24 i El / K2 1.20/1.80 1.20/1 80 1.20/1.80 1.20/1.40 1 20/1.80 SIIPRESS 8031.90 8031.90 8031.90 8031.90 3031.90 5I IONI 459.35 1446.17 0.00 740.30 405.85 SIITHER) 10590.04 10406.92 0.00 5588.41 3889.88 PM . P8 8809.42 10479.74 8031.90 9831.86 9014.69 PM+P8*0*F 59343.71 62608.58 14457.42 49128.28 37265.23 0 *F 50534.30 52128.83 6425.52 39296.42 28246.54 i RESI ST 45000.00 45000.00 45000.00 45000.00 45000.00 i
j VIELO ST 18800.00 18800.00 18800.00 18800.00 18800.00 MOD. ELA. 25666000.00 25666000.00 25666000.00 25666000.00 25666000.00
SRI TOTAL 1.8304 1 9424 1.1605 1.7249 1.5241 s
C3 C Il C C C C C C f
.] C C C C U C C C C o- g
(
4 1
eeee ee e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e ee e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e ee e e e e e e e e e e ee e e e e e e eee ee e e e
- 5CDAE o
- MuTECH -- WER$10N 1.0.0 -- PAGE 34
- e DUANE ARNOLD RECIRCULATION PIPING LOOP A 18 04/01/80 e seeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee
! e STRESS RULE INDEX EVALUATION -
SUMMARY
e seeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee**eoooooeeeeeeeeeeeeeeeeoooeceoceecoeeteoooooooooeseeeeeeococeecesooooseeososeeeeeeeeeeees
! I5I RSA-J12 RCA-J38 RCA-J41 RCA-J43 AMA-J6 WELD ID A22 RD-N-A2-E R0-N-42-C A9 RD-N-A3-E j WELD TYPE V-WOL P-P P-T T-CR CR-CP PIPE SIZE 4.00 22.00 22.00 22.00 22.00 l N00E NO 167A 173A 175A 180A 185A i
! COMP TYPE TRANS PIPE TEE TEE TEE I
j 81 / 82 .50/1.00 .50/1.00 1.00/2.35 1.00/2.35 1.00/2.35 C1 / C2 1.34/1.45 1 10/1.00 1 50/3.13 1.50/3.13 1.50/3.13 i
K1 / E2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 l 5IIPRESI 8031 90 12748.55 12748.55 12748.55 12748.55 4
j SI IDiel 1623.18 5.23 98.48 398.75 0.00 i
j SilTHERI 5460.72 195.94 219.90 511.41 0.00 i PM e PS 5639.13 6379.51 12979.91 13685.35 12748.55 PM*PS*0eF 31448.36 17190.16 24742.49 20079.18 22947.40 Qe F 25809.23 10810.65 11762 59 14393.84 10198.84
]
f RESI ST 45000.00 28000.00 28000.00 28000.00 28000.00 l YlELD ST 18800.00 18800.00 18800.00 18800.00 18800.00 t
I MOD. ELA. 25666000.00 25666000.00 25666000.00 25666000.00 25666000.00 l
SRI.PRI .3000 .3393 .6904 .7279 .6781 5R1,$EC 1.0097 .5534 .5670 .6045 .5447
.._....._.._. ...~ . _ . . - - - . . . - _ . _ .
5RI TOTAL 1.3096 8927 1.2574 1.3324 1.2228
L _J E .> r- 1 L__.; O E. .3 t_.] o a r -) O L.__; rn aa a a a .
t_a
......c o . . . . . . . . * . e . . * . . . . . . o . . . o e c e o o . . . o e . c o c e e . c o c e s e . o o e . c o o * * . 0 0. . o * * * * * * . * * * * * * *
- e . * * * * * * * * . e . o o e t e t e * * * * * *
- e o o o o * * *. . ..e e e e 5C0R E .
e NUTECH -- VERSION 1.0.0 -- PAGE 35
- O DUANE ARNOLD RECIRCULATION PIPING. LOOP A E8 04/01/80 *
, eeeeeeeeeeeeeeeeeooooooseeeeeeeee***eteeo******eo********eocee*******eoo************eestotese*********************eo000eceece****
e STRESS RULE INDEX EVALUAil0N -
SUMMARY
e soeeeee e e e e o s e e e e e e e e e ee o o o o o s e c o e e e e s.e e s e e e * *
- e c e s s e e e * *
- e e e o o e * * *o o o o o *
- e o o * *
- o o o o o e t e * *
- e o o e e e e * *eo o * ** * ** e c e ee e ee o* **** oo o o o I5I RMR-JS RMA-J4 RRG-J7 RRG-J5 RRG-J4 WELD 10 RD-N-A3-D RD-N-A3-C A12 RD-N-A6-8 AD-N-A6-C q WELD TYPE HDu-CR HOR-A A-P P-E E-P P!PE SE2E 16 00 10.00 10.00 10.00 10.00 NODE NO ,1874 190A ADATR 195A 200A I COMP TYPE TEE TEE PIPE ELBOWLR ELBOWLR I
I i
! B1 / 82 1.00/2.35 1.00/2.31 .50/1.00 1.00/3.18 1.00/3.18 I C1 / C2 1.50/3.13 1. 50/ 3.09 1.10/1.00 1.26/4.24 1.26/4.24 i
K1/ K2 1 20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 5t! PRE 53 12482.49 11930.12 11930.12 11930.12 11930.12 St EDWI 167.25 470.40 870.40 567.81 227.12
\
l 5t!THERI 1941.48 9150.02 9150.02 3204.63 2603.61 PM e PS 12875.42 13944.97 6835.46 13735.73 12652.34 PM+PBe0+F 34358.26 77144.38 33784.50 46798.68 39611.68 0o F 21482.84 63199.40 26949.04 33062.95 26959.33 4
RESI ST 30000.00 33500.00 33500.00 33500.00 33500.00 l
l VIELO ST 18800.00 18800.00 18800.00 18800.00 18800.00
] MOD. ELA. 25666000.00 25666000.00 25666000.00 25666000.00 25666000.00 SRI.PRI .6449 .7418 .3636 .7306 .6730 1
i SRI,5EC .7341 1.3 Fa t .8619 .9491 .8621
^
l d
SGI TOTAL 1.4169 2.1206 1.2255 1.67'77 1 5351 1
i
P t
t LJ eOOOOOO e e e rd . e e e e 40e e
'.. e mee e 6 e %e e o =a e o e woe e e
g e o%e e 4ee e jm e e. O e *
- e e w e e e e e e e o e e o p e e.
. e. .
e e y e .e
- e. e e e e o e e e e e e C e e o e
- O N a O e a e O O O i, e e e v =e e
as e = e e e e O o
O O O O e e 4 e o O $ e e o e e e e e e e Pm p e W e e e P* W ls m e =e O N e =a e e as O O O e O 4 e e o e4 .A % % % m m e e e O O O 4 e e e o e =D t O 3 O 4 O e as O m e m e e O e e e o e e 52 O 4 O O N N es m N N O m e 4 -e e e e Zt e. o O e e e e ee se e m m as e e e e aO O O M .4 se me as e e e e um w me N w e u e e *e N e e e o e e - t e e e $
e o e i e e O m
[
e e e ls N O e O e O O O $
e e e e ** N e me eo e ee ee m O O O e e O P e o e t 8 o e e e e e o e e g se m t e e ao e P= m i m e =4 O e o e o N O O O ls 4 e I e e *
- e4 y 5 % % % m e e m P 4 O O Q e e e e ens e e =t I O m 5 0 4 O e
- e se e e e e e e o e e o e *>e 12 O 4 O 9 O N N N N O e m e e **
i O 4 ewe Z4 w e e e $ e o e =e .e g N m se e e e4e sO 9 O N =a ** =* ** 4 e e.
- E o Wm en =4 N W e L- e e
CeEe N oe3e e 9 e =.se a e oe F e oe 8e l e ze e O e O P O O e m e O O O e e == a 2 e as i O e e *e O O Pe N @ O O O O ** P=
L e e
i e. e o e 1 == * == e m
$ 5 ls e
- e e
=e e
=e N e
O o
O e e e
- e m O e o O
e O
e l
i N
m e
N me 4
e e. e s= * **
- W % % % e e O 4 0 e e I m e P e O e4e "5 I Q. O en O 4 O e N e == O e O I e e 9 e e et tX X O 4 3
- m N N 4 O o e o E l e w O o .e .a3e 4 e T e O as e o e e ce .e* m .* e 1 6 e e == e 4
- EQ e. 4 N W *e se 4 e g se e= e y e gg u se N ti= c l 9
g o 4 ewe N O $
e Q z .J e
- 0 I e c 3 e as e l t e u == u e w e v $
i e en u e O e E e en er ==
- E o O O O N e P= se m N O O O I e w u o == e O O e se d se P* e se O O O e e $ N
' e >We e e e e e e e e e e e e e i e O l @
e aowe 8 =4 ** =4 O M e e se m O O O [u N N 9 e e t * .A e Pm 1 % % % M M ** P 4 4 O O O m e 4 **
e j e3e ** O M j O O O P es e O =e O e e O l e *
- e Qeae O e= w e se N .e P* d O e m e 4 ed
[
i a 5 e ae e 1m e. e 4 e. lu e e e me m N m se 4:
o ceee m se i O O em se se 4 lu
- 2eee a4 4 se 4 en j e e Wewe u N le e 4 e og
- 0 $
. e e e= e 0 $
i y e wewe 0 $
I e Xe o 8 8 l
4 e 0 - e O ~ O N e e o O O
- e. 3 e e l e O e N .* O.e
. 4 e O O O ls N e O
"' e oe e t 0 e e e e o e e o e e e e me m eP6 e e e m 0 N M ** O en e m =e e O O O I e e e o e e N4 8 % % % M m P* e Pm N O O O I 4 N e
- b. , e o e =e I at O O O O P as e N P P= un e O e e 0 +
e 12 9 4 e N =* P* N em m m e 4 =e **
t o. e. e 4 e = O. e w O. e e .e -e 4 e m .* 4
. . e so o O as . .* .e .e e la o e e am Z me N a= est 9 e o e N t e e o e e o e e I '
(' e e e e a t e e e $ i e e e l
[_]' L) F7 O C C3 I"] U ! I r] y [] y (*] g F. 7 (( [] [t j [ . . .
l l
...e...............................e...............e.e.o....o..e.........o.........e..................e..o........e..............
e 5C0RE
- e NUTECH -- WERSION 1.0.0 -- PAGE 37
- e DUANE ARNOLD RECIRCULATION PIPING LOOP A &B 04/01/80 e eeooooeeeeeees.oooooooseeeeeoseeeeeee***oeotese***.eeee*****eoeeseeoeooooooooooseeeeeeeeesseeeeococeoeeeeeeeeeeoooooooooooeeeeeos e STRESS RULE thDEX EVALUATION -
SUMMARY
6 00000e0eeoe00000o0000000000e***o**etete**o***o**etete******************************e000000********e**0000040000000900044900000000 ISI RMA-JF RMA-Je RuF-JF RRF-JS RRF-J4 WELD ID RD-N-A3-F RD-N-43-G All RD-N-AS-8 RD-N-AS-C WELD TYPE CR-HDR HOR-A A-P P-E E-P PIPE SIZE 16.00 10.00 10.00 10.00 10.00 NODE NO 237A 2404 ADATR 245A 229A j COMP ftPE TEE TEE PIPE ELS0WLR EL30WLR t
j . _ _ _ . - - _ .
81 / 82 1.00/2.35 1.00/2.31 .50/1.00 1.00/3.18 1.00/3.18 C1 / C2 1.50/3.13 1.50/3.09 1.10/1.00 1.26/4.24 1.26/4.24 K1/K2 1.20/1.80 1.20/1.00 1.2C/1.80 1.20/1.80 1.20/1 00 ,
SIIPRE55 12482.*9 11930.12 11930.12 11930 12 11930.12 5I IDWD 145.50 802.20 882.20 612.61 218.54 i
SitTHER) 1380.76 5263.53 8263.53 3276.00 1492.08 PM + PS 12824.32 13972.29 6847.26 13878.17 12625.06 PM+PB+0.F 31074.07 72284.89 32210.06 47685 28 31063.16
{ 0+ F 18249.T6 50312.60 25362.80 33807.11 18438.10 f
RESI ST 30000.00 33500.00 33500.00 33500.00 33500.00 l
YIELD ST 10000.00 18000.00 18800.00 18800.00 18800.00 I
! M00. ELA. 25666000.00 25666000.00 25666000.00 25666000.00 25666000.00 SRI,PRI .6521 .7432 .3642 .7382 .6715 I SRI,5EC .68eo 1.3091 ,.8393 9597 .7406 i SRI TOTAL 1.3701 2.0523 1 2015 1.6979 1.4121 i
j
O F l O O O O O O O O O LJ O E1lJ E] U w O[J %; O - -
ee.......................................................................................................................e..o...e
. 5C0ae e o suffCH -- vtR$10h 1.0.0 -- PAGL 38 e e OuAht ANh0LO REClkCULAllbN PIPING. LOOP A L 4 04/01/50
- eee...........ee..e..e..+........**.e.***....*******..**.****.*.....*o*..**.****o***es.***.*********************ee.***ece*es*****
e %ihE55 kuLE IN0EE EVALUATION - SUM 9&MY
- oeee.....e e .....e e......ee e e ee e.e.oo ee. ...e e.e..o oo ooo o e.o oo oe s e.eooo ooo e.ee ee s.ooe.o e e se ee ec es e..eeeeoo es ee ee ee eeoo oo osee eeee e, 151 RNA-J10 kRE-JF RNA-J11 RRE-JS kRE-J4 stLO ID RD-N-A3-H A10 RD-h-43-J A0-N-44-8 RD-N-A4-C dELD TYPE HOE-A A-P HDR-CP P-F E-P PIPE Si2f 10.00 10.00 16.00 10.00 10.00 NODE NO 26SA ADATR 2FOA 275A 280A C01P IVPE TEF P.PE TRANS EL80WLR EL80WLR 81 / 82 1.00/2.31 .50/1.00 .50/1.00 1.00/3.1m 1.00/3.15 C1 / C2 1.50/3.09 1.10/1.00 1.36/1.48 1.26/4.24 1.26/4.24 El / K2 1.20/1.80 1.20/1.50 1.20/1.80 1.20/1.80 1.20/1.80 illPRE59 11930.12 11930.12 12482.49 11930.12 11930 12 51 10ml 169.86 169.86 0.00 122.30 27.31 SIITHERI 6357.0a 63S7.08 0.00 3020.30 1726.S6 PM . P8 12323.31 6134.91 6241.25 12319.01 12016.96 PM.P8 0.F SFF35.7$ 27i96.24 2040$.23 41991.79 31393.27 0 .F 45412.44 21361.33 14163.98 29672.78 19376.30 RESI ST 33500.00 33$00.00 30000.00 33500.00 33500.00 VIELD ST 18n00.00 18500.00 18u00.00 18800.00 18800.00 M00. ELA. 25666000.00 25666000.00 2$666000.00 25666000.00 25666000.00
_ . . . _ - - _ - _ . . _ = _ _ - - - - - _ . . - - - . . - - - _ _ _ = .
SAI.PRI .6SSS .3263 .3320 .6553 .6392 5d t .5f C 1.123/ .Fe23 .6297 9006 .FS40
%dl falAL 1.le01 1 1016 9617 1.SS60 1.3932
O [7 u RJ O O O ' C E]
.___.) L.JmC r I I '6_ J LJ C b ' '
.ooe ee e e e.e e..e .e e e e e e e.e e e.e e e e...e e e..e e e e..e.e..e e.e e e.e e e.e.e e.ee e e e..e e e e e..e e e e..e ee e e ee ee e e.e e e e e e e.ee.o.ee e ee e.e e ee ee eee e e 5 CUR t o e %uTECH -- vt451CN 1.0.0 -- PAGE 39 e e duaha AtNOLD utCIRCULATIGA PIPINCeLOOP A E a 09/01/50
- eeeee ee e e e ee e e e e ee e eeeee e ee e eeee e ee ee ee e ee ee e eee ee *+ eee e ee eee ee e e** s e e eeeee eeee ee ee eeee oo ss eeeeeoo oo see eeeeeeeeeeeeeeeeooos eeeeee o STRfi$ duLE INDEX LVALUATION -
SUMMARY
e eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee 15I BCB-J3 NCu-J4 kCB-JS RC8-J6 8.?-J7 dELD ID di RS-N-81-A R$-h-81-8 62 45-N-62-A mELO TYPE SE_P P-E E-P P-T T-P v PIPE SIZE 22.G0 22.00 22.00 22.00 22.00 h00E NO 106 158 208 238 238 COMP TYPE TRANS EL80dLA EL80mLA TEE TEE
...___. .______.._________________= - - - - ___ ________ ____ _
81 / R2 .50/4.00 1.00/3.52 1.00/3.S2 1.00/2.59 1.00/2.59 C1 / C2 1.3F/1.50 1.23/4.70 1.23/4.70 1.50/3.45 1.SO/3.45 K1 / d2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 SitPRES) 12388.70 12388.70 12388.70 12388.70 12388.70 SI 10d8 628.10 390.10 59.94 0.00 377.71 SItinEkl 843.00 866.06 600.35 400.09 $77.96 PM e PB 6622.45 13762.48 12S99.78 12388.70 13366.67 PM*PA+0eF 24378.17 28975.73 24615.61 24785.84 28238.21 0 *F 1 FS SS. 72 15213.25 12015.83 12397.14 19871.54 RE5I ST 29000.00 28000.00 28000.00 28000.00 28000.00 YlfLD ST 18800.00 18800.00 ton 00.C0 18800.00 18800.00 900. ELA. 2S666000.00 25666000.00 25666000.00 25666000.00 2S666000.00
_________. __________.. = = - _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
SklePRI .3629 .7320 .h702 .6590 .7110 54Ie5EC .h*90 .6162 .3F06 .S?60 .6113 SMI TOTAL 1.012) 1.5432 1.2405 1.2 3SO 1.3223
l O P L- l C .] O M O O O O O O CJ i] LJ
! L. J l
O[]
....ee..ooe......e.........e.........e.o..e..e..e.e...e.o............e...o...e.....................e.............................
%N - -
. 5Coae .
. NulfCn -- vtR510h 1.0.6 -- PAGE 40 e
. Duant ARh0LD NECIRCULATI0t. PIPING. LOOP A sd 04/01/60 e e...eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeooeeeeeooeeeeeeeooooooooeeeeeeeeeeeeoosee****eoecooocesse.eoeo.co.e.cooessee..eees.ee
. STdf55 RULE INDEX EVALUATION -
SUMMARY
e
..eeeeeeeeeeeeeeeeeeeeeeeeeeooe.eeeeeeeeeeeeeeeeoeoooooooe.eeeeeeeeeeeeeeeee. coco.ooooooose.oooseeeeo.. sos.ooooooeseee.eee..eooe, l
l rcd-J9 RCo-J1S hCs-J16 RC8-J18 RCB-J21 158 wtLD 10 RS-h-82-Al RS-N-S2-E b3 84 RS-N-83-A WELO TVPE P-P P-E E-V V-P SPC PIPE 512E 22.00 22.00 22.00 22.00 22.00 N00E NO NB2A1 35b 408 S$8 608 COMP TYPE PIPE EL80dLR EL80nLu TPANS GRANRON
.---.-----=-- --- -- - - - - - - __ ------ - ---_ _ _.
81 / 82 .50/1.00 1.00/3.52 1.00/3.52 .50/1.00 1.00/1.00 C1 / C2 1.10/1.00 1.23/4.70 1.23/4.70 1.37/1.50 2.00/1.00 K1 / K2 1.20/1.50 1.20/1.00 1.20/1.80 1.20/1.80 1.20/1.80 SitPRES) 123bo.70 12388.70 12388.70 12388.70 12388.70 SI IDWI 110.77 352.63 465.27 211.92 103.13 SitTHERI in6.75 610.02 506.64 379.e4 345.30 PM e PB 6305.13 13630.52 14027.21 6406 27 12491.83 PnePeeQeF 17248.63 26495.02 26S73.34 22007.99 30540.06 0 e F 10943.51 12864.50 12546.12 15601.72 18048.23 kE5I ST 28000.00 28000.00 28000.00 28000.00 28000.00 YIELD ST 15500.00 18800.00 18800.00 18800.00 18800.00 M00. ELA. 25666000.00 25666000.00 25666000.00 25666000.00 25666000.00 SRI.PRI .3354 .7250 .7461 .3408 .6645 SRie5EC .S$53 .5827 .$181 .6217 .6S66
- ----- =_ _ .....-- .....--==_===-_ _= ------ -----------------_---
Sdl TufAL .o907 1.3077 1.3243 .9625 1.3211
o 1 vJa i i L__.J O L _J L] O C-] L_.J L _J LJ O ER O -
F_Q [7 U U -
e.ee e e e e.e o..e.. . ..e e.o o e e...e e e e e o..e e....e e e e e eo o o e e e.ooo o e e e e e e e o o o o o o e.o o e.e.o e e e e e e e e e e.o e o o e.o.o o o o o.e oo eee ee e eo ooooo oe e.
e 5 C0R e o e huitCH -- WER$10N 1.0.0 -- PAGE 41 e e DUANL ANNOLO RFCIRCULATION PIPING. LOOP A E h 04/01/a0 e eeeeeeeeeeeeseeeeeeeeeeeeeeeeeeeee**eeeeeeeeeeeeeeeeeeeeeeeeeeoooeseeeooooooooooooseeeeeoooooooooooseeooooooooooooosseeeeeeeeeeee e SIRE 55 RULE IN0Ea EVALUATION - SUMMARV e sooo s e e, e e e e ee e e e e e e ee e e e e e e e e e e e e ee ee e e e e e e e e e e eo e e s e. o o e e ee e e e e e eee e eo oo oo oo s s ee oo oe e e ee oo o e se eo os eeee ee eeee ee eeee ss ee eeee eee s, 151 RC8-J24 MC8-J2$ SCd-J27 RC8-J30 RC8-J31 WELD ID RS-N-83-D d$ 66 RD-N-B1-A 87 MELD TYPE P-E E-PP FP-P SPC P-V PIPE SI2E 22.00 22.00 22.00 6.00 22.00 NODE NO 6S8 108 908 9$8 1008 COMP IVPE ELR0=5k EL80mSR TRAN5 TEE TRAN5
_____.______..._________..__.. ------ _ _ _ . . . _ _ _ . . ~ . . . . . . _ _ . _ _ _ _ _ . . . . . _ _ _ _ .
81 / 82 1.00/4.62 1.00/4.62 .50/1.00 1.00/2.35 .50/1.00 C1 / C2 1 46/6.1$ 1.46/6.1% 1.36/1.48 1.50/3.13 1.36/1.48 K1 / K2 1 20/1.80 1 20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 SitPRESI 1238u.70 123ss.70 12 F4 8.55 3987.40 12748.SS SI (Owl 44S.10 975.82 2$3.73 199.77 48.20 SilIHERI 277.13 33S.77 226.75 2873.99 231.29 PM e Ps 14442.93 16892.31 6628.00 44$6.73 6422.48 PMePeeQeF 29713.34 36241.40 22144.58 24508.27 21607.42 Q e F 15270.41 19349.09 15 $ 16. S u 20051.S4 15184.95 RESI ST 2d000.00 2s000.00 28000.00 39000.00 28000.00 VIELD ST 18d00.00 18100.00 18800.00 18800.00 18800.00 MOD. ELA. 2S666000.00 25666000.00 2S666000.00 2$666000.00 2S666000.00 SRI.PRI .7652 .6905 .3S26 .2371 .3416 sul.5f C .6110 .6731 .620$ .e420 .6158
.__....___.-_...______ _......_..._..______.... ..._______.__..~..... .__.__. .
Sdl TOIAL 1 3822 1.413F .9730 1.0191 .9574
w w m n L__J C] O L._J L__J C-] {C C L._J C L_J C- Q C .J U U
....o.....e.....eees.......................e..........e..o.+........e.........e...........................>......................
"iCO -
. 5 Coae e
. NuTECH -- Vfd5 ION 1.0.0 -- PAGE 42 e
. Du4NL AnNOLO REClkCULAiluh PIPING. LOOP A E o 04/01/80 e
. .ooeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee****eseeeeee***+eoeeeeeeeeeeeee**eeee*****eeeeeeeeeeeeeoeseeeeeeeeeeeeeeeeeeoeoseeeeeeoesee
. %iAE55 NULE thDfX EVALU4Il0N - $UMMARY .
....eeeeeeeeeeeeeeeeeeeee.coceeoooeseeeeeeeeeeeooooooooooooooeeeeeeeeeooooooooooseeoeoooooooooosecoceeoo..oooooe.ceeoeoeooooosees i
151 RCB-J33 RCb-J35 RCB-J37 R88-J1 R88-J2 I wtL3 10 us RD-N-d2-A RD-N-82-8 818 R0-N-88-A niLG TYPE V-1 E-P BPC WOL-P P-E PIPE Silt 22.00 22.00 6.00 4.00 4.00 NUDE NO 115d 1208 125b 818 1308 COMP IYPE ELB0mLW EL80dLR TEE PIPE EL80WLR 81 / 82 1.00/3.la 1.00/3.18 1.00/2.35 .50/1.00 1.00/2.43 C1 / C2 1.23/4.24 1.23/4.24 1.50/3.13 1.10/1.00 1.27/3.24 41 / K2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 5tIPRF53 12748.55 12748.55 3987.40 8031.90 8031.90
$1 IDwl 223.04 172.81 1124.39 657.56 73.86 SIITHERI 246.12 175.00 2993.11 9449.36 3011.41 PM e P8 13458.21 13298.39 6628.94 4673.50 8211.47 PM*PB+0eF 22440.95 21514.32 30396.60 28812.56 30201.72
- Q *F 8982.74 8215.93 23757.66 24139.05 21990.24 .
Rf51 ST 24000.00 28000.00 39000.00 45000.00 45000.00 YlfLO ST lue00.00 15600.00 16800.00 18800.00 18800.00 MUD. ILA. 25666000.00 25666000.00 25666000.00 25666000.00 25666000.00 Sal,PRI .7159 .7074 .3526 .2486 .4368 5dl 5EC .5273 .5164 .8950 .9d58 .9552
%=I idIAL 1.2412 1.2238 1.2476 1.2344 1.3920
[_ .J '~l [ C C C C C imd L_ } O I~ I C C C bk C C J U U -
eeee.e.* * *...e e..e.e e..e e e.e *
- ee *
- e e e.e e o o oe. e e e e ee e e * * *
- e o co co e s e e e.c o c o c o e..ee.o oe *
- e s e se oo o oe oe o c oes e *
- e oo e s e.ee e e s co o** *.o ese e 5C0R i o e NuffCn -- vfRSION 1.0.0 -- PAGE 43
- e cuaNt AdNULO RECIRCULATION PIPING. LOOP A E u 04/01/40 e ese***eeeeeeeeeee**********e**eeee******e+++eeee*************eoeoe******eoeoootse***eseo****oose***eseceo*****eooooooooecesoseoso e STRESS RutE INDEM EVALUATION - SunMARY e seeoeoeeeeeeeeeeeeeeeeeeeeeeeeeoooesseeoooooooooooooooooooooooooooeeeeeeeeoooeseeeeeeeeeooseeeeeeeeeeeeeeeeeeeeeeeeeeeeeoeooseeee ISI R88-J3 Hu8-J6 rub-Ju R88-J7 R88-J9 MELD ID RD-N-d%-8 819 820 AD-N-89-A RD-N-810-A mELO TYPE E-P P-T T-P T-FL P-E PIPt Silf 4.00 4.00 4.00 4.00 4.00 .
NODE NO 1358 1908 1908 1458 1508 COMP TYPE ELeonLR TEE TEE TEE EL80WLR 81 / 82 1.00/2.43 1.00/1.69 1.00/1.69 1.00/1.69 1.00/2.43 C1 / C2 1.27/3.24 1.50/2.26 1.$0/2.26 1.50/2.24 1 27/3 24 K1 / K2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 SItPdESS 8031'.90 8031.90 8031.90 8031 90 8031.f4 51 (DW) 17 3.6N 477.39 1962.36 1029.63 746.35 SitINERI 4147.79 11066.86 10910.63 0.00 5674.30 i PM e P8 84$4.18 8839.95 10676.40 9774.68 9846.56 ,
PnePBeQeF 37415.41 61353.99 6$126.83 18640.10 49664.76 l 0 *F 28961.22 52514.04 54450.43 8865.41 39818.20 l
RESI SI 45000.00 45000.00 4$000.00 45000.00 45000.00 YIELD ST 18a00.00 lus00.00 18800.00 18800.00 18800.00 MOD. ELA. 25666000.00 2S666000.00 25666000.00 25666000.00 25666000.00 SRI.PNI .4497 .4702 .5679 .5199 .5238 SRI 5EC 1.0546 1.3904 1.4180 .7681 1.2094 5dl TOTAL 1.SO43 1.o606 1.9eS9 1.2880 1.7332
O O M ('~ 2 [7 F7 C r 1 ! j f I i.,_,,_j O Q Q Q L_J L, ,j O[7 O
..............................................e..e...e.....e.....ee...............e......e.......................................
%1 - -
. 5C0# E o
. NuffCH -- vtNSION 1.0.0 -- PAGE 44 *
. uuaNE AdNOLD NfClwCutATION PIPING. LOOP A E 5 04/01/80 e eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee***eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee
. STRESS RutE INDEX EVALUATION . SUMMANY 9
.eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeooooopoeeeeeeooeeeeeeeeoeseeeeeeeeeeeeeeeeooooseeeeeeeeo,eeeee 151 uss-J10 238-J12 RC8-J41 AC8-J44 RC8-J46 wtLO 10 821 822 RD-N-82-E R D'N-8 2-C 89 mfLD TYPE E-v W-w0t P-P P-T T-CR PIPE SilE 4.00 4.00 22.00 22.00 22.00 NODE NO 152s 1676 1738 175b 1808 COMP TYPE eld 0mLN TRANS PIPE TEE TEE ,
_ . . - - - ---.__= ----
81 / B2 1.00/2.43 .50/1.00 .50/1.00 1.00/2.35 1.00/2.35 C1 / C2 1.2F/3.24 1.34/1.45 1.10/1.00 1.50/3.13 1.50/3.13 K1 / K2 1.20/1.d0 1 20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 SIEPRES) 8031.90 a031.90 12 7 4 8.SS 12748.55 12748.55 51 (Owl 413.40 1052.74 57.24 431.51 381.12 u:THERS 3 793.9 F 3769.66 492.65 1649.T2 517.30 PM e Pd 9037.03 $668.69 6431.52 13762.30 13643.93-PM PueQeF 16749.58 27101 63 17d17 40 34682.07 28013.04 0 e F 21712.$$ 21432.94 11J86.38 20919.77 14369.11 .
ME5I ST $5000.00 4S000.00 2d000.00 28000.00 28000.00 Y1ELO ST 1se00.00 18800.00 toe 00.00 18800.00 18800.00 900. ELA. 2$666000.00 2$666000.00 25666000.00 25666000.00 2S666000.00 l ...__.._........ ..._ _.==_=_ - - - - - - - . . . . . _ - - _ . - - - - - . . _ _ _ . _ - - - - - -
i Sul PWI 4607 .301S .3421 .7320 .7257
%dl.5EC 1.G364 9413 .5616 .6975 .6041 l
%wl TOTAL 1.5115 1.24se .9037 1.4296 1.3299 l
C L.J 47 n L_J i 2 LJ LG 1 J LW Q L; n CD CD LJ CC L_J b U ' '
oose..............................e.e.... ........+..e.e.e..e.ee......o.e.eee.e.ooe.eee.eee.e.o.ooe.ooe.oese......oo...e...oese.e
. 5c0,e e o huiFCes -- vEkS10h 1.0.0 --
PAGE 45 e e 00 a ht AFN9LO RECidCutATION PIPING. LOOP A L a 04/01/50 e esee.ee..eeeeeeeeeeeee...eeeeeeeeeeee.***eoeo.**eeeeeeeeeeeeeeeeeooooooooooooooseeeeooooooooooeseeeeeeeeeeeeeoeesesseeeeeeeeeeeee o Sivt%5 kuLE th0EM EVALUATION -
SUMMARY
e ooseeeeee.eeeeeeeeee.eeeeeeeeeeeoeooeeeeee**ee.oeoeooeeeeeeeeeeeeeeeeeeooseee*****eseooeeeeeeeoooseeeeeeeeooooseeeeeeeeoooooseese 158 dMe-JF RMB-J6 RM8-JS RRC-JF ARC-JS MELD 10 AD-4-83-6 RD-h-d3-D M D-h- 8 3-C 812 RD-N-86-8 alLD TYP1 CR-CP HOR-Ca HOR-A A-P P-E PIPE Silt 22.00 16.00 10.00 10.00 10.00 ,
h00E NO teSe 18F8 1908 ADAIR 1958 COMP TYPf TI L TEE TEE PIPE EL80WLR 81 / B2 1.00/2.59 1.00/2.59 1.00/2.31 .50/1.00 1.00/3.18 C1/ C2 I.$0/3.4% 1.50/3.4% 1.SO/3.09 1.10/1.00 1.26/4.24 K1 / K2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1 20/1 80 SitPAE55 12F48.S$ 12482.49 11930.12 11930.12 119ad.12 SI IDel 0.00 292.96 886.40 886.40 613.22 SItinEkl 0.00 1775.68 anFS.73 9479.33 3591.54 PM
- PB 12F48.SS 1J241.01 13982.00 68$1.45 13880.13 .
PM.PH.Q.F 2294F.40 3S323.04 7SF09.42 34406.06 50098.12 O e F 10198.84 22082.03 61727.41 27554.61 36217.98 RESI ST 2a000.00 30000.00 33500.00 33500.00 33500.00 YIELD ST 1u600.00 18800.00 18600.00 18800.00 18800.00 900. ELA. 2$066000.00 2S666000.00 25666000.00 2S666000.00 2S666000.00 5dl.P48 .6Fdt .F043 .F437 .3644 .F383
%dt.5iC .S4*F .F426 1.3SF8 .6706 .9941 541 f1Tal 1.2224 1 4469 2.1016 1.2350 1.7324
E3 ( L m CD E' L-.J CC (_ J C~3 C"] M C~] C~3 C] C~] CJ.
O.J U %L. J eeeee ee e e e ee e e e e ee e ee ee ee ee e..ee e e ee ee ee ee e e*
- ee eee e e ee e ee* **ece ***ee e eeee,* e se eeee.ee e e eee e***ece eeeee ee ee eeeeeeeeeeeeeeeeeeee ee e 5C0R 1 e o NulfCn -- vfk% ION 1.0.0 --
PAGE 46
- e DuAhl 4 d P40L O REclacutATION PIPINGeLOOP A L 8 04/01/80 4 eseeeeeeeeeeeeeeeeee++ee****eoo***ee*********eooo******eeeeeeeeeeeeeeee****eseee*****e**eeeeeee***eeee****eoeeeeoooooooseeeososee
- $1AE55 kutE th0E4 kWALuaTION -
SUMMARY
e eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeseeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee 151 RNC-J4 RM8-J2 NdO-JF RMB-JL R40-JS mELO ID dD-N-ob-C R D-h-d 3-u 813 RD-N-ul-A RD-N-87-8 dELD TYPE E-P HDR-A A-P CP-HOR P-E P1P1 5IJE 10.00 10.00 10.00 16.00 10.00 ,
N00E NO 2006 2158 A0 Aid 220b 2258 CO9P TYPE ELdumLk TEE P!PE TRANS EL80MLR
.--------.....----...........-- -. =. ._. -- .. - - _ . . _ _ . .
dl / 32 1.00/3.18 1.00/2.31 50/1.00 .50/1.00 1.00/3.18 C1 / C2 1.26/4.24 1.$0/3.09 1.10/1.00 1.36/1.48 1.26/4.24 El / K2 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 5IIPMESI 11930.12 11930 12 11930.12 12482.49 11930.12 58 40ml 296.90 338.07 338.07 0.00 232.12 SIITHER) 1247.S1 6603.35 6bO3.3S 0.00 2974.12 PM
- PB 12s74.25 12712.71 6303.13 6241.25 12668.26 .
PheP8eQeF 29794.74 60038.48 25242.31 20405.23 42477.59 0 e F 16920.49 47325.77 21939.18 14163.98 29809.33 RESI ST 33S00.00 33500.00 33500.00 30000.00 33500.00 YIELO ST 18800.00 18800.00 18a00.00 18d00.00 18800.00 M00. ELA. 2S666000.00 2S666000.00 2S666000.00 25666000.00 25666000.00 SRIePRI .6848 .6762 .3353 .3320 .6738 -
5dle5EC .7149 1.1$25 .790$ .6297 .9027
- . . - - - - - - - - - - - - - .....-- .._.------....__ ==..---_ _ - ..-- ..-_ ... .
SRI IOTAL 1.4017 1.d287 1.12$8 .9617 1.5766
C ( b C I C L- J C M C C C C C C C U %-
-Os
.......... ..................e....................o..e.. ..e.ceo.e....o............oo.....o..oo..oe.ooe.....oo..o....o...o..oo..e e 5C09 E o o NuffCn -- WEW510N 1.0.0 -- PAGE 47
- e dd A fel ANNOLD RECIRCULATION PIPING LOOP A & 8 04/01/80
- eoeoee.eee..eeeeeee.oooooooooooooooooe.+ooee**eoeooooooooooooooooseeooooeeeeeeeeeeeooooooooooeeeeeeeooooooooooooooeeeeeeeeeeeeeee e SINE 55 RULE INDEX EVALUAil0N -
SUMMARY
e ese.eeeee.eoo.eeeeeeeeeeeeeeeeeeeeeeoose*******oooooooseeeeooooooooooooseeeeeeeseeeeeeeeooooooooooteeeeeeeeeeeeeeeeeeeosecoeooeee 1%I HND-J4 WMS-Ja RMe-J9 RRB-JF RR8-JS MELD ID RD-%-8F-C R0-N-8 3-F RD-N-83-G 811 RD-N-85-8 mELO IVPE E-P CR-HOR HDR-A A-P P-E PIPE SilE 10.00 16.00 10.00 10.00 10.00 ,
NODE NO 230n 2378 2408 ADATR 24Sb COMP TYPF ELoddLR TEF TEE PIPE EL86dLR l
i 81 / d2 1.00/3.la 1.00/2.3S 1.00/2.31 .50/1.00 1.00/3.18 l C1 / C2 1.26/4.24 1.50/3.13 1.$0/3.09 1.10/1.00 1.26/4.24 W1 / K2 1.20/1.80 1.20/1.80 1.20/1.50 1.20/1.80 1.20/1.80 SilPaE 5 5 11930.12 12482.49 11930.12 11930.12 11930.12 51 IDwl al.S1 $2.a4 d27.30 827.28 659.58 SIlinERI 2013.67 1314.65 10130.23 10130.23 3617.92 PM e P8 12192.50 12606.63 1384S.21 6792.34 14027.54 -
PM*P8eQ+F 34005.74 30178.88 82350.72 35471.28 S0653.21 Oe F 21813.24 1FST2.25 68505.S1 28678.94 36625.67 NE55 ST 33500.00 30000.00 33$00.00 33500.00 33500.00 YIELD ST 18800.00 18800.00 18603.00 18800.00 18800.00 900. ELA. 2$666000.00 25666000.00 25666000.00 25666000.00 25666000.00
.......................--.......... --..== ...--..- . .... . ..... ..
Sul,PNI .64sS .6706 .F364 .3t13 .7461 S R I . 51 C .7047 .6le) 1.4545 .an66 .9999
. .... ........--- ...........--- ----.......-... =........--... . . ..
1
%WI idIAL 3 4172 1.3449 2.1909 1.2479 1.7461
m L_ J Ca n CJ M L_ J Q n CO n O Q Q Q C1 CG CD fx J
/
L)3
..o..ooeeeeeeeooee.o.....ee....o.e....e.........ee...............o..o.................e...............o.................... 0e o.
. 5C0ae .
e Nu TFCn -- vf45tDN 1.0.0 -- PAGE 48 e
. JU ant AWNOLO RECIdCULATION PIPING. LOOP A E h 04/01/80 .
..eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeoseeeeeeeeeo**eseeeeeeeeoeoooooseeeeeeeeeeeeeeoooteoeeeeeesoooooeseceoooooooooooooeceseeeeeeeeeee
. STRES5 RULE INDEX EVALUATION -
SUMMARY
....ee e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e e * ** e o e o o o oo o o o o s e e e o o o o o e c e s e e e e o oo o o o s e e e e o e s ee c o c o o eo os ee e ee oo o c e o o ss e e e a c e 6 a e o s e e e 158 aWB-J4 RMB-J11 RRA-JF RM8-J12 RSA-JS wfLD 30 ND-N-85-C RD-Nad3-H BLO RD-N-83-J A0-N-84-8 efLO TYPt E-P HDN-A A-P HDR-CP P-E PIPE SI2E 10.00 10.00 10.00 16.00 10.00 ,
NODE NO 2$03 26S8 ADATR 2708 2758 COMP TYPE Etuu=LW TEE PIPL TRANS EL80WLR *
..-_--_....--...._---.....--.- _= ...==_ =_...--..--.----.... _ _ ._-_ _ _ _
bl / 82 1.00/3.1a 1.00/2.31 .$0/1.00 .50/1.00 1.00/3.18 C1 / C2 1.26/4.24 1 50/3.09 1.10/1.00 1.36/1.48 1.26/4.24 K1 / K2 1.20/1.d0 1.20/1.80 1.20/1.80 1.20/1.80 1 20/1.80 SIIPRE55 11930.12 11930.12 11930.12 12462.49 11930.12 SI IDWI 474.77 41.8F 61.87 0.00 163.19 StiTHE45 260$.3% 8729.46 5729.46 0.00 3099.86 PM e Pa 13439.87 12073.34 6026.93 6241.25 12449.07 .
PM*P8eQeF 41S15.03 70315.97 31572.15 20405.23 42911.14 0e F 2807$.17 58242.63 2$$45.22 19163.98 30462.07 RESI ST 33S00.00 33$00.00 33500.00 30000.00 33500.00 YIELD ST 18a00.00 18800.00 18500.00 18800.00 18800.00 M00. ELA. 25666000.00 2S666000.00 25666000.00 256660J0.00 25666000.00
. . . . - - - . . . . . . . - - - _ ==...... ...._ _--..---. . _ . - - - _ _ - _ - _
SRI.PRI .7149 .6422 .3206 .3320 .6622 SRie5EC .6760 1.10d1 .5419 .6297 .9120
.....= .....-- ===..... .--.. ===.._ _... . ..--..._ _ _. _ _ _ _.---
SRI TOTAL 1.5929 1.9503 1.1625 9611 1.5742
bd w U * #
U '
)
i
\% 't
%./
i e**eese+....e.eeeeeeeee****.*e**** ***o*******************o*e**********eeeoooooooese***eeeeee**eceeeeeeooe**e0000000e990000000000 e 5 C0 h t *
- Nes t ' c., -- v e d 51% 1.0.u -- PAGE 49 *
- + PJ A N s 4 4 7.0 L G k r C i d C u L a l l W. PlethGeLOOP A L M 04/01/d0 *
- e.eeeeeeeeeeeeeeeee*eseeooe*o****************************************************e****************************************
e '-
Sidf55 kutt INut s EvaLuall0N . SUMMAkV 9 eee*e.oe eee++eeeeeeeeeeeeeeee++++++++++**********o****e******* *****************************************************************
lit kdA-J*
mtLD ID d 6'-N-5 4-C attb TYPI &-P flPE Sitt 10.00
- 1 N0pi NO 240n C09P TYPt E L . sod L k .
81 / 62 1.0G/3.16 C1 / C2 1.26/4.24 W1 / d2 1.20/1.10 SitPRt%) 1L930.12 SI 10dl 198.Fd
$ l l i tit u l 3212.64 PM . PB 12S62.23 Paersedef 4633).02 oe F 31F?o.do util SI 3)S00.00 TitLD ST 11100.00 103. ELA. 2S66h000.00 5dlePdt .6642 Shl,StC 9% 82 Sul idiaL 1.6/F4
LM C C U C C LJ C n C- O W C C Q O Ll L. _.)
oeooseeeeoseeeeeeeeeeeooosoeeeeeooeveeeeeeeoeooseeeeoesoseesseeeeoseeeeeeeeeoooooeseeosoeeoseeeeooooooooeteooseeeeeeeeeooseeeeeee e 5C0R E *
- MUTECH -- VERSION 1.0.0 -- PAGE 10 *
- DUANE ARNOLD RE CIRCUL AT ION INLET E OUTLET N022LE 04/01/80 *
, eseeeeeeeooooeseeoeoooooooooooseeeeeeeeeooooeseosoceeeeescoceeeeeeeeeeeeeeeeeeeeeeeeee***ooeeeeetooeceoo**eescotocooseeoeoseeoo**
- STRESS RULE INDEX EVALUATION -
SUMMARY
e eeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee ISI RAA/H-J4A RRA/H-J3 RRA/H-F2A RRA/H-F2A RRA/H-F2 WELD ID WELD TYPE P-P P-SEX P-SE P-5E SE-N2 PIPE SIZE 10.00 10.00 10.00 10.00 12.00 NODE NO WELDS WELO6 WELD 4 WELO4 WELD 2 COMP TYPE PIPE PIPE TRANS TRAN5 TRANS l 81 / 82 .50/1.00 .50/1.00 .50/1.00 .50/1.00 . 50/1.0C C1 / C2 1 10/1.00 1.10/1.00 1.36/1.48 , 1.3511.46 1.34/1.45 W1 / K2 1.20/1.80 1.20/1 80 1.20/1.80 1.20,d.80 1.20/1.80 SIEPRES) 9916.97 9916.97 9916.97 7757.14 6833.33 .
SI EDW3 673.30 3014.93 3251.25 2574.37 5185 24 SIITHERS 3283.88 7026.02 7442.46 5893.48 3431.22 PM e PB 5631.79 7973.41 8209.74 64S2.94 8601.91 PMeP8+0+F 20213.34 31164 11 44653.84 34819.26 33557.56 0 e F 14581.S5 23190.69 36444.10 28366.32 24955.65 RESI ST 33500.00 33500.00 33500.00 40000.00 38000.00 YIELD ST 18800.00 18800.00 18800.00 28130.00 28130.00 M00. ELA. 25778000.00 25778000.00 25778000.00 29416000.00 29416000.00 SRI +PRI .2996 .4241 .4367 .2294 .30S8 SRI +5EC .6834 .8058 .9941 .7862 .7239 SRI total .9830 1.2299 1.4308 1.0156 1.0297
La C C L- ) (d '
W C C ) C C C C C C l- .I e 5C0R E *
- NUTECH -- VERSION 1.0.0 --
PAGE 11 .
e suahE ARh0LD AECIRCULATION INLET E OUTLET N0ZlLE 04/01/80 e eoosese ee eee eee eoso ooooo ooseeo ooe ceoe sse ee e e * ** * * **
- eoo o o oo oooo s e e e ee e *** *e o oo o oo*** *.c o coo s eo* *** e seeeesooocoot ecoceeeee eeeooooo e STRE55 RULE INDEX EVALUATION -
SUMMARY
e ococeee e e e e e e ee e e e e e e o o o e.c o c oo 6e o e o o.o o o o o s e.e* *
- e o o o o o e s e.o.c o o o o oo o oo o o oo o o s e eo o e e e e e e e e e e e e.** e e 0000 00 e 00 00 0 o 00 00 e.00 0o 0 000 eo 151 RCA-F2 RC8-F2 WELD ID WELD TYPE SE-NZ SE-NZ PIPE SIZE 12.00 12.00 NODE NO NLA N1B COMP TYPE TRAN5 TRANS 81 / 82 .50/1.00 .50/1.00 C1 / C2 1.34/1.45 1.34/1.45 K1 / K2 1.20/1 80 1.20/1.80 SIIPRESI 6833.33 6833.33 -
SI IDWI 2085.38 1832.14 SIITHERI 2996.39 2292.12 PM e PR 5502.05 5248.81 PM*P8eQeF 24302.30 21795.16 0 *F 18800.25 16546.35 RESI ST 32000.00 32000.00 YIELD ST 18800.00 18800.00 MOD. ELA. 25778000.00 25778000.00 SRI PRI .2927 .2792 SRI,5EC .7220 .6900 5RI TOTAL 1 0147 .9692
CJ Q C3 L_.) CD E7 CR L.J CD L CJ L) C~] Q CJ Q CD h.> C2)CD (v
.oo..o.o.o.e.ooooo..ooooo.ee.ooe.e.e.o..oooooo..e..oose..ooooooo....oese.o.oooe..ooooe.o.o.co.ee.o.co..ooe..oote,ee....oooe.co.e.
0 $C0Re .
o NUTECH -- VERSION 1.0.0 -- PAGE 1 e 0 OUANE ARNOLD RESIOUAL HEAT REMOWAL PIPING 04/01/80 e ooe.coceoeeeeeeeeeeooooooosseeeeeeooeeeeeeeooseseoeoeooooseeeeeeeeeeoeooooooooooooooooooooooooooeeeeeeeeeeeeeooooooooooooooeeeeee o STRES5 RULE INDEN EVALUATION -
SUMMARY
eseeeeeoooseeooeseeoeoeoeooseeeeeoooeeewesooooo******ooooooooosseeeeee**eoo*****eseeee****eecooeoeooecoceeoeooooeceeeeeeeeeoeoooo ISI RHC-J1 RHC-F2 RH8-JL RHS-J2 RMS-F)
WELD ID WELD TYPE T-P P-P T-P SPIP-WOLI P-P PIPE SIZE 20.00 20.00 18.00 18.00 18.00 NODE NO 175A 290A 238 4108 4158 COMP TYPE TEE PIPE TEE SRANRUN PIPE 81 / 82 1.00/2.59 .50/1.00 1.00/2.59 1.00/1.00 .50/1.00 C1 / C2 1 50/3.45 1.10/1.00 1.50/3.45 2.00/1.00 1.10/1.00 K1 / K2 1.20/1.40 1.20/1.80 1.20/1.80 1.20/1.80 1.20/1.80 511 PRE 55 9699.32 9699.32 9605.12 9605.12 9605.12 51 10WI 854.61 546.02 431.29 230.50 441.72 SIITHERI 1004.44 1054.68 769.18 517.63 461.25 PM
- P8 11912.05 5395.68 10721.40 9835.62 5244.28 PM+P800eF 29010.94 15702.35 24F48.92 24398.92 14304.11 0*F 17098.89 10306.67 14027.13 14563 30 9059.83 RESI ST 28500.00 28500.00 29000.00 29000.00 29000.00 Y! ELD ST 18800.00 18800.00 18800.00 18400.00 18800.00 MOD. ELA. 25946000.00 25946000.00 25946000.00 25946000.00 25946000.00 SRI.PRI .6336 .2870 .5703 .5232 .2790 SRI.5EC .6450 .5493 .6087 .6162 .5384 SRI TOTAL 1.27dl .8360 1 1790 1.1394 .8173 j
C C C U C C L-- J C) U k) C L) C C C C C O
oe.eet.co.e.e.oe..eeeeeee...e.eeeeeeooseeeee.co..e.oeooe.o.e..eoooeee.eeee.ooeeeeeeeeee...e...eeeeee...o.eoeeee.eeeeeeeee.eoooooe e 5C0R E *
- NUTECH -- VERSION 1.0.0 -- PAGE 10
- e DUAhf ARNOLD RE5 tDUAL HE A T REMDV AL PIPING 04/01/40
- oeeeeeeeeeeeeeoseeeeeeeeeeeeeeeeeoeooooessesseeeeeeeeeeeeeeeeeeeeeeeeeeeeoooooooooseeeeeeeeeeeeeeeeeeeeeeeoooooooseeeeeeeeeeeeeee o STRESS RULE INDEX EVALUATION - SUMM ARY e eseeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeeee ISI RHD-J1 RHD-F2 WELD 10 WELD TYPE T-P P-P PIPE SIlF 20.00 20.03 NODE NO 17$8 2908 COMP TYPE TEE PIPE 81 / 82 1.00/2.59 .50/1.00 C1 / C2 1.50/3.45 1.10/1.00 K1/ K2 1.20/1.80 1.20/1.80 SitPRE53 9699.32 9699.32 51 (DWI 882.68 538.56 SitTHERI 1077.82 1128.25 PM e PS 11984.72 5308 22 PM*P8+0eF 29641.28 15803.35 0*F 17656.57 10415.14 RESI ST 28500.00 28500.00 YlELD ST 18800.00 15800.00 M00. ELA. 25946000.00 2S946000.00
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SRiePRI .6375 .2866 SRie5EC .6529 .S505 SRI TOTAL 1.2904 .8371
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NG-82-2653 4 December 1, 1982 f
A) 17 welds - no indications B) 21 welds - geometry < 50% DAC C) 5 welds - geometry 50% to 75% DAC D) 4 welds - geometry > 75% DAC E) *1 weld - Linear Indication
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,t-1982 - A Total of 21 Welds Were Examined With The Following Results:
"A) 8 Welds - Geometry < 50% DAC B) 3 Welds - Geometry 50% to 75% DAC C)- 9 Welds - Geometry > 75% DAC D) *1 Weld - Linear Indication
- Weld RRC-BJ4 was examined with identical results in 1981 and 1982.
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