ML19326C407
| ML19326C407 | |
| Person / Time | |
|---|---|
| Site: | Arkansas Nuclear  |
| Issue date: | 08/30/1976 |
| From: | Ziemann D Office of Nuclear Reactor Regulation |
| To: | Phillips J ARKANSAS POWER & LIGHT CO. |
| References | |
| NUDOCS 8004220956 | |
| Download: ML19326C407 (4) | |
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We are reviewing your June A,1976 submittal which provided the Arkansas i
Nuclear One - Unit M.1 10 CFR Part 50, Appendix I Evaluation. We have determined that the information described in the enclosure, some of
' which was requested in our_ February 19, 1976 letter...is necessary to-l 3 @ f continue our review.. dwe ss #,d.W w i n.. s M & 4 c, w Q g W W,er=
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2-AUG 3 0 B76 Arkansas Power & Light Company cc w/ enclosure:
Horace Jewell, Esquire House. Holms & Jewell 1550 Tower. Building Little' Rock, Arkansas 72201 Mr.' Donald Rueter Manager, Licensing Arkansas Power & Light Company Post Office Box 551 Little Rock, Arkansas 72201 Arkansas Polytechnic College Russellville, Arkansas 72801 O
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ARKANSAS POWER & LIGHT COMPANY ARKANSAS NUCLEAR ONE - UNIT NO.1 DOCKET NO. 50 '13 REQUEST FOR ADDITIONAL INFORMATION. REGARDING.
ANO - UNIT NO. 1 APPENDIX I SUBMITTAL DATED' JUNE'4,'1976
References:
1.
Letter, Mr. J. Phillips to Mr. R. DeYoung, May 17, 1972.
2.
Letter and attached Report regarding AN0-1 Appendix I Evaluation, Mr. W. Cavanaugh III to Director of Nuclear Reactor Regulation, June 4,1976.
3.
Letter, Mr. D. Ziemann to Mr. J. Phillips, February 19,c1976.
'l.
Response to Question 19 of reference 1 indicates that there is no' separate cation demineralizer for lithium and cesium while Table 3 of reference 2 indicates that there is. Explain this discrepancy.
2.
Response.to Question 14 of reference 1 indicates that the condensate demineralizer flow is 7,826,000 lb/hr which is approximately 70% of the steam flow rate indicated in response to Question 13 of reference 1.
Table 3 of reference 2 indicated 100% steam flow becomes condensate 3.
demineralizer flow.
Explain this discrepancy.
3.
Provide a. docketed reference for the values listed in Table 3 of refarence.3 for. equipment' drain and clean waste flow rates.
4.
Table 3 of reference 2 indicates that there will be 4 purges per year during power operation.
Indicate whether this purge frequency is based on operating experience or engineering judgement.
5.
For each of the plant release points, provide the following:
1.
Height above grade.
2.
Height above adjacent structures.
3.
Expected average temperature difference between gaseous effluents and ambient air, i
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Effluent flow rate.
5.
Effluent exit velocity.
6.
Vent size and shape.
7.
The use of deflectors or diffusers or the vent.
6.
You based your model on the general straight-line airflow model described in Regulatory Guide 1.111; however, you did not specifically describe the version which you used.
Describe your model including all equations used.
Discuss its validity and accuracy as related to this site and region.
7.
Our review of information supplied in reference 2 indicates that ce.tain information requested in reference 3 was not supplied. Specifically, we require the information requested in Questions 2, 3, 5, 7, 8 and 9 of 'to~ reference 3.
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