ML20116M065
| ML20116M065 | |
| Person / Time | |
|---|---|
| Site: | South Texas  |
| Issue date: | 08/15/1996 |
| From: | HOUSTON LIGHTING & POWER CO. |
| To: | |
| Shared Package | |
| ML20116M062 | List: |
| References | |
| NUDOCS 9608190288 | |
| Download: ML20116M065 (2) | |
Text
.
)
ATTACHMENT 3 MARKUPS OF PROPOSED CHANGES TO TECHNICAL SPECIFICATIONS I
l l
l I
l 9608190288 960815 PDR ADOCK 05000498 P
PDR TSC-96\\5403,w iij
PLANT SYSTEMS SURVEM LANCE REOUIREMENTS (Continued) 3)
Verifying that the system maintains the control room envelope at a positive pressure of greater than or equal to 1/8 inch Water Gauge at less than or equal to a pressurization flow of 2000 cfm relative to adjacent areas during system operation; 4)
Verifying that the makeup filter unit heaters dissipate 4.5
- 0.45 kW when tested in accordance with ANSI N510-1980; and 5)
Vrifying in en : High Tcnic C= :::: :;ign:1, i: ::y::::= cu:cm; !=!!y
- v. itch = in:c
- =irculation med: cf cpration by i=!;;ing ic ncrm;!
supply c.nd exhau; flcve..iiin 5 =ccada.
f.
After each complete or partial replacement of a HEPA filter bank, by verifying that the HEPA filter bank satisfies the in-place penetration and bypass leakage testing acceptance criteria ofless than 0.05% in accordance with ANSI N510-1980 for a DOP test aerosol while operating the system at a flow rate of 6000 cfm i j
10% for the cleanup units and 1000 cfm 10% for the makeup units; and i
1 g.
After each complete or partial replacement of a charcoal adsorber bank, by verifying that the charcoal adsorber bank satisfies the in-place penetration and bypass leakage testing acceptance criteria ofless than 0.10% in accordance with ANSI N510-1980 for a halogenated hydrocarbon refrigerant test gas while operating the system at a flow rate of 6000 cfm i 10% for the cleanup units and 1000 cfm i 10% for the makeup units.
SOUTH TEXAS - UNITS 1 & 2 3/4 7-18 Unit 1 - Amendment No. 7 TSC-966403.w