ML18053A370: Difference between revisions

From kanterella
Jump to navigation Jump to search
(Created page by program invented by StriderTol)
 
(Created page by program invented by StriderTol)
 
(4 intermediate revisions by the same user not shown)
Line 3: Line 3:
| issue date = 05/09/1988
| issue date = 05/09/1988
| title = Provides Confirmation That Required Procedures Re Generic Ltr 88-03 Concerning Generic Issue 93, Steam Binding of Auxiliary Feedwater Pumps, in Place & Will Be Maintained
| title = Provides Confirmation That Required Procedures Re Generic Ltr 88-03 Concerning Generic Issue 93, Steam Binding of Auxiliary Feedwater Pumps, in Place & Will Be Maintained
| author name = KUEMIN J L
| author name = Kuemin J
| author affiliation = CONSUMERS ENERGY CO. (FORMERLY CONSUMERS POWER CO.),
| author affiliation = CONSUMERS ENERGY CO. (FORMERLY CONSUMERS POWER CO.),
| addressee name =  
| addressee name =  
Line 17: Line 17:


=Text=
=Text=
{{#Wiki_filter:. I, -* consumers Power l'OWERINli NllCHlliAN'S l'ROliRESS General Offices: 1945 West Parnall Road, Jackson, Ml 49201 * (517) 788-0550 May 9, 1988 Nuclear Regulatory Commission Document Control Desk Washington, DC 20555 DOCKET 50-255 -LICENSE DPR-20 -PALISADES PLANT -STEAM BINDING OF AUXILIARY FEEDWATER PUMPS -RESPONSE TO GENERIC LETTER 88-03 Generic Letter 88-03 concerning the resolution of Generic Issue 93, "Steam Binding of Auxiliary Feedwater Pumps" required Licensees to confirm that certain procedures are in place and will be maintained.
{{#Wiki_filter:.I, consumers Power l'OWERINli NllCHlliAN'S l'ROliRESS General Offices: 1945 West Parnall Road, Jackson, Ml 49201 * (517) 788-0550 May 9, 1988 Nuclear Regulatory Commission Document Control Desk Washington, DC 20555 DOCKET 50-255 - LICENSE DPR PALISADES PLANT -
In particular, it that the Licensee should: J. Maintain procedures to monitor fluid conditions within the AFW system each shift during times when the system is required to be operable.
STEAM BINDING OF AUXILIARY FEEDWATER PUMPS - RESPONSE TO GENERIC LETTER 88-03 Generic Letter 88-03 concerning the resolution of Generic Issue 93, "Steam Binding of Auxiliary Feedwater Pumps" required Licensees to confirm that certain procedures are in place and will be maintained. In particular, it r~quired that the Licensee should:
This monitoring should ensure that fluid temperature at the AFW pump discharge is maintained at about ambient levels. 2. Maintain procedures for recognizing steam binding and for restoring the AFW system to operable status, should steam binding occur. As stated in our response to IE Bulletin 85-01 dated February 26, 1986, the requirement to monitor the Auxiliary Feedwater piping is a part of our Auxiliary Building Data Sheet (Primary).
J. Maintain procedures to monitor fluid conditions within the AFW system each shift during times when the system is required to be operable. This monitoring should ensure that fluid temperature at the AFW pump discharge is maintained at about ambient levels.
This data sheet is completed by the Auxiliary Operator each shift and is reviewed and initialed by the shift Supervisor.
: 2. Maintain procedures for recognizing steam binding and for restoring the AFW system to operable status, should steam binding occur.
In addition, Attachment 2, Part III (system testing) to the Feedwater System Operating Procedure (SOP 12) specifies testing for check valve back leakage. This part includes guidelines for restoring the AFW system should high pump temperatures occur. By this letter, Consumers Power Company provides confirmation that the required procedures are in place and will be maintained.
As stated in our response to IE Bulletin 85-01 dated February 26, 1986, the requirement to monitor the Auxiliary Feedwater piping is a part of our Auxiliary Building Data Sheet (Primary). This data sheet is completed by the Auxiliary Operator each shift and is reviewed and initialed by the shift Supervisor.
OC0488-0116-NL02 8805120272 8:30509 PDR ADOCK 05000255 P DCD I'\ , Steam Binding of Auxiliary Feedwater Pumps -Response to Generic Letter 88-03 May 9, 1988 3 A copy of the current data sheet and the pertinent page for SOP 12 *is attached. L Kuemin Licensing Engineer CC Administrator, Region III, NRC NRC Resident Inspector
In addition, Attachment 2, Part III (system testing) to the Feedwater System Operating Procedure (SOP 12) specifies testing for check valve back leakage.
-Palisades Attachment OC0488-0116-NL02 CONSUMERS POWER COMPANY Palisades Plant Docket 50-255 License DPR-20 Response to Generic Letter No 88-03 Dated February 17, 1988 At the request of the Commission and pursuant to the Atomic Energy Act of 1954 and the Energy Reorganization Act of 1974, as amended, and the Commission's Rules and Regulations thereunder, Consumers Power Company submits our response to NRC letter dated February 17, 1988, entitled,"Resolution of Generic Safety Issue 93, "Steam Binding of Auxiliary Feedwater Pumps (Generic Letter 88-03)." Consumers Power Company's response is dated May 9, 1988. CONSUMERS POWER COMPANY David P Hoffman, Nuclear Operations Sworn and subscribed to before me this 9th day of May 1988. E Buehrer No ary Public Jackson County, Michigan My commission expires October 31, 1989 OA0488-0116-NL02 
This part includes guidelines for restoring the AFW system should high pump temperatures occur.
.: .. ''' .,, OPERATOR'S INI flALS 11*10 Hill EQUIPMENT ROOM F-54A PURIFICATION FILTER AP dPl-0204 (< 15 P51) F-54B PURIFICATION Fil TER AP dPl-0205 (< 15 PSll WGDT T-101APRESSURE PIA-1160 (< 100 PS1G) WGDT T-101B PRESSURE .PIA-1161
By this letter, Consumers Power Company provides confirmation that the required procedures are in place and will be maintained.
(< 100 PSIG) WGDT T-101C PRESSURE PIA-1162 (< 100 P51G) WEST SAFEGUARDS SUMP'ROOM LEI/EL ll-10078 (2-15%) EAST SAFEGUARDS SUMP1ROOM LEllEL Ll-11108 (2*
OC0488-0116-NL02 8805120272 8:30509 PDR ADOCK 05000255 P                         DCD
C-33 PANEL SECURE (2 LOCIC.S) WASTE GAS SURGE TANI( PRESSURE PIA-1111 (14* 1 5 PSIA) WGDT T*68A PRESSURE PIA-1119 (< 100 PSIG) WGDT T-68B PRESSURE PIA-1120 (< 100 PS1Gl WGDT T-68C PRESSURE PIA-1121 (< 100 PSIG) WASTE GAS DECAY TANK IN SERll1CE SOUTH LAUNDRY DRAIN TANK LEVEL LIA*l 124 (20*
NORTH LAUNDRY DRAIN TANK LE\/El LIA-1127 (20*7S%) WEST DIRTY WASTE TANK LEVEL LIA-1115 (20-92%) EAST DIRTY WASTE TANK LEVEL LIA* 1117 {20-92.,.l NORTH FILTERED WASTE TANK LEVEL LIA* 11 30 -(0-88'+-ii)
SOUTH Fil TE RED WAS TE TANK LEVEL LIA* 1133 Fil TERED WASTE TANK IN SERlll(E PRIMARY SYSTEM DRAIN TANK PRESSURE PIA-100'1 (0-S PS1G) PRIMARY SYSTEM DRAIN TANI( LEI/El LIA-1001 VACUUM DEGAS1F1ER TANK LEI/EL LI(* 1061 (40-60%) VACUUM DE GA SI FIE RT ANI( PRESSURE Pl-1004 (3*10PSIA)
VACUUM DEGAS1F1EA PUMP DISCH Pl* 1005 (65*90 PSIG) CLEAN WASTE ACVR TANI< PRESSURE PIA-1065 (<lPSIG) 'A' CLEAN WASTE AC\/A TANK LEVEL llA-1012 (<95"'i.l
'B' CLEAN WASTE ACllA TANK LEVEL LIA-1014
*c CLE AN WAS TE AC11A T ANIC LEVEL LIA-1016
'D' CLEAN WASTE. RCVA TANK LEllEL LIA-1018 (<95%) CLEAN WASTE ACVA TANK IN SERVICE NORTH CHEM DRAIN TANK LEVEL LIA-1006 SOUTH CHEM DRAIN TANK LEVEL LIA-1007 (20-80,.)
FUEL POOL DEMIN :. p dPIA 0924 (< 30 PSI) CONSUMERS POWER COMPANY .ILIARY BUILDING DATA SHEET e (Primary)
A B c DRAIN TANK LEI/EL LI *1008 (20 NORTH TREATED WASTE TANK LEI/EL (. ... LIA*1046 (0-90%) SOUTH TREATED WASTE TANIC LEI/EL LIA* 1048 1ND1CATED DILUTION FLOW FR-1050 C-161 GAS BOTTLES (3) (>200 PSIG) STATION 5 BOTTLE PRESSURE Pl-22 79A ( 2000 PSIG) STATIONS HEADER PRESSURE Pl-2279B (80-90 PSIG) 'A' CCW HEAT EXC11 dPl-0918 (< 1 7 PSI) 'B' CCW HEAT EXCH 6P dPl-0919 (< 17 PSI) y T .....-T .,,. 1J *c* AFW DISCH PIPING TO B SIG CCW TtMPtlUlTV"E TIC-OB21 (74-90&deg; f) r . "( ... _y) A&B AFW PIPING TO B SIG l A&B AFW PIPING TO A S1G I \ 'C' AFW PIPING TO A StG . --STATI'QN 1 BOTTLE PJftSSURE P1-2273A ( 2000 PSIG) STATION 1 HEADER PRESSURE Pl-2 2 738 (60* 70 PSIG) ST A TION 1 A BOTTLE PRE SS URE Pl-2280A ( 2000 PSIG) STATION lA HEADER PRESSURE P1*2280B (80*90 PSIGl SIRW TANK RECIRC TEMPERATURE n-0371 <45-100* Fl SPENT FUEL POOL PUMPIHX ROOM TREATED WASTE EQUIPMENT ROOM '8' BORIC ACID STOR TANK TEMPERATURE TIC-0206 (158-16S&deg;Fl
'B' BORIC ACID STOA TANK TEMPERATURE TIC-0207 (lSB-165&deg; F) 'A' BORIC ACID STOA TANK TEMPERATURE TIC-0208 {158-165*
Fl 'A' BORIC ACID STOA TANIC: TEMPERATURE TIC-0209 (158*165&deg; F) PURIFICATION DE MIN dPl-0203 (< 15 PSI) C* 162 GAS BOTTLES (3) ( >200 PS1Gl PUMP ROOM 'A' CHARGING PUMP OIL PRESSURE Pl-0217A (> 20 PSIG) *9* CHARGING PUMP OIL PRESSURE Pl-021 78 (>20 PSIG} 'C Ct1AAGING PUMP OIL PRESSURE I Pl-02 17( ( > 20 PSIG) 'A' CHARGING PUMP SEAL LEAKAGE ( < 500 ML/MIN) 'B' CHARGING PUMP SEAL LEAKAGE '. ( < 200 ML/MIN) *c* CHARGING PUMP SEAL LEAKAGE (<200 ML'MIN) PRIMARY SYSTEM DRAIN TANK PUMP ROOM S112W TAN< i.JOZ. Z.1.&#xa3;
.. *PIPING SHOULD BE COOL TO TOUCH. SIGNIFYING NO BA.CK LEAKAGE FROM THE STEAM GENERATORS I I 8 I A B c ! ' I I **.** .,. ... *:-: .. < . :T.r ' i l I ! I I ! I ! . * .. " .. I ' ! ' I ! --r-.. -----j ! ' '
I I ! I I l ! I i I ! I !
WG COMPRESSOR ROOM LAUNDRY TANK ROOM C-54 WG COMPRESSOR ROOM BAMIX TANK STATUS BA EYE WASH STATION FLUSH AUX BUILDING CHILLER & HN ROOM FUEL POOL TEMPERATURE TIA-0925 FUEL POOL LEVEL LOCAL VISUAL SFP GATE N 2 PRESSURE Pl 2252 (80-110&deg;F)
{2*8" <SKIM) { 10PS1G) SFP AREA SAFETY CHAINS IN PLACE SFP VENT & MCC ROOM V-8A&B VENT EQUIPMENT ROOM CV-3029 HP AIR Pl-30298 CV-3029 LP AIR Pl-3029A CV-3057 HP AIR Pt-30578 CV-3057 LP AIR Pl-3057A EAST SAFEGUARD HP AIR Pl-0439 * {170-175PSIG)
(55-65 PS1G) { 170-1 75 PSIG) (55-65 PSIG) (300-325 PSIG) A B c CV-3031 HP AIR Pl-30318 CV-3031 LP AIR P1-J031A CV-3030 HP AIR Pl-30308 CV-3030 LP AIR Pl-3030A WEST SAFEGUARD HP AIR Pt-0441 ( 170-1 75 PSIG) (55-65 PS1G) ( 1 70-1 75 PSIG) (55-65 PSIG) (300-325 PSIG) CONTAINMENT SAFETY CHAINS CONTAINMENT TOUR IF REACTOR HEAD REMOVED* CHECK FOR LOOSE MA TE RIAL SUPERVISOR"S REVIEW COMMENTS A NOTE: Out-of-specification readings are to be circled in red ink, and a brief explanation concerning the problem provided in the Comments Section.
SYSTEM TESTING ?roe No SOP 12 Attachment 2 Revision 12 Page 2 of 2 3. Stop the **K-7A; **K-78 auxiliary oil pump by turning its Local hand switch (Panel '"'''EC-24;
''*EC-25) from "auto" to "off" to "auto." III. TEST FOR CHECKVALVE BACKLEAKAGE
: l. Verify, by carefully touching the AFW piping near each flow control valve, that there is no backleakage from the steam generators. (If the piping is cool to the touch, significant backleakage does not exist.)
* 2. If the AFW piping is hot to the couch, take the following actions: 2.1 Notify Control Operator and Shift Supervisor.


===2.2 Check===
I'\
temperature of the associated AFW pump(s). 2.3 Start an AFW pump and flush the hot portions of the AFW piping to the steam generator(s).  
Steam Binding of Auxiliary Feedwater Pumps -                                  3 Response to Generic Letter 88-03 May 9, 1988 A copy of the current data sheet and the pertinent page for SOP 12 *is attached.
          /.~
L Kuemin Licensing Engineer CC Administrator, Region III, NRC NRC Resident Inspector - Palisades Attachment OC0488-0116-NL02


===2.4 Monitor===
CONSUMERS POWER COMPANY Palisades Plant Docket 50-255 License DPR-20 Response to Generic Letter No 88-03 Dated February 17, 1988 At the request of the Commission and pursuant to the Atomic Energy Act of 1954 and the Energy Reorganization Act of 1974, as amended, and the Commission's Rules and Regulations thereunder, Consumers Power Company submits our response to NRC letter dated February 17, 1988, entitled,"Resolution of Generic Safety Issue 93, "Steam Binding of Auxiliary Feedwater Pumps (Generic Letter 88-03)."
piping and pump temperatures for reoccurrence of backleakage.
Consumers Power Company's response is dated May 9, 1988.
2.S If an AFW pump is found too hot to touch (Step 2.2) or if high piping temperatures reoccur a Work Request/Work Order, to repair the leaking valves at the next shutdown, should be issued.
CONSUMERS POWER COMPANY David P Hoffman, Nuclear Operations Sworn and subscribed to before me this 9th day of May 1988.
* 2.6 If backleakage is sufficient to cause high pump temperatures, isolation of the leakage path with one of the FOGG valves should be considered. (Backleakage has actually disabled AFW pumps by steam-binding at other nuclear plants.) With the backleakage path isolated, the pump and local discharge piping should be vented to refill the pump with cool condensate.
E Buehrer No ary Public Jackson County, Michigan My commission expires October 31, 1989 OA0488-0116-NL02
The discharge piping should then be flushed to the steam generators and the FOGG valve reopened.
 
NOTE: Isolating FOGG valve renders associated flow control valve inoperable and initiates a 72 hrs LCO; see Technical Specification 3.S. pa0280-l043c-89-91}}
CONSUMERS POWER COMPANY
                                                  .ILIARY BUILDING DATA SHEET (Primary) e A            B    c                                                        A        B                  c E~UIPMENT    DRAIN TANK LEI/EL OPERATOR'S INI flALS                                                      LI *1008                              (20 90~.)
                                                            ~* :~          NORTH TREATED WASTE TANK LEI/EL 11*10 Hill EQUIPMENT ROOM                              (.  ...            LIA*1046                                (0-90%)                                        !
F-54A PURIFICATION FILTER AP                                              SOUTH TREATED WASTE TANIC LEI/EL                                                          '
dPl-0204                          (< 15 P51)                              LIA* 1048                                (0*90~o)
F-54B PURIFICATION Fil TER AP                                            1ND1CATED DILUTION FLOW                                                                I dPl-0205                          (< 15 PSll                              FR-1050                                                                                  I WGDT T-101APRESSURE                                                        C-161 GAS BOTTLES (3)                                  **.** .,....  *:-: :~
PIA-1160                        (< 100 PS1G)                                                                (>200 PSIG)                            .. < .
WGDT T-101B PRESSURE                                                      STATION 5 BOTTLE PRESSURE
.PIA-1161                        (< 100 PSIG)                              Pl-22 79A                      ( ~ 2000 PSIG)
WGDT T-101C PRESSURE                                                      STATIONS HEADER PRESSURE                                                          :T.r PIA-1162                        (< 100 P51G)                              Pl-2279B                          (80-90 PSIG)
WEST SAFEGUARDS SUMP'ROOM LEI/EL                                          'A' CCW HEAT EXC11 ~p ll-10078                            (2-15%)                              dPl-0918                              (< 17 PSI)
EAST SAFEGUARDS SUMP1ROOM LEllEL                                          'B' CCW HEAT EXCH 6P Ll-11108                            (2* 15~*l                            dPl-0919                              (< 17 PSI)                                        i C-33 PANEL SECURE (2 LOCIC.S) y    T . .-
                                                                        ~ *c* AFW DISCH PIPING TO B SIG T  .,,. 1J                                                        l I
WASTE GAS SURGE TANI( PRESSURE PIA-1111                        (14* 15 PSIA)
CCW TtMPtlUlTV"E TIC-OB21                              (74-90&deg; f)                        !
r    .        "( . . _y)
WGDT T*68A PRESSURE PIA-1119                        (< 100 PSIG)                              A&B AFW PIPING TO B SIG                                                                I WGDT T-68B PRESSURE PIA-1120                                                              l  A&B AFW PIPING TO A S1G                                                                I
(< 100 PS1Gl WGDT T-68C PRESSURE PIA-1121 WASTE GAS DECAY TANK IN SERll1CE
(< 100 PSIG)          I                \ .          -
                                                                            'C' AFW PIPING TO A StG STATI'QN 1 BOTTLE PJftSSURE I
P1-2273A                        ( ~ 2000 PSIG)
SOUTH LAUNDRY DRAIN TANK LEVEL                                            STATION 1 HEADER PRESSURE LIA*l 124                          (20* 75~o)                              Pl-2 2 738                        (60* 70 PSIG)
NORTH LAUNDRY DRAIN TANK LE\/El                                            ST ATION 1A BOTTLE PRE SS URE LIA-1127                          (20*7S%)                                Pl-2280A                        ( ~ 2000 PSIG)
WEST DIRTY WASTE TANK LEVEL                                                STATION lA HEADER PRESSURE LIA-1115                          (20-92%)                                P1*2280B                          (80*90 PSIGl EAST DIRTY WASTE TANK LEVEL                                                SIRW TANK RECIRC TEMPERATURE LIA* 1117                          {20-92.,.l                              n-0371                              <45- 100* Fl NORTH FILTERED WASTE TANK LEVEL                                            SPENT FUEL POOL PUMPIHX ROOM LIA* 11 30                          -(0-88'+-ii)
SOUTH Fil TE RED WAS TE TANK LEVEL LIA* 1133                            (0-88~)                              TREATED WASTE EQUIPMENT ROOM                                              I Fil TERED WASTE TANK IN SERlll(E                                          '8' BORIC ACID STOR TANK TEMPERATURE TIC-0206                          (158-16S&deg;Fl PRIMARY SYSTEM DRAIN TANK PRESSURE                                        'B' BORIC ACID STOA TANK TEMPERATURE PIA-100'1                        (0-S PS1G)                              TIC-0207                          (lSB-165&deg; F)                                        '
PRIMARY SYSTEM DRAIN TANI( LEI/El LIA-1001                          (20-90~*.)
                                                                            'A' BORIC ACID STOA TANK TEMPERATURE TIC-0208                          {158-165* Fl VACUUM DEGAS1F1ER TANK LEI/EL LI(* 1061                          (40-60%)
                                                                            'A' BORIC ACID STOA TANIC: TEMPERATURE TIC-0209                          (158*165&deg; F)                          I
                                                                                                                                                --r-..-----j VACUUM DE GA SI FIE RT ANI( PRESSURE                                      PURIFICATION DE MIN ~p                                                    !
Pl-1004                          (3*10PSIA)                                dPl-0203                              (< 15 PSI)                                        ''
VACUUM DEGAS1F1EA PUMP DISCH Pl* 1005                        (65*90 PSIG)
C* 162 GAS BOTTLES (3)
( >200 PS1Gl        H~i~ +;;;,?;w~
CLEAN WASTE ACVR TANI< PRESSURE PIA-1065                          (<lPSIG)                                CWRT~ESIN    PUMP ROOM                                                                I
'A' CLEAN WASTE AC\/A TANK LEVEL                                          'A' CHARGING PUMP OIL PRESSURE                                                          I llA-1012                            (<95"'i.l                              Pl-0217A                            (> 20 PSIG)
'B' CLEAN WASTE ACllA TANK LEVEL                                          *9* CHARGING PUMP OIL PRESSURE                                                          !I LIA-1014                            (<95~**>                              Pl-021 78                          (>20 PSIG}                                          I
*c CLE AN WAS TE AC11A TANIC LEVEL                                        'C Ct1AAGING PUMP OIL PRESSURE LIA-1016                            (<95~.)                        I      Pl-02 17(                          ( > 20 PSIG)
'D' CLEAN WASTE. RCVA TANK LEllEL LIA-1018                            (<95%)
                                                                            'A' CHARGING PUMP SEAL LEAKAGE
( < 500 ML/MIN)                                              l CLEAN WASTE ACVA TANK IN SERVICE                '.
                                                                            'B' CHARGING PUMP SEAL LEAKAGE
( < 200 ML/MIN)
                                                                                                                                                      !              I i
NORTH CHEM DRAIN TANK LEVEL                                                *c* CHARGING PUMP SEAL LEAKAGE                                                            I LIA-1006                          (20*80~**)                                                          (<200 ML'MIN)
SOUTH CHEM DRAIN TANK LEVEL LIA-1007                          (20-80,.)                              PRIMARY SYSTEM DRAIN TANK PUMP ROOM                                      I              !
FUEL POOL DEMIN :. p dPIA 0924                          (<  30 PSI)
S112W TAN< i.JOZ. Z.1.&#xa3; 1..~ICA<.~
                                                                                                                          .. ~"
*PIPING SHOULD BE COOL TO TOUCH. SIGNIFYING NO BA.CK LEAKAGE FROM THE STEAM GENERATORS
~,.,  II    8I
 
A    B        c                                                A CV-3031 HP AIR WG COMPRESSOR ROOM                                              Pl-30318                  ( 170-1 75 PSIG)
CV-3031 LP AIR LAUNDRY TANK ROOM                                                P1-J031A                      (55-65 PS1G)
CV-3030 HP AIR C-54 WG COMPRESSOR ROOM                                          Pl-30308                  ( 170-1 75 PSIG)
CV-3030 LP AIR BAMIX TANK STATUS                                                Pl-3030A                      (55-65 PSIG)
WEST SAFEGUARD HP AIR BA EYE WASH STATION FLUSH                                        Pt-0441                    (300-325 PSIG)
AUX BUILDING CHILLER & HN ROOM FUEL POOL TEMPERATURE                                            CONTAINMENT SAFETY CHAINS TIA-0925                        (80-110&deg;F)
FUEL POOL LEVEL                                                  CONTAINMENT TOUR LOCAL VISUAL                  {2*8" <SKIM)
SFP GATE N 2 PRESSURE                                            IF REACTOR HEAD REMOVED*
Pl 2252                        { ~ 10PS1G)
SFP AREA SAFETY CHAINS IN PLACE                                  CHECK FOR LOOSE MA TE RIAL SFP VENT & MCC ROOM V-8A&B VENT EQUIPMENT ROOM CV-3029 HP AIR Pl-30298                  * {170-175PSIG)
CV-3029 LP AIR Pl-3029A                        (55-65 PS1G)
CV-3057 HP AIR Pt-30578                    { 170-1 75 PSIG)
CV-3057 LP AIR Pl-3057A                        (55-65 PSIG)
EAST SAFEGUARD HP AIR                                            SUPERVISOR"S REVIEW Pl-0439                    (300-325 PSIG)
COMMENTS NOTE: Out-of-specification readings are to be circled in red ink, and a brief explanation concerning the problem provided in the Comments Section.
 
                                                                          ?roe No SOP 12 Attachment 2 Revision 12 Page 2 of 2 SYSTEM TESTING
: 3. Stop the **K-7A; **K-78 auxiliary oil pump by turning its Local hand switch (Panel '"'''EC-24; ''*EC-25) from "auto" to "off" to "auto."
III. TEST FOR CHECKVALVE BACKLEAKAGE
: l. Verify, by carefully touching the AFW piping near each flow control valve, that there is no backleakage from the steam generators. (If the piping is cool to the touch, significant backleakage does not exist.)      *
: 2. If the AFW piping is hot to the couch, take the following actions:
2.1  Notify Control Operator and Shift Supervisor.
2.2  Check temperature of the associated AFW pump(s).
2.3  Start an AFW pump and flush the hot portions of the AFW piping to the steam generator(s).
2.4 Monitor piping and pump temperatures for reoccurrence of backleakage.
2.S If an AFW pump is found too hot to touch (Step 2.2) or if high piping temperatures reoccur a Work Request/Work Order, to repair the leaking valves at the next shutdown, should be issued.
* 2.6 If backleakage is sufficient to cause high pump temperatures, isolation of the leakage path with one of the FOGG valves should be considered. (Backleakage has actually disabled AFW pumps by steam-binding at other nuclear plants.) With the backleakage path isolated, the pump and local discharge piping should be vented to refill the pump with cool condensate. The discharge piping should then be flushed to the steam generators and the FOGG valve reopened.
NOTE: Isolating FOGG valve renders associated flow control valve inoperable and initiates a 72 hrs LCO; see Technical Specification 3.S.
pa0280-l043c-89-91}}

Latest revision as of 13:02, 3 February 2020

Provides Confirmation That Required Procedures Re Generic Ltr 88-03 Concerning Generic Issue 93, Steam Binding of Auxiliary Feedwater Pumps, in Place & Will Be Maintained
ML18053A370
Person / Time
Site: Palisades Entergy icon.png
Issue date: 05/09/1988
From: Kuemin J
CONSUMERS ENERGY CO. (FORMERLY CONSUMERS POWER CO.)
To:
NRC OFFICE OF ADMINISTRATION & RESOURCES MANAGEMENT (ARM)
References
TASK-093, TASK-93, TASK-OR GL-88-03, GL-88-3, NUDOCS 8805120272
Download: ML18053A370 (6)


Text

.I, consumers Power l'OWERINli NllCHlliAN'S l'ROliRESS General Offices: 1945 West Parnall Road, Jackson, Ml 49201 * (517) 788-0550 May 9, 1988 Nuclear Regulatory Commission Document Control Desk Washington, DC 20555 DOCKET 50-255 - LICENSE DPR PALISADES PLANT -

STEAM BINDING OF AUXILIARY FEEDWATER PUMPS - RESPONSE TO GENERIC LETTER 88-03 Generic Letter 88-03 concerning the resolution of Generic Issue 93, "Steam Binding of Auxiliary Feedwater Pumps" required Licensees to confirm that certain procedures are in place and will be maintained. In particular, it r~quired that the Licensee should:

J. Maintain procedures to monitor fluid conditions within the AFW system each shift during times when the system is required to be operable. This monitoring should ensure that fluid temperature at the AFW pump discharge is maintained at about ambient levels.

2. Maintain procedures for recognizing steam binding and for restoring the AFW system to operable status, should steam binding occur.

As stated in our response to IE Bulletin 85-01 dated February 26, 1986, the requirement to monitor the Auxiliary Feedwater piping is a part of our Auxiliary Building Data Sheet (Primary). This data sheet is completed by the Auxiliary Operator each shift and is reviewed and initialed by the shift Supervisor.

In addition, Attachment 2, Part III (system testing) to the Feedwater System Operating Procedure (SOP 12) specifies testing for check valve back leakage.

This part includes guidelines for restoring the AFW system should high pump temperatures occur.

By this letter, Consumers Power Company provides confirmation that the required procedures are in place and will be maintained.

OC0488-0116-NL02 8805120272 8:30509 PDR ADOCK 05000255 P DCD

I'\

Steam Binding of Auxiliary Feedwater Pumps - 3 Response to Generic Letter 88-03 May 9, 1988 A copy of the current data sheet and the pertinent page for SOP 12 *is attached.

/.~

L Kuemin Licensing Engineer CC Administrator, Region III, NRC NRC Resident Inspector - Palisades Attachment OC0488-0116-NL02

CONSUMERS POWER COMPANY Palisades Plant Docket 50-255 License DPR-20 Response to Generic Letter No 88-03 Dated February 17, 1988 At the request of the Commission and pursuant to the Atomic Energy Act of 1954 and the Energy Reorganization Act of 1974, as amended, and the Commission's Rules and Regulations thereunder, Consumers Power Company submits our response to NRC letter dated February 17, 1988, entitled,"Resolution of Generic Safety Issue 93, "Steam Binding of Auxiliary Feedwater Pumps (Generic Letter 88-03)."

Consumers Power Company's response is dated May 9, 1988.

CONSUMERS POWER COMPANY David P Hoffman, Nuclear Operations Sworn and subscribed to before me this 9th day of May 1988.

E Buehrer No ary Public Jackson County, Michigan My commission expires October 31, 1989 OA0488-0116-NL02

CONSUMERS POWER COMPANY

.ILIARY BUILDING DATA SHEET (Primary) e A B c A B c E~UIPMENT DRAIN TANK LEI/EL OPERATOR'S INI flALS LI *1008 (20 90~.)

~* :~ NORTH TREATED WASTE TANK LEI/EL 11*10 Hill EQUIPMENT ROOM (. ... LIA*1046 (0-90%)  !

F-54A PURIFICATION FILTER AP SOUTH TREATED WASTE TANIC LEI/EL '

dPl-0204 (< 15 P51) LIA* 1048 (0*90~o)

F-54B PURIFICATION Fil TER AP 1ND1CATED DILUTION FLOW I dPl-0205 (< 15 PSll FR-1050 I WGDT T-101APRESSURE C-161 GAS BOTTLES (3) **.** .,.... *:-: :~

PIA-1160 (< 100 PS1G) (>200 PSIG) .. < .

WGDT T-101B PRESSURE STATION 5 BOTTLE PRESSURE

.PIA-1161 (< 100 PSIG) Pl-22 79A ( ~ 2000 PSIG)

WGDT T-101C PRESSURE STATIONS HEADER PRESSURE :T.r PIA-1162 (< 100 P51G) Pl-2279B (80-90 PSIG)

WEST SAFEGUARDS SUMP'ROOM LEI/EL 'A' CCW HEAT EXC11 ~p ll-10078 (2-15%) dPl-0918 (< 17 PSI)

EAST SAFEGUARDS SUMP1ROOM LEllEL 'B' CCW HEAT EXCH 6P Ll-11108 (2* 15~*l dPl-0919 (< 17 PSI) i C-33 PANEL SECURE (2 LOCIC.S) y T . .-

~ *c* AFW DISCH PIPING TO B SIG T .,,. 1J l I

WASTE GAS SURGE TANI( PRESSURE PIA-1111 (14* 15 PSIA)

CCW TtMPtlUlTV"E TIC-OB21 (74-90° f)  !

r . "( . . _y)

WGDT T*68A PRESSURE PIA-1119 (< 100 PSIG) A&B AFW PIPING TO B SIG I WGDT T-68B PRESSURE PIA-1120 l A&B AFW PIPING TO A S1G I

(< 100 PS1Gl WGDT T-68C PRESSURE PIA-1121 WASTE GAS DECAY TANK IN SERll1CE

(< 100 PSIG) I \ . -

'C' AFW PIPING TO A StG STATI'QN 1 BOTTLE PJftSSURE I

P1-2273A ( ~ 2000 PSIG)

SOUTH LAUNDRY DRAIN TANK LEVEL STATION 1 HEADER PRESSURE LIA*l 124 (20* 75~o) Pl-2 2 738 (60* 70 PSIG)

NORTH LAUNDRY DRAIN TANK LE\/El ST ATION 1A BOTTLE PRE SS URE LIA-1127 (20*7S%) Pl-2280A ( ~ 2000 PSIG)

WEST DIRTY WASTE TANK LEVEL STATION lA HEADER PRESSURE LIA-1115 (20-92%) P1*2280B (80*90 PSIGl EAST DIRTY WASTE TANK LEVEL SIRW TANK RECIRC TEMPERATURE LIA* 1117 {20-92.,.l n-0371 <45- 100* Fl NORTH FILTERED WASTE TANK LEVEL SPENT FUEL POOL PUMPIHX ROOM LIA* 11 30 -(0-88'+-ii)

SOUTH Fil TE RED WAS TE TANK LEVEL LIA* 1133 (0-88~) TREATED WASTE EQUIPMENT ROOM I Fil TERED WASTE TANK IN SERlll(E '8' BORIC ACID STOR TANK TEMPERATURE TIC-0206 (158-16S°Fl PRIMARY SYSTEM DRAIN TANK PRESSURE 'B' BORIC ACID STOA TANK TEMPERATURE PIA-100'1 (0-S PS1G) TIC-0207 (lSB-165° F) '

PRIMARY SYSTEM DRAIN TANI( LEI/El LIA-1001 (20-90~*.)

'A' BORIC ACID STOA TANK TEMPERATURE TIC-0208 {158-165* Fl VACUUM DEGAS1F1ER TANK LEI/EL LI(* 1061 (40-60%)

'A' BORIC ACID STOA TANIC: TEMPERATURE TIC-0209 (158*165° F) I

--r-..-----j VACUUM DE GA SI FIE RT ANI( PRESSURE PURIFICATION DE MIN ~p  !

Pl-1004 (3*10PSIA) dPl-0203 (< 15 PSI)

VACUUM DEGAS1F1EA PUMP DISCH Pl* 1005 (65*90 PSIG)

C* 162 GAS BOTTLES (3)

( >200 PS1Gl H~i~ +;;;,?;w~

CLEAN WASTE ACVR TANI< PRESSURE PIA-1065 (<lPSIG) CWRT~ESIN PUMP ROOM I

'A' CLEAN WASTE AC\/A TANK LEVEL 'A' CHARGING PUMP OIL PRESSURE I llA-1012 (<95"'i.l Pl-0217A (> 20 PSIG)

'B' CLEAN WASTE ACllA TANK LEVEL *9* CHARGING PUMP OIL PRESSURE !I LIA-1014 (<95~**> Pl-021 78 (>20 PSIG} I

  • c CLE AN WAS TE AC11A TANIC LEVEL 'C Ct1AAGING PUMP OIL PRESSURE LIA-1016 (<95~.) I Pl-02 17( ( > 20 PSIG)

'D' CLEAN WASTE. RCVA TANK LEllEL LIA-1018 (<95%)

'A' CHARGING PUMP SEAL LEAKAGE

( < 500 ML/MIN) l CLEAN WASTE ACVA TANK IN SERVICE '.

'B' CHARGING PUMP SEAL LEAKAGE

( < 200 ML/MIN)

! I i

NORTH CHEM DRAIN TANK LEVEL *c* CHARGING PUMP SEAL LEAKAGE I LIA-1006 (20*80~**) (<200 ML'MIN)

SOUTH CHEM DRAIN TANK LEVEL LIA-1007 (20-80,.) PRIMARY SYSTEM DRAIN TANK PUMP ROOM I  !

FUEL POOL DEMIN :. p dPIA 0924 (< 30 PSI)

S112W TAN< i.JOZ. Z.1.£ 1..~ICA<.~

.. ~"

  • PIPING SHOULD BE COOL TO TOUCH. SIGNIFYING NO BA.CK LEAKAGE FROM THE STEAM GENERATORS

~,., II 8I

A B c A CV-3031 HP AIR WG COMPRESSOR ROOM Pl-30318 ( 170-1 75 PSIG)

CV-3031 LP AIR LAUNDRY TANK ROOM P1-J031A (55-65 PS1G)

CV-3030 HP AIR C-54 WG COMPRESSOR ROOM Pl-30308 ( 170-1 75 PSIG)

CV-3030 LP AIR BAMIX TANK STATUS Pl-3030A (55-65 PSIG)

WEST SAFEGUARD HP AIR BA EYE WASH STATION FLUSH Pt-0441 (300-325 PSIG)

AUX BUILDING CHILLER & HN ROOM FUEL POOL TEMPERATURE CONTAINMENT SAFETY CHAINS TIA-0925 (80-110°F)

FUEL POOL LEVEL CONTAINMENT TOUR LOCAL VISUAL {2*8" <SKIM)

SFP GATE N 2 PRESSURE IF REACTOR HEAD REMOVED*

Pl 2252 { ~ 10PS1G)

SFP AREA SAFETY CHAINS IN PLACE CHECK FOR LOOSE MA TE RIAL SFP VENT & MCC ROOM V-8A&B VENT EQUIPMENT ROOM CV-3029 HP AIR Pl-30298 * {170-175PSIG)

CV-3029 LP AIR Pl-3029A (55-65 PS1G)

CV-3057 HP AIR Pt-30578 { 170-1 75 PSIG)

CV-3057 LP AIR Pl-3057A (55-65 PSIG)

EAST SAFEGUARD HP AIR SUPERVISOR"S REVIEW Pl-0439 (300-325 PSIG)

COMMENTS NOTE: Out-of-specification readings are to be circled in red ink, and a brief explanation concerning the problem provided in the Comments Section.

?roe No SOP 12 Attachment 2 Revision 12 Page 2 of 2 SYSTEM TESTING

3. Stop the **K-7A; **K-78 auxiliary oil pump by turning its Local hand switch (Panel '"'EC-24; *EC-25) from "auto" to "off" to "auto."

III. TEST FOR CHECKVALVE BACKLEAKAGE

l. Verify, by carefully touching the AFW piping near each flow control valve, that there is no backleakage from the steam generators. (If the piping is cool to the touch, significant backleakage does not exist.) *
2. If the AFW piping is hot to the couch, take the following actions:

2.1 Notify Control Operator and Shift Supervisor.

2.2 Check temperature of the associated AFW pump(s).

2.3 Start an AFW pump and flush the hot portions of the AFW piping to the steam generator(s).

2.4 Monitor piping and pump temperatures for reoccurrence of backleakage.

2.S If an AFW pump is found too hot to touch (Step 2.2) or if high piping temperatures reoccur a Work Request/Work Order, to repair the leaking valves at the next shutdown, should be issued.

  • 2.6 If backleakage is sufficient to cause high pump temperatures, isolation of the leakage path with one of the FOGG valves should be considered. (Backleakage has actually disabled AFW pumps by steam-binding at other nuclear plants.) With the backleakage path isolated, the pump and local discharge piping should be vented to refill the pump with cool condensate. The discharge piping should then be flushed to the steam generators and the FOGG valve reopened.

NOTE: Isolating FOGG valve renders associated flow control valve inoperable and initiates a 72 hrs LCO; see Technical Specification 3.S.

pa0280-l043c-89-91