ML17157A205
ML17157A205 | |
Person / Time | |
---|---|
Site: | Susquehanna ![]() |
Issue date: | 06/08/1990 |
From: | Gallo R NRC OFFICE OF INSPECTION & ENFORCEMENT (IE REGION I) |
To: | Keiser H PENNSYLVANIA POWER & LIGHT CO. |
Shared Package | |
ML17157A206 | List: |
References | |
NUDOCS 9006210048 | |
Download: ML17157A205 (100) | |
See also: IR 05000387/1990080
Text
ACCELERATED DISTRIBUTION DEMONSHMTION SYSTEM
REGULATORY INFORMATION DISTRIBUTiON SYSTEM (RIDS)
ACCESSION NBR:9006210048
DOC.DATE: 90/06/08
NOTARIZED: NO
DOCKET I
FACIL:50-387 Susquehanna
Steam Electric Station, Unit 1, Pennsylva
05000387
50-388
Susquehanna
Steam Electric Station, Unit 2, Pennsylva
05000388
AUTH.NAME
AUTHOR AFFILIATION
GALLO,R.M.
Region 1, Ofc of the Director
RECIP.NAME
RECIPIENT AFFILIATION
KEISERgH.W.
Power
s Light Co.
SUBJECT:
Forwards
EOP Insp
6 Requalification
Reexam Repts
50-387/90-08
& 50-388/90-80
on 900423-27.
DISTRIBUTION CODE:
IE42D
COPIES
RECEIVED:LTR
ENCL
SIZE:
TITLE: Operator Licensing Examination Reports
NOTES:LPDR
1
cy Transcripts.
LPDR 1 cy
Transcripts.
05000387
05000388
RECIPIENT
ID CODE/NAME
PDl-2
INTERNAL: ACRS
NRR SHANKMAN,S
NRR/DLPQ/LOLB10
RGN1
FILE
01
EXTERNAL: LPDR
NOTES:
COPIES
LTTR ENCL
1
1
2
2
1
1
1
1
1
1
1
1
1
1
2
2
RECIPIENT
ID CODE/NAME
THADANI,M
AEOD/DSP/TPAB
NRR/DLPQ/LHFBll
EG F
02
NRC PDR
COPIES
LTTR ENCL
1
1
1
1
1
1
1
1
1
NOTE TO ALL"RIDS" RECIPIENTS:
PLEASE HELP US TO REDUCE WASTE! CONTACT THE DOCUMENT CONTROL DESK.
ROOM P 1-37 (EXT. 20079) TO ELIMINATEYOUR NAMEFROM DISTRIBUTION
LISTS FOR DOCUMENTS YOU DON'T NEED!
TOTAL NUMBER OF COPIES
REQUIRED:
LTTR
15
ENCL
15
~ g
JUN
8 199Q
Docket Nos.
50-387
50-388
Power
and Light Company
ATTN:
Mr . Harold W.
Kei ser
Senior Vice President
Nuclear
2 North Ninth Street
Al 1 entown,
Penn sy1 van ia
18101
Gentlemen:
SUBJECT:
EMERGENCY OPERATING
PROCEDURES
INSPECTION AND REQUALIFICATION
RE-EXAMINATION- REPORT
NOS 50-387/90-80
and 50-388/90-80
This refers to the special
safety inspection
conducted
by an
NRC Emergency
Operating
Procedure
Inspection
Team
on April 23-27,
1990, of acti vities at the
Susquehanna
Steam
El ectr ic Station
(SSES) Units
1 and 2,
and requal ification
re-examinations
admi ni stered
on Apri 1 25,
1990,
and to the di scussi on of our
findings with Mr.
H .
G. Stanley
and other members of your staff at the concl u-
sion of the inspection
~
The purposes
of the i n specti on were to veri fy that the
Emergency Operating
Procedures
( EOPs)
are technically correct, that the
EOPs can
be physically
carried out in the plant,
and that the
can
be implemented
by the plant
staff, ~
The inspection
concluded
the
EOPs are generally acceptable
~
However, there
were
many differences identified between
the
and the
BWR Owner '
Group
Emergency
Procedure
Guidelines
and the
Emergency
Procedure
Guidelines
which need addi tiona1 attenti on
~
The inspection
concluded that the
can
be physically carried out in the
plant and the operators
can
implement the procedures.
However, findings and
concerns
were identified which affected both areas.
The most significant
finding i s the limited avai 1 abi 1 ity of suppression
chamber
pressure
i ndi cati on
to make decisions
in the primary containment control
.
Another area of
concern is the
suppor ting procedures
for carrying out the
EOP di rected tasks .
The steps
necessary
to carry out the
EOP di rected tasks
( e
~ g ~, venting of
generally involve use of multiple procedures
and
do not
reference
the procedure
section utilized to per form the specific steps
needed,
this determinati on i s left to the user.
While the training and ability of your
staff allowed the tasks to be p'erformed during the
wa 1 kdown s, the procedura
1
method could result in delay or error i n accompl i shi ng
EOP directed tasks .
Your staff took prompt action to i n form the plant operator s of the suppression
chamber
pressure
indication issue
and determined that
an engineering
analysis
would be completed.
90062 i0048 900b08
P DR
ADOCK 05000387
9
PNU
II
~
r,ro
c
Power 5 Light Company
In a telephone
discussion
between your staff (R. Wehry, J. Maertz,
and
D. Kaposchinsky)
and
D. Florek of this office on May 18,
1990,
we were informed
of the results of the engineering
analysis
and short term and long term plans
regarding
the suppression
chamber
pressure
issue.
Procedure
changes
are to be
implemented
by June
15,
1990,
and long term plans include adding wide range
suppression
chamber
pressure
indication in the control
room.
Several
unresolved
items are
summarized
in the executive
summary of the
enclosed
inspection report.
We note that your staff had identified that
a
schedule for resolution of the inspection findings,
as presented
to your staff
by the
NRC inspection
team,
would be provided by June
15,
1990.
We request
that you respond,
in writing, within 30 days of receipt of this letter confirm-
ing your staffs verbal
commitments in the
May 18,
1990 telephone
discussion
and
identifying the actions
taken or planned to address
the specific unresolved
items identified in the Executive
Summary of the enclosed
inspection report.
In addition, requalification re-examinations
were administered
to two reactor
operators
who had previously failed the simulator portion of the requalifica-
tion examination.
Both reactor operators
passed
the requalification re-exami-
nations.
In accordance
with 10
CFR 2.790 of the Commission's
regulations,
a copy of
this letter and the enclosures will be placed in the
NRC Public Document
Room.
The responses
requested
by this letter are not subject to the clearance
proce-
dures of the Office of Management
and Budget as required
by the paperwork
reduction act of 1980, Public
Law No.96-511.
Should you have
any questions,
please
contact the undersigned
at (215) 337-
5291.
Sincerely,
Original Signed Bg$
ROBERT M. GALLO
Robert
M. Gallo, Chief
Operations
Branch
Divisi on
of Reactor Safety
Enclosure:
Combined Report Nos. 50-387/90-80
and 50-388/90-80
cc w/encl.:
A.
R. Sabol,
Manager,
Nuclear Quality Assurance
J.
M. Kenny, Licensing Group Supervisor
R.
G.
Bryam, Superintendent
of Plant-SSES
S.
B. Ungerer,
Manager, Joint Generation
Projects
Department
J.
D. Decker,
Nuclear Services
Manager,
General
Electric Co.
OFFICIAL RECORD
COPY
FLOREK/SSES
REPORT/5/15/90 - 0001.1.0
06/07/90
'l
h
1P
I
h
Jl
E
t
lI
pgg
1 'p H
Power 5 Light Company
cc w/encl. (cont'd.):
B. A. Snapp,
Esquire, Assistant Corporate
Counsel
H.
D. Moodeshick,
Special Office of the President
J.
C. Tilton, III, Allegheny Electric Cooperative,
Inc.
C. Meeker,
System Specialist,
COMEX
L. Ostrom,
Human Factor Specialist,
INEL
Public Document
Room (PDR)
Local Public Document
Room (LPDR)
Nuclear Safety Information Center
(NSIC)
'RC
Resident
Inspector
Commonwealth of Pennsylvania
bcc w/encl.:
Region I Docket
Room (with concurrences)
Management Assistant,
DRMA (w/o encl)
R. Bellamy,
DRSS
P.
Swetland,
J. Caldwell,
M. Thadani,
M. Hodges,
R. Gallo,
R. Conte,
D. Florek,
Master-Exam
Fi1 e
OL Facility File
DRS Files (5)
06/
/90
06
/90
Gallo
06/
/90
Jo
on
06/ /
Ho
06/ /
OFFICIAL RECORD
COPY
FLOREK/SSES
REPORT/5/15/90 - 0002.0.0
06/07/90
4'
ll
U.S.
NUCLEAR REGULATORY COMMISSION
REGION I
SUSQUEHANNA STEAM ELECTRIC STATION
EMERGENCY OPERATING PROCEDURE
INSPECTION
Combined
Re ort Nos.
Faci1 it
Docket Nos.
Facilit
Licence Nos.
Licensee:
N
Ins ection Conducted:
Team Members:
50-387/90-80
and 50-388/90-80
50-387
and 50-388
Power
and Light Company
2 North Ninth Street
Allentown, Pa.
18101
Susquehanna
Steam Electric Station Units
1 and
2
Berwick,
Pa
April 23-27,
1990
C. Meeker,
System Specialist,
COMEX
J. Stair,
SSES Resident
Inspector
L. Ostrom,
Human Factor Specialist,
INEL
T. Walker, Senior Oper tions Engineer,
Region I
Team Leader:
Donald J. Flore
,
r. Operations
Engineer
D te
chard J.
Conte,
hief,
BWR Section
Operations
Branch,
ate
r
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Ins ection Summar:
Ins ection
on A ril 23-27
1990
Combined Ins ection
Re ort Nos. 50-387/90-80
and 50-388/90-80
Areas Ins ected:
Special
announced
inspection of the Susquehanna
Steam Elec-
tric Station
SSES)
Emergency Operating
Procedures
(EOPs) to include
a compa-
rison of the
EOPs with the
BWR Owner's
Group Emergency
Procedure
Guidelines
and
the plant specific
Emergency
Procedure
Guidelines,
a review of the
by
control
room and plant walkdowns,
an evaluation of the
on the plant refer-
ence simulator,
a
human factors analysis of the
EOPs,
a review of the on-going
evaluation
program for EOPs,
and the quality assurance
program involvement in
the
EOPs.
Results:
See Executive
Summary in Report,
N'
P
em~
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"
~
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Executive
Summar
The technical
adequacy
review (Section
4) identified differences
between
the
Susquehanna
Steam Electric Station
Emergency
Procedure
Guidelines
(SSES
EPGs),
the
BWROG Emergency
Procedure
Guidelines
and the
EOPs.
These
differences
included different entry condition values, different logic sequences,
different system
usage,
and different setpoint values.
In the differences identified between
the
and the
EPGs (Un-
resolved
Items 387 & 388/90-80-01),
the documented justification was not always
sufficient to determine that the differences
were technically acceptable.
The
major differences
include entry condition into the
RPV Control guideline
on low
reactor water level, entry condition into the Primary Control guideline
on high
suppression
pool temperature,
a majority of the entry conditions into. the
Secondary
Control guideline,
and the level/power control strategy.
The differences
between
the
and the
EOPs include activities
or logic
required in the
EPGs that cannot
be identified in the
as well as
activities or logic found in the
EOPs that cannot
be supported
by the
EPGs.
(Unresolved
items 387 & 388/90-80-02).
The team identified that suppression
chamber pressure
indication would not
always
be available during emergency conditions which affects the ability of
the operator to make the decisions
required in the primary containment control
EOP.
The control
room indication is limited to 3 psig, is isolated for 10
minutes following a
LOCA signal,
must
be read locally when it exceeds
3 psig
and the local indication
may not be accessible
due to environmental
conditions.
This was the most significant individual item identified by the
NRC inspection
team.
The licensee
took prompt corrective action
as discussed
below.
(Un-
resolved
items
387 & 388/90-80-03).
The walkdowns of the
EOPs in the plant concluded that the
can
be performed
(see
section 5.0).
However,
the supporting
procedures
for carrying out
directed tasks
are generally difficult to use
due to the method of
referencing'etween
procedures
and the use of a series of procedures
(ES/ON/OP) to accom-
plish
some
EOP directed activities.
This method of procedure
use results in
unnecessary
steps
which may not be able to be accomplished
and could result in
delay or error in the completion of the
EOP directed task.
The inspection
determined that
some procedural
steps
are identified in
EOP basis
documents
and
not in procedures,
some confusing
steps
are contained
in the
and
some
equipment is difficult to access.
(Unresolved
items
387
& 388/90-80-04).
Notwithstanding the above,
the operators
accomplished
the
EOP tasks with reli-
ance
on their'knowledge
and training.
The simulator exercises
(section
6) demonstrated
that the operators
can effect-
ively utilize the.EOPs
to respond to plant accidents.
The simulator exercises
and follow-up discussions
with the operators
confirmed many of the items that
were identified in the
NRC human factor and technical
reviews.
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The
human factors review (section
7) concluded that the
EOPs are high quality
with an appropriate
level of detail
and
a clearly designed
format.
Operator
acceptance
of the flow chart format is very high.
From
a
human factors stand-
point, operators
used
the flowchart portion of the
EOPs very well in the
simulator.
Human factors concerns
(Unresolved
items
387 5 388/90-80-05) with the
stem
primarily from the inconsistencies
in the implementation of the direction from
the
EOP writers guide
(AD-QA-330) or lack of direction for formatting numerous
steps.
The numerous
inconsistencies
suggest that the verification of the
was less than adequate.
Although the inconsistencies
did not cause
any obvious
problems in human performance
in the simulator scenarios,
in real
emergencies,
inconsistencies
may impact the use of the
EOPs.
The
human factors review also
supported
the concern
on the manner in which the operators
were directed to
various supporting procedures.
The number
and type of transitions takes
time
and
may cause
operator error and confusion.
The ongoing evaluation
program (section 8) for the
EOPs is recently developed.
This program identifies and tracks
open items, deficiencies
and enhancements
for the
and the
EPGs identified outside of the validation and veri-
fication program.
The program is acceptable
with additional effort needed in
the licensee's prioritization of
EOP open items.
As discussed
in section 9.0,
QA involvement in the initial development of the
was minimal.
The
QA Department is scheduled
and prepared
to be
an active
participant in the major
EOP revision process
that will incorporate revision
4
the
BWR Owner's
Group
EPGs.
The inspection
concluded that the apparent
reason for the majority of the
inspection findings was that the verification and validation process
performed
on the prior revisions of the
was less
than adequate.
The verification
process
compared
the
EPGs to the
EOPs to ensure that
EPG actions were
contained
in the
EOPs,
but did not ensure that all
EOP actions
were justified
in the
EPGs.
The validation program did not walkdown all of the support-
ing EOPs.
In addition, the problems
appear to have
been
compounded
by failure
to update
the
EPGs when revising the
EOPs.
Prior to the inspection,
the
licensee
revised the
EOP program controls for future
EOP revisions
based
on
lessons
learned
from other facility EOP inspections
(NUREG-1358).
The
program controls for future revisions of the
EOPs were generally acceptable
and
should preclude the additional similar problems in the future.
Prior to the
inspection,
the licensee
reviewed the current
EOPs using the
new program
controls
and identified many of the
same
items that were identified by the
inspection
team.
The staff at
SSES took prompt action to inform the plant operators of the
suppression
chamber pressure
indication issue
and identified that an engineer-
ing analysis would be completed
by May 11,
1990, with follow-up actions to be
implemented
by May 18,
1990.
A schedule for resolution of the remainder
detailed inspection findings would be provided by June
15,
1990.
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Section
11.0 discusses
the requalification re-examinations
administered
to two
Reactor Operators
(ROs)
who had failed this portion of the requalification
examination administered
during the week of January
22,
1990.
Both operators
passed
the examinations.
I
t
DETAILS
1.0
~Back round
Following the Three Mile Islan'd (TMI) accident,
the Office of Nuclear
Reactor Regulation developed
the "TMI Action Plan"
and
NUREG-
0737) which required licensees
of operating reactors to reanalyze transi-
ents
and accidents
and to upgrade
emergency
operating
procedures
(EOPs)
(Item I.C. 1).
The plan also required the
NRC staff to develop
a long-term
plan that integrated
and expanded efforts in the writing, reviewing,
and
monitoring of plant procedures
(Item I.C.9).
"Guidelines for
the Preparation
of Emergency Operating
Procedures,"
represents
the
NRC
staff's long-term program for upgrading
EOPs,
and describes
the use of a
"Procedure
Generation
Package"
(PGP) to prepare
EOPs.
The licensees
formed four vendor
type owner groups corresponding
to the four major
reactor types in the United States.
Working with General Electric and the
NRC, the Boiling Water Reactor
Owners
Group
(BWROG) developed
the
Emergency
Procedure
Guidelines which are generic
procedures
that set forth
the desired
BWROG accident mitigation strategy.
The
EPGs were to be used
by the licensee
in developing their
PGP.
Submittal of the
PGP was
made
a
requirement
"Supplement
1 to NUREG-0737, Require-
ments for Emergency
Response
Capability.".
The generic letter requires
each licensee
to submit
a
PGP which includes:
(i)
Plant-specific technical
guidelines
(ii) A writers guide
(iii) A description of the program to be used for the validation
of EOPs
(iv) A description of the training program for the upgraded
From this
PGP, plant specific
EOPs were to have
been developed that would
provide the operator with the directions to mitigate the consequences
of
a broad range of accidents
and multiple equipment failures.
The
PGP for the Susquehanna
Steam Electric Stations
(SSES)
was submitted
to the
NRC in
a letter dated
May 13,
1985.
The Safety Evaluation for the
was issued
on March 16,
1990.
To determine
the success
of the implementation,
generically,
a series of
NRC inspections of EOPs were conducted
in 1988 which examined
the final
product of the program,
the
EOPs.
The results of the
NRC inspections
conducted during 1988 were
summarized
in NUREG-1358 "Lessons
Learned
from
the Special
Inspection
Program for Emergency Operating Procedures."
This
inspection is
a continuing effort of the
NRC to evaluate
the
EOPs at
licensee facilities.
During the week of April, 23-27,
1990,
an
NRC team of inspectors consist-
ing of two
NRC license operators
examiners/inspectors,
a reactor
systems
consultant,
a
human factor specialist
and the resident inspector
conducted
an inspection of the Emergency Operating
Procedures
(EOPs) at the Susque-
hanna
Steam Electric Station
(SSES) Units
1 and 2.
SSES is a
BWR 4 with a
Mark II containment structure.
The objectives of the inspection
were to
determine if: the
EOPs are technically correct;
the
can physically
carried-out in the plant;
and that the
can
be performed
by the plant
staff.
The objectives would be considered
to be met if review of the following
areas
were found to be adequate:
comparison of the
EOPs with the
emergency
procedure
guidelines
(SSES
EPG)
and the
BWROG emergency
proce-
dure guidelines
(BWROG EPG), review of the technical
adequacy of the
deviations
from the
room and plant walkdowns of the
EOPs,
real time evaluation of the
on the plant simulator, evaluation
of the licensee
program
on continuing improvement of the
and perform-
ance. of human factor analysis of the
EOPs.
The inspection
focused
on the
adequacy of the end product,
the
EOPs,
and did not depend
'on the review of
the process
to develop the
EOPs.
If any of the areas
were not found to be
acceptable,
the inspection
would assess
other areas
as necessary
to under-
stand the basis for the deficiencies.
-The-EOPs
were implemented in essentially their current form in August
1985.
The facility utilized the
(SSES version of the plant
specific technical guideline), writers guide, verification and validation
program
as described
in the procedures
generation
package
submitted to the
NRC in May 1985.
Two procedure
revisions
had
been
made to the
since
August 1985.
The facility has modified their administrative
program
controls
and
EOP development
process
since the initial revision of the
EOPs following issuance
of NUREG-1358.
The revised
program
has identified
many of the
same
items
as the
NRC inspection
team.
2.0
Persons
Contacted
Sus
uehanna
Steam Electric Station
J. Diltz, Plant Control Operator
R. Dixon,
"A. Dominguez,
Sr, Results
Engineer
"A. Fitch, Operations Training Supervisor
E.
Heckman,
Sr. Project Engineer
"D. Heffelfinger, Coordinator Engineer - NQA
"D. Kapuschinsky,
Sr. Nuclear Plant Specialist
M. Kirkpatrick, Plant Control Operator
"W. Lowthert, Manager
Nuclear Training
- J. Maertz, Operations
Engineer
- T. Markowski, Dayshift Supervisor
tb
t VV'ly Illghtq,yb(AVW,(pVYQI/ge'~Vg~CPP+J lllo f gpt ls'V4'"P
2.0
Persons
Contacted
Cont'd.
J. Miller, Plant Control Operator
L. Patnaude,
Human Factors Specialist
- M. Peal,
Nuclear Operations Training Supervisor
"R. Prego,
QA Supervisor - Operations
"J. Refling Sr. Project Engineer-Systems
Engineering
"E. Stanley,
Superintendent
of Plant
"R. Wehry, Compliance Engineer
U. S. Nuclear
Re ulator
Commission
S. Barber,
Senior Resident
Inspector
"D. Florek,- Sr. Operations
Engineer
"C. Meeker,
NRC Consultant
COMEX
- L. Ostram,
NRC Consultant - INEL
"J. Stair,
Resident
Inspector
- T, Walker, Sr. Operations
Engineer
The inspectors
also contacted
other members of the licensee
operation
and
technical staff.
- Denotes those present at the exit meeting conducted
on April 27,
1990.
3.0
Basic
EOP/BWR Owners Grou
Com arison
A comparison of the facility EOPs
and
BWR Owners Group Emergency
Procedure
Revision 3,
was conducted to ensure that the
licensee
has developed
the procedures
indicated in the
BRWOG EPGs.
The
EOPs reviewed are listed in Attachment
A of this report.
The facility
EOPs are in agreement with the'WROG
on the type of procedures
required to respond to symptoms which result in entry into these
proce-
dures'~
4.0
Inde endent Technical
Ade uac
Review of the
Emer enc
0 eratin
Procedures
The
EOPs in Attachment
A were reviewed to assure that the procedures
are
technically adequate
and accurately
incorporate
the
BWR Owners
Group
Emergency
Procedure
Guidelines
A comparison of the
Emergency
Procedure
Guidelines
(SSES
EPGs) to the
and
was
also performed.
Differences
between
the
and
EPGs were
assessed
for adequate
technical justification.
Selected
specific values
from the procedures
were reviewed to determine that the values
were
correct.
4.1
and
In general,
the differences
between. the
and the
have adequate
technical justification.
Several differences
identi-
fied by the
NRC inspection
team did not have adequate
technical
l
II
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justification.
These justifications are for differences
in entry
conditions to
RPV Control, Primary Containment Control
and Secondary
Containment Control, deletion of the secondary
containment water
level control guidelines,
and for not removing fuses to de-energize
scram solenoids
in the reactor
power control leg of RPV Control
(RC/Q).
The details of these differences
are discussed
in Attachment
B of this report.
The differences
between
the
and the
EPGs is considered
to be
an unresolved
item (387/90-80-01
and
388/90"80"01).
The
EPG accident mitigation strategy for Level/Power Control
differs from the
SSES limits the controlled lowering of
RPV water level to -129 inches rather than to the top of active fuel
(-161 inches).
This results
in a higher steady state
power level
being maintained for the
ATWS condition.
The differences
between
the
EPG strategy
and the
EPG strategy
have
been
the topic of
several
meetings
between
the licensee
and
NRC Headquarters
staff.
. This inspection did not assess
whether the licensee
developed
strategy is technically adequate,
but only assessed
whether the
licensee
has
implemented their strategy in the
EOPs,
The inspectors
identified discrepancies
between
the
and the
EOPs for
level/power control
as discussed
in Section 4.2.
The inspectors
also
questioned
the facility as to whether their accident mitigation
strategy
should defer to the
EPG strategy
when suppression
pool
temperatures
approach
the
HCTL curve as discussed
in section 4.4.
4.2
Com arison of SSES
and
The
NRC inspection
team identified a large
number of inconsistencies
between
the
and the
EOPs.
These inconsistencies
include
directions in the
EOPs that are not included in the
EPGs;
differences
between
the
and the
EOPs for procedure refer-
ences,
figure titles,
and parameter
values;
cases
in which the logic
of the
EPGs is not preserved
in the
EOPs;
and
EOP directions
that do not meet the intent of the
EPG guidelines.
Examples of
these
inconsistencies
are provided in the following paragraphs.
The
detailed findings are discussed
in Attachment
B.
The steps
in the
EOPs do not have to correspond
verbatim or on
a
one-for-one basis with the plant specific guidelines
in the
EPGs, but the
EOPs must preserve
the logic delineated
in the plant
specific guidelines.
The inspection
team identified areas of RPV
Control, Primary Containment Control, Secondary
Containment Control,
Level Restoration,
Level/Power Control
and
RPV Flooding in which the
logic of the
EPGs is not preserved
in the
EOPs.
Examples of
logic sequences
that are not preserved
in the
EOPs include the
direction for reactor
power control
when power is less
than
5/o, but
all control rods are not inserted; direction for rapid depressuriza-
.tion while implementing Secondary
Containment Control
and Level/Power
Control;
and direction for RPV flooding in the Primary Containment
Pressure
Control leg of E0-103.
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The inspection
team identified
EOP directions that did not meet the
intent of the
EPG guidelines.
These inconsistencies
resulted in
omission of SSES
EPG directions, conflicting direction in the
EOPs,
and incomplete
or incorrect directions in the
EOPs.
Examples of
these
problems include conflicting guidance for RPV pressure
control
when pressure
must be reduced for suppression
pool level or temper-
ature control,
no direction to reduce
RPV injection when performing
RPV flooding with more than
one control rod not inserted,
and entry
into Secondary
Containment
Control based
on conditions rather than
symptoms of high secondary
containment
temperature.
The inspection
team identified several
parameter
values that are not
consistent
between
the
and the
EOPs.
In most cases,
the
values in the
EOPs are
more conservative
than the values in the
EPGs.
In these
cases,
the
EOP values were clearly chosen
because
they could be easily determined
using available indications.
While
this is an adequate
reason for choosing
these
values, it is not
documented.
For example,
the limitation for use of SRVs was changed
from 4.5 feet as specified in the
EPGs to
5 feet in the
EOPs.
In several
cases,
the deviations
in the parameters
are not clearly
conservative
and
may result in incorrect direction in the
EOPs.
For
example,
the
EPGs specify
111 psig as the Minimum RPV Flooding
Pressure,
while EO-114 specifies
values
based
on the
number of open
SRVs.
All of the values in EO-114 are lower than
111 psig.
The
EPGs often reference
specific procedures
for performing
related actions.
One of the purposes
of the
EPG is to specify
the technical
guidelines for the procedures.
The verification
process for the
EOPs should ensure that all the technical
guidelines
are incorporated into the
and procedures
referenced
by the
EOPs.
Other plant procedures
should not be used
as
source basis
documents
for the
EPGs.
Several
discrepancies
were identified with
procedure
references
in the
and
EOPs.
For example,
the
EPG referred to a procedure for cold shutdown that was in-
correctt.
EO-101 referred to the correct procedure.
The inspection
team also identified numerous actions
in the
EOPs that
are not justified or addressed
in the
EPGs.
The
do
not need to delineate
specific actions that must be performed,
but
all
EOP actions which affect the accident mitigation strategy
should
be contained
in the
EPG and justification should
be provided for
any actions that are not addressed
in the
Examples of
actions in the
EOPs that are not addressed
in the
EPGs include
bypassing
high steam tunnel
temperature
and low condenser
vacuum MSIV
closure interlocks, initiation of ARI, and
shutdown of Core Spray
pumps
when performing rapid depressurization
with more than
one
control rod not fully inserted.
This problem appears
to have
resulted
from simultaneous
development of the
and
EPGs,
rather than developing the
EOPs from the plant specific guidelines.
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Several
discrepancies
between
the
and
EOPs related to plant
equipment
were identified by the inspection
team.
For example,
the
EPGs direct use of the Reactor Water Cleanup
system for inject-
ion of boron, but there is no method available for performing this
action.
The verification process
that was performed
on the current
and prior
versions of the
EOPs did not detect the numerous
inconsistencies
between
the
and
due to deficiencies
in the process.
The verification process
compared
the
EPGs to the
EOPs to ensure
that
EPG actions
were contained
in the
EOPs,
but did not ensure
that all
EOP actions
were justified in the
EPGs.
This problem
appears
to have
been
compounded
by fai lure to update the
when revising the
EOPs.
Prior to the inspection,
the licensee
revised the
EOP program
controls for future
EOP revisions
based
on the lessons
learned
from
other facility EOP inspections
(NUREG-1358).
The
program
controls for future revisions of the
EOPs were generally acceptable
and should preclude the type of inspection findings in the future.
Prior to the inspection
the licensee
reviewed the current
EOPs using
the
new program controls
and identified many of the
same
items that
were identified by the inspection
team.
(Licensee identified items
-- are ind'icated in the detailed findings in Attachment B.)
Many of the
facility identified items still remain
open
(see Section 8.0).
The differences
between
the
and the
EOPs are considered
to
be unresolved
item (387/90-80-02
and 388/90-80-02).
4.3
Technical
Ade uac
of EOPs
During the technical
adequacy
review of the
EOPs,
the inspection
identified deficiencies
in several
areas.
A few incorrect transi-
tions caused
by typographical
errors were identified.
.Several
proce-
dures contained
steps that did not appear to be necessary
or steps
that did not appear to be in the correct order for performance of the
desired action.
The majority of the technical
adequacy deficiencies
consisted of
terms that were are not clearly defined and steps that do not provide
complete direction.
For example,
the terms "reactor shutdown"
and
"SRV cycling" are not clearly defined in the
EOPs or in the
EOP basis
documents.
Procedural
direction is provided to restrict
use of HPCI
and
RCIC with low suppression
pool water level, but EO-103 does not
provide direction to override initiation signals which would be
necessary
to prevent automatic operation of HPCI and
RCIC.
The inspectors identified one technical
adequacy
problem that indi-
cated that the associated
procedures
could not be utilized.
Suppress-
ion chamber
pressure
above
3 psig cannot
be monitored for at least
10
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isolation signal at 1.72
psig
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Suppression
chamber pressure
indication is not available in
the Control
Room above
3 psig.
Local indication using the Contain-
ment Atmosphere Monitoring (CAM) system is isolated for 10 minutes
following the isolation signal
and must be realigned manually and
read locally.
Actions for Primary Containment
Pressure
Control,
Drywell Temperature
Control,
Level Restoration,
and
RPV Flooding are
dependent
upon suppression
chamber pressure.
The licensee
took
prompt corrective action to identify the issue to the operators
and
provided additional direction
on
how to handle the loss of suppress-
ion chamber
pressure.
The licensee
indicated that by May 11,
1990 an
engineering
evaluation
would be completed
on alternate
indications to
be utilized for primary containment control.
This was acceptable
to
the inspection
team.
Pending licensee
actions to resolve the adequ-
acy of suppression
chamber pressure,
this item is considered
to be
unresolved
(387/90-80-03
and 388/90-80-03).
The inspection
team identified that references
to procedures
in the
EOPs were inconsistently
employed.
Some actions that operators
would
be expected
to perform without referring to the procedure
referenced
specific procedures,
while other actions that operators
would be
expected to perform with the procedure
in hand did not reference
the
procedure.
These
inconsistencies
did not result in any specific
-- technical
adequacy
problems,
but provide the potential for missed
actions while implementing the
EOPs.
The licensee identified the
inconsistency
in referencing
procedures
prior to the inspection
and
planned to review the
EOPs to correct the problem.
4.4
Technical
Ade uac
of Calculations
The inspection
team identified several
concerns
based
on review of
the technical justification and calculations of the Heat Capacity
Temperature
Limit (HCTL) and Pressure
Suppression
Pressure
(PSP)
curve.
The
HCTL curve during the
ATWS conditions
was determined
based
on
two loops of suppression
pool cooling in service
and assumed
a time
to insert control
rods
by normal
manual insertion.
The inspectors
questioned
whether the curve was also appropriate for use with only
one loop of suppression
pool cooling in service.
In addition the
inspectors
were concerned that the curve was based
on insertion of
control rods by normal
methods.
If control
rods or boron injection
is delayed,
the actions identified in the
EOPs to reduce
pressure
may
not be sufficient.
In that case,
further reduction of RPV water
level to the top of active fuel
may be appropriate
to further reduce
reactor
power and the resultant
energy reduction into the suppression
pool.
There was
no documented
basis for the lower curve,
5 psig below the
PSP curve, at which suppression
pool sprays is directed in E0-103.
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5.0
Control
Room and Plant Walkdowns
The inspectors
walked down the
and procedures
referenced
therein to
confirm that the procedures
can
be implemented.
The purpose of the walk-
downs was to verify that instruments
and controls required to be used to
implement the procedures
are consistent with the installed plant equip-
ment;
ensure that the indicators, controls
and annunciators
referenced
in
the procedures
are available to the operator;
and ensure that tasks
can
be accomplished.
The walkdowns of the
EOPs in the plant concluded that the
can
be
performed.
Detailed
comments
are identified in Attachment
C.
Notwith-
standing
the comments,
the operators
can accomplish
the
EOPs with reliance
on their knowledge
and training.
Pending
licensee
actions to resolve
the
detailed walkdown comments, this item is considered
to be unresolved
(387/90-80-04
and 388/90-80-04).
A concern identified by the inspection
team is the method in which normal
operating procedures
and abnormal
procedures
are
used for performance of
EOP required tasks.
The majority of the tasks directed
by the
require
use of one or more procedure that are written for a purpose other
than performance of the desired
task.
As a'esult, it is sometimes diffi-
cult to locate the appropriate
section of the procedure,
numerous
proce-
--dural actions
would be unnecessary
during emergency conditions,
and it is
not clear whether
some specified actions
should
be performed considering
the degraded
conditions that would be present
when the task was performed.
For example,
the directions for venting primary containment to reduce
pressure
at:
1) any time when performing Primary Containment
Pressure
Control (PC/P),
and 2) to prevent containment failure regardless
of off-
site dose limitations at primary containment
design limits are both
contained in the
same off-normal procedure
(ON) for loss of Reactor
Building Chilled Water.
The Primary Containment Control
EOP does not
specify the section to be performed for either case
and the
ON does not
have
a table of contents in the beginning of the procedure.
The
same
section of the
ON is used for reducing containment
pressure
with or
without impending containment failure.
This section of the
ON references
normal operating
procedures
(OPs) for sampling containment
and actual
performance of the venting.
The
OP that is referenced for venting does
contain
a table of contents,
but the section that must be used for venting
is labeled "Primary Containment Nitrogen Makeup and Pressure
Control."
This section of the
OP contains
numerous prerequisites
and precautions
that are applicable only during normal operations.
Reduction of contain-
ment pressure
is addressed
in three sub-sections
of the designated
section
of the OP.
These sub-sections
then reference
another
OP for operation of
the Standby
Gas
system
(SGTS).
As
a result,
the operator
who is directed
to vent the containment
must make
numerous decisions
as to which procedure
sections
must
be performed
and which procedure
steps
are applicable.
This
process
could result in performance of unnecessary
actions
and interrupt-
ion of the
SRO for guidance, all leading.to potential
delays
and operator
errors in performing the assigned
task.
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Only the
ES procedures
were walked-down step
by step during the facility's
initial validation of the
EOPs.
The initial validation process
did not
identify the deficiencies
in the use of numerous
support procedures
because
of the failure to walk-down the
EOs,
ONs,
and
OPs that support the
EOPs.
6.0
Simulator
Six scenarios
were conducted
on the plant specific simulator by two shift
crews.
The simulator scenarios
provided information on real time activi-
ties.
The purposes
of these
exercises
were to determine that the
provide operators
with sufficient guidance
such that their responsibili-
ties
and required actions during emergencies
both individually and
as
a
team are clearly outlined; verify that the procedures
do not cause
opera-
tors to physically interfere with each other while performing the
EOPs;
and verify that the procedures
do not duplicate operator actions
unless
required (i.e.,
independent verification).
In addition,
when
a transition
from one
EOP to another
EOP or other procedure
is required,
precautions
are taken to ensure that all necessary
steps,
prerequisites,
and initial
conditions are met or completed
and that the operators
are
knowledgeable
about where to enter
and exit the procedure.
The simulator exercises
demonstrated
that the operators
can effectively
-utilize the
EOPs to respond to plant accidents.
The simulator exercises
and follow-up discussions
with the operators
confirmed many of the items
that were previously identified in the
human factor and technical
reviews.
Most items identified related to confusing
EOP steps
and level/power
control issues.
When implementing
E0-103,
Primary Containment Control, the
SROs are
slow
to direct initiation of suppression
pool cooling and bypassing
drywell
cooling logic isolations to allow restoration of drywell cooling for
containment
pressure control.
In follow-up discussions,
the
SROs stated
that they would perform ON-159(259)-002 to verify isolations prior to
bypassing drywell cooling logic isolations.
The bases for EO-101 state
the ON-159(259)-002
should
be performed
as time permits to verify isola-
tions.
The bases
for EO-103 do not address
ON-159(259)-002.
Bypassing drywell cooling logic isolations is a time consuming task and
it did not appear that there
was adequate justification for delaying
direction of that task to verify isolations in accordance
with an off-
normal procedure.
7.0
Human Factors
Review of the
As a result of the
human factors review of the
EOPs,
several
concerns
have
been generated.
A desk top review of the
was conducted prior to the
on-site inspection.
Observation of simulator exercises,
interviews with
SSES staff, plant walk downs,
and control
room tours were used to both
corroborate
those
items noted during the desk top review and to identify
additional
concerns.
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Generally,
the
EOPs are high quality with an appropriate
level of detail
and
a clearly designed
format.
The flow charts
are laminated to a semi-
rigid plastic material
which gave
them strength
and durability.
The
EOP text is legible under all conditions for which they will be used.
However, the text used for "Yes" and "No" answers
to decisions is smaller
than the other text and may not be legible under certain conditions (i.e.,
degraded lighting).
The supporting
procedures
(ES,
OP,
and
ON) are
readily available in the control
room and are well maintained.
Operator acceptance
of the fl'ow chart format is very high.
From a
human
factors standpoint,
operators
used the.flowcharts
very well in the simu-
lator scenarios.
There were
no problems with operators
physically handl-
ing the flowcharts or finding steps
on the flowcharts.
In this
same
regard,
the place
keeping aids provided by the flow charts is adequate.
It was noted that
a
common convention for operator
placekeeping
on the
flowchart does
not exist;
however,
no decrement
in human performance
was
observed during the simulator scenarios.
The
human factors concerns with the
stem primarily from the incon-
sistencies'in
the implementation of 'the direction from the
EOP. writers
guide (AD-gA-330) or lack of direction for formatting numerous
steps.
Also, numerous
action verbs are not defined in the procedures writers
-guide.
When action verbs are defined in the writers guide, the action
verbs
used
on the flow charts
are not always
used in
a manner consistent
with the definitions in the writers guide.
The numerous
inconsistencies
suggest that the
human factors verification of the
was less
than
adequate.
Although the inconsistencies
did not cause
an obvious decrement
in human performance
in the simulator exercises,
in real
emergencies
inconsistencies
may impact the
use of the
EOPs.
Another concern in the
EOPs is the manner in which the operators
are
directed to various other
EOPs or supporting
procedures
(ES,
OP,
and ON).
In most cases
during the simulator scenarios,
the operators
handled the
transition from one procedure
to another without much difficulty.
How-
ever, in some flowchart procedures
the operator is directed to an
ES,
ON,
or OP procedure
and then to another
ON or OP procedure.
The
EOPs utilized
four types of transition formats,
but the
EOP writers guide only discussed
two formats.
A summary of concerns is listed below.
Attachment
D contains detailed
examples of the concerns.
Pending
licensee
actions
on the
human factor
concerns,
this is considered to be unresolved
(387/90-80-05
and 388/90-
80-05).
7.1
Verification of EOPs from a
Human Factors
Pers ective
In numerous
instances,
the
do not follow the direction of the
EOP writers guide.
The result of this is
a lack of consistency
both
within and
among the procedures.
For example, if an operator
expects
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a right exit from a decision
diamond to always
be
a "Yes" on
a
certain flow path
and it is not, then the operator
may perform
actions which might cause
the plant condition to get worse.
Human
factors verification of the
EOPs is expected to identify
inconsistencies
in the procedures.
7.2
Actions Verbs
Action verbs
used in the procedures
are not always defined in either
the
EOP writers guide (AD-gA-330) or the procedures
writers guide
(OI-AD-055).
The use of action verbs in the procedures
is not always.
consistent with the definitions given in the writers guides.
This
leaves
the interpretation of the action verb up to the individual
operator,
which has
a major effect on the actions
they take.
7.3
Cautions
and Notes
Cautions
are
used to describe
hazardous
conditions that can
cause
injury and equipment
damage
and should describe
the consequence
of
the hazard.
Notes are intended to provide supplemental
information
to the operator.
Neither cautions
nor notes
should contain operator
actions.
Because
of the critical nature of the information contained
in cautions, it is particularly important that cautions
be emphasized
- in a way that distinguishes
them from notes
and that they be located
where operators will not overlook them.
Direction for properly placing cautions is contained
in the writers
guide, but is not always followed in the flow charts..
In the current
, revision of the flow charts cautions
and notes
are placed together
and appear at various locations
on the flow chart.
Cautions
do not
always appear before the step to which they pertain.
7.4
Writers Guide
The
EOP writers guide does not contain direction
on
how to format
many types of steps.
This lack of direction caused
inconsistency
in
the writing of EOPs.
7.5
Transitions
Although the information in this section pertains
to the
EOP writers
guide,
the importance of this information warrants its own section.
The
EOP writers guide provides
two methods of transitions
between
the
various types of procedures.
These
are
a concurrent
type of transi-
tion (concurrent exit) and exit.
Concurrent exit means to continue
with the actions required in the current procedure
and also perform
the actions in the referenced
procedure.
Exit means to leave the
current procedure
and
go to
a step in the referenced
procedure
or
another
step in the
same
procedure.
However,
two other
types of
transitions
are
used in the flow charts that are not addressed
in the
writers guide.
These
appear
as
"IAW" (in accordance
with) and
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7.6
"perform" statements
on the flow charts.
The types of transitions in
flow charts
should
be consistent
and minimized in order to provide
clear consistent
operator direction.
The operator
should
have clear directions
as to the steps
they need
to perform.
The
IAW transition
assumes
the operator
understands
which steps
are important and which are not.
This may not always
be
the case in an emergency situation
and unnecessary
steps
may be
performed or critical steps
may be missed.
The steps
necessary
to
perform the task should
be clearly indicated in the procedure.
In
this regard,
and supporting
procedures" should avoid sending the
operators
into numerous other procedures
and clearly state
the speci-
fic procedure
reference
where the operator
should transition.
If the
entire procedure is to be performed,
then
a reference
to the entire
procedure
is appropriate.
If only a portion of the referenced
proce-
dure is to performed,
then the transition should clearly state
the
portion of the procedure to be performed.
The operator
should tran-
. sition into as
few procedures
as possible.
Ste
and Table Wordin
7.7
Several
steps
in the
and
ES procedures
were worded in a confusing
manner.
Examples
are provided in Attachment
D.
Human Factors
Involvement in Procedure
Develo ment and On-Goin
Evaluation
8.0
On-
Experience
has
shown that
a team effort should
be used in the
development
and on-going evaluation/upgrading
of EOPs
(NUREG-1358).
This team should include
a
human factors specialist.
The
human
factor specialist
involvement in the development of EOPs
was limited
to the original validation of the
and was not included in the
development
and writing of the
EOPs.
It is apparent
from documentation
provided by the facility (verifi-
cation checklists
and personal
interviews) that the
human factors
professional
was not involved in the verification of the flow charts
and has not been involved in the continuing evaluation of the
EOPs.
does plan to have
human factors involved in the future upgrade
of the
EOPs to implement revision
4 of the
oin
Evaluation of EOPs
The
NRC team inspected
the ongoing evaluation
program for the
EOPs.
The
licensee
had recently developed
a program to evaluate
the
on
a
regular basis.
OI-AD-071, EOP/EPG
Open Items Tracking,
was written to
identify and track open items, deficiencies
and enhancements
for the
and the
EPGs identified outside of the validation and verification
program.
1
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i
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18
The inspectors
questioned
the adequacy of the licensee's
prioritization
of EOP open items.
The licensee
had identified numerous
open
items prior
to the inspection
and
had prioritized them based
on criteria defined in
OI-AD-071.
The majority of the items were designated
as Priority 2 items
because
they were based
on differences
between
the
EPG and
EOPs.
It
did not appear that
a thorough evaluation
was performed
when items were
identified to ensure that they did not have potential
adverse effect on
procedure
implementation or create
adverse
consequences
not previously
evaluated
(which would meet the criteria for Priority 1 designation).
For
example,
the licensee
had identified two open items associated
with the
discrepancies
in the Reactor
Power Control leg of RPV Control concerning
the definition of "reactor shutdown"
and the required actions
when reactor
power is below 5%.
These
items were designated
as Priority 2 items,
because
they were differences
between
the
and the
EOPs.
A
thorough review was not performed to determine
the extent of the impact of
these
items
on procedure
implementation.
9.
99
The
NRC team inspected
the
QA organization
involvement in the programmatic
approach of the
EOP program.
The inspection
focused
on those policies,
procedures
and instructions
necessary
to provide
a planned
and periodic
audit of the
EOP development
and implementation
process.
During the development
and implementation of Revision
0 of the
EOPs in
1985, the
QA Department
was not
a participant.
Since revision
0 of the
was issued,
the
QA Department
has
conducted periodic audits of the
EOPs with a focus
on ensuring that subsequent
revisions
were correctly
incorporated into the
EOPs.
The
QA Department is prepared to be
an active participant in the major
revision process that will incorporate revision
4 the
BWR Owner's
Group
EPGs.
The
QA Department
expects to focus primarily on ensuring that the
EPG revisions are correctly incorporated in the
EOPs.
The
QA Department
plans to use technically knowledgeable
personnel
to support their effort
in this process,
and all aspects
of the revision process
can
be covered.
10.0 Unresolved
Items
Unresolved
items are matters
about which more information is required to
ascertain
whether they are acceptable
items,
items of noncompliance
of
deviations.
Unresolved
items identified during the inspection
are
discussed
in sections
4.0, 5.0 and 7.0.
11.0
Re uglification Examinations
Dynamic simulator requalification re-examinations
were administered
to two
reactor operators
(ROs) who had failed this portion of the requalification
examination
administered
during the week of January
22,
1990,
The exami-
nations
were administered
using the guidelines described
in
19
"Operator
Licensing Examiner Standard,"
Rev.
5, section
"Admini-
stration of NRC Requalification
Program Evaluations."
The facility submitted
proposed
scenarios
to be used for the examinations.
The
NRC reviewed the scenarios
and selected
two to be used for the exami-
nations.
These
scenarios
were run in advance
on the plant specific simu-
lator.
Facility personnel
that participated
in the preparation
of the
examination
signed security agreements
to ensure
there
was
no compromise
of the examinations.
Both operators
passed
the examinations.
The facility licensee
was effect-
ive in remediating
the operators with respect
to their previous
examina-
tion results.
Since only two operators
were examined, this review did not
constitute
a program evaluation
and
no generic strengths
or weaknesses
were noted.
12.0 Exit Interview
At the conclusion of the inspection
on April 27,
1990,
an exit meeting
was
conducted with those
persons
indicated in paragraph
2.
The inspection
scope
and findings were
summarized.
The licensee did not identify as
proprietary
any of the materials
provided to or reviewed
by the inspect-
ors during the inspection.
The licensee
actions to respond to the inspection findings are
summarized
as follows.
The licensee
took immediate actions to inform the operators
'egarding
the uncertain availability of the suppression
chamber
pressure
indication
and provided additional
guidance
on
how to respond if the
suppression
chamber
pressure
indication is not available.
By May 11,
1990,
the licensee
was expected
to complete analysis
and use of drywell
pressure,
or other alternate
indication, instead of suppression
chamber
pressure
for EOP implementation.
By May 18,
1990, the licensee
would
implement drywell pressure
in the
EOPs if it was determined to be techni-
cally adequate
and identify a schedule
for other methods if drywell
pressure
cannot
be used.
By June
15,
1990,
the licensee
would develop
a
plan for the resolution of the inspection findings.
The inspection
team
found the licensee
actions to be acceptable.
W '4'
4
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'*'
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!
'l
Flowchart
ATTACHMENT A
DOCUMENTS REVIEWED
"EO-100-101
- EO-100-102
"EO-100-102
- EO-100-103
"EO-100-104
- EO-100-105
"EO-100-111
- EO-100-112
"EO-100"113
- EO-100-114
EO-200-101
EO-200-102
EO-200-102
EO-200-103
EO-200-104
EO-200-145
EO-200-111
EO-200"112
EO-200-113
EO"200"114
EOP Bases
EO-100-101
EO-100-102
EO-100-103
EO-100-104
EO-100-105
EO-100-111
EO-100-112
EO-100-113
EO-100-114
EO-200-101
EO-200-102
EO"200" 103
EO-200-104
EO-200-105
EO-200-111
EO-200-112
EO"200-113
EO"200"114
Revision
1 and
2
RPV Control
Sh.
1, Revision
1 and
2
RPV Control
Sh. 2, Revision
2
Primary Containment Control, Revision
1
Secondary
Containment Control, Revision
Radioactivity Release
Control, Revision
Level Restoration,
Revision
1
Rapid Depressurization,
Revision
1
Level/Power Control, Revision
1 and
2
RPV Flooding, Revision
1 and
2
Revision
1
RPV Control
SH 1, Revision
1
RPV Control
SH 2, Revision
1
Primary Containment Control, Revision
1
Secondary
Containment Control, Revision
Radioactivity Release
Control, Revision
Level Restoration,
Revision
1
Rapid Depressurization,
Revision
1
Level/Power Control, Revision
1
RPV Flooding, Revision
1
Revision
2
RPV Control, Revision
2
Primary Containment Control, Revision
2
Secondary
Containment Control, Revision
Radioactivity Release
Control, Revision
Level Restoration,
Revision
2
Rapid Depressurization,
Revision
2
Level/Power Control, Revision
2
RPV Flooding, Revision
2
Revision
1
RPV Control, Revision
1
Primary Containment Control, Revision
1
Secondary
Containment Control, Revision
Radioactivity Release
Control, Revision
Level Restoration,
Revision
1
Rapid Depressurization,
Revision
1
Level/Power Control, Revision
1
RPV Flooding, Revision
1
and 2.
1 and
2
1 and
2
1
1
< ~
i ~
i
q -,
r
Emer enc
Su
ort
and Related
Procedures
ES" 134-003
- ES-149-001
- ES-150"002
- ES-155-001
ES" 156-001
- ES-184-001
ES-249"001
"ES"070-001
"EO-100-030
"EO-100-032
"ON-134-001
"ON-155-007
- ON-159-002
- EO-200-032
"OP-070-001
"OP-173-001
"OP-218-001
- OP-225-001
"OP-234-001
Bypassing
Drywell Cooling Logic Isolations,
Rev
2 with PCAF
Bypassing
Drywell Cooling Logic Isolations during
a
LOOP,
Rev
2
Re-establishing
Rx Building HVAC, Rev 2
Overriding
pump initiations,
Rev 2
RCIC Turbine Isolation and Trip Bypass,
Rev
2
Boron Injection Using
RCIC System,
Rev
3
HPCI Turbine Isolation, Trip and Initiation Bypass,
Rev
3
HPCI Suction Auto Transfer Bypass,
Rev
1
Vent
CRD to Insert Control
Rods,
Rev
1
Bypassing
Rod Blocks,
Rev
1
Bypassing
MSIV Isolations,
Rev
3
Bypassing
Drywell Cooling Logic Isolations,
Rev
2 with PCAF
Re-establishing
Rx Building HVAC, Rev
2
Overriding
pump initiations,
Rev
4
RCIC Turbine Isolation and Trip Bypass,
Rev
2
Boron Injection Using
RCIC System,
Rev 4
HPCI Turbine Isolation, Trip and Initiation Bypass,
Rev
3
HPCI Suction Auto Transfer Bypass,
Rev
2
Vent
CRD to Insert Control
Rods,
Rev
2
Bypassing
Rod Blocks,
Rev
1
Bypassing
MSIV Isolations,
Rev
3
Manual Initiation of SBGTS in Automatic Control,
Rev
2
Fire Water Injection, Revision
7
Operation of HPCI with High Suppression
Pool Temperature
Loss of RBCCW (Vent Drywell and Suppression
Chamber),
Rev 8
Cross connect
CRD from Unit, Rev
7
Restore
Containment
Instrument
Gas,
Rev
12
HPCI System Operating Guidelines During Station Blackout,
section 2.3
Standby
Gas Treatment
System
Containment
Atmosphere Control System,
sections
3.5 and
3 '
Instrument Air System,
section
3.1
Containment
Instrument
Gas System,
section 3.2
Reactor Building Chilled Water System,
section
3. 1
Administrative Controls
AD-gA-330 Symptom - Oriented
EOP Writers Guide,
Rev 4
AD-gA-331 Verification Program for SSES-EPG
and
Symptom
Oriented
AD-gA-332 Validation Program for Symptom - Oriented
OI-AD-055 Procedures
Writer's Guide, Revision
4
OI-AD-071 EOP/EPG
Open Items Tracking,
Rev
0
Procedures
Generation
Package
Volume
1 and
2 dated
March 1984
EOP Trainin
Material
PP002A
EOP Simulator Scenarios,
Rev
2
SM001C Training Plan Event Based
EOPs,
Rev
0
I
I
I
I
'
'I
'J
'W 'PA
<<
I
A
5'f
~
p'
ewart, ~~ no
s
r
w
r eery
EOP Trainin
Material
Cont'd.
SY015F-9 Training Plan
Emergency Support Procedures
Ot~er tvte
EPG and source
documents
contained therein,
Revision
1
Calculations
Reviewed
EO-104 Max normal
and
max safe temperatures
EO-103 Pressure
Suppression
Pressure
Curve
SLC tank levels vs boron weight
EO-103 Drywell spray initiation limit curve
EO-103 Heat capacity temperature limit curve
- Denotes those
procedures
walked down
ht
p 1 %'7
4 4't
J
$
'h
4
~ ) "t f
'F 4
V,',NWt71
4
tO
-%9j
1 t
I, t'th
ATTACHMENT B
DETAILED TECHNICAL ADE UACY COMMENTS
1.
and
A.
RPV Control
Reactor
Water Level Entr
Condition
The
EPG justification for lowering the reactor water level entry
condition from the
scram setpoint (+13") to -38" is not technically
adequate.
The
EPG justification for this difference is to
prevent
an unwarranted
entry into the
RPV Control Guideline.
No
technical justification for the difference is documented.
Addition-
ally, the
EPG indicates that entry into E0-101,
on
a low
water level
scram ensures
that all
EPG required actions are
performed.
The review of the
EOPs indicated
two procedural
actions
(monitoring
RPV water level
and ensuring isolations
and
actuations)
that are not adequately
addressed
by EO-101
and E0-102.
B.
Primar
Containment
Control
Su
ression
Pool
Tem erature
Entr
Condition
The
EPG justification for raising the suppression
pool temper-
ature guideline from 90 degrees
F to 105 degrees
F is not technically
adequate.
Entry into Primary Containment
Control at
105 degrees
F
conflicts with the actions of the Suppression
Pool Temperature
Control leg (SP/T) which require initiation of suppression
pool
cooling at
90 degrees
F,
The
SSES justification for reducing the
operator
response
time addresses
one specific event (inadvertent
opening of a safety relief valve).
This is not adequate justifica-
tion because
the
EOPs are designed
to address
symptoms not specific
events'.
Secondar
Containment Control Secondar
Containment Differential
Pressure
Entr
Condition
D,
The
EPG justification for changing the secondary
containment
differential pressure
entry condition is not technically adequate.
The
EPG justifies altering the entry condition by a percent
change to the Technical Specification value.
This does not provide
adequate justification for including
a time criteria for the entry
condition.
l
Secondar
Containment Control
HVAC Exhaust Radiation
Level Entr
Condition
The
EPG justification for not including Zone I and Zone II
HVAC radiation levels
as entry conditions for Secondary
Containment
~
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~ "g""i * g \\
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Vl'
V7 t I+ ~
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Control is not technically adequate.
The fact that these
systems
do
not isolate
on high radiation levels is not adequate justification
for not requiring entry into Secondary
Containment Control if high
radiation levels are detected
in the reactor building exhaust
vents
by the Split Particulate
Iodine and Noble Gas
(SPING) monitors.
High
release
rates detected
by the
SPING monitors would be indicative of
secondary
containment
problems.
Requiring entry into Secondary
Containment Control
when
Zone I or Zone II HVAC is not in service for
an extended
period time is not an equivalent substitution for exhaust
radiation level entry conditions.
E.
Secondar
Containment Control Area Radiation
Level Entr
Condition
The
EPG justification for selecting
ten times the alarm value
as the
maximum normal operating radiation level is not technically
adequate.
The justification to allow operators
to use alarm response
and off-normal procedures
prior to entering the
EOP is not technic-
ally adequate.
Allowing sufficient margin to the
maximum safe
operating radiation level is not adequate justification for delaying
entry into the
EOP.
There is no apparent correlation
between
ten
times the alarm and the normal operating radiation levels specified
in the Final Safety Analysis Report.
(The
FSAR was used to determine
~
the maximum safe operating radiation levels.)
F.
Secondar
Containment Control
Sum
and Area Water Level Entr
Conditions
and Secondar
Containment
Water Level Control Guidelines
The
EPG justification for deleting the floor drain
and area
water level entry conditions into Secondary
Containment
Control
and
the secondary
containment water level control guidelines is not
technically adequate.
The fact that there is no area water level
indication available is not adequate justification for these differ-
ences.
Local indication of water level
can
be utilized.
Addition-
ally, the off-normal procedures
referred to in the
EPG justifi-
cation
do not address all the
containment
water level control
and do not direct the operator to enter
E0-104,
Secondary
Containment Control.
G.
RPV Control
Reactor
Power
Control
Removin
Fuses
to De-ener ize
Scram Solenoids
RC/ -5. 1
The
EPG justification for not removing fuses to de-energize
the
scram solenoids is based
on
SSES policy that prohibits operators
from removing fuses during
an emergency.
Actions to open the break-
ers to de-energize
the
scram solenoids
were originally substituted
for pulling fuses.
These actions
were subsequently
deleted.
The
EPG justification for deletion of the direction to open the
breakers
to de-energize
the
scram solenoids
does not indicate that
the direction to pull fuses
should
be deleted for the
same
reasons
(to prevent closure of the MSIVs).
The justification for not remov-
ing fuses is not technically adequate.
2.
Com arison of SSES
and
A.
Cautions
Caution ¹14
EOP steps that include this caution for depressurization
without
motor driven pumps available
are not consistent with the guide-
lines in the
EPGs.
The
EPGs caution that the
should not be depressurized
below 104 psig unless
motor driven
pumps are available.
The
EOPs caution against depressurization
below 150 psig.
There is no documented justification for this
deviation.
2.
Caution ¹26
Caution
9 in the
EOPs is not consistent with Caution ¹26 of the
EPGs.
Caution
9 alerts the operator to the potential for
water level
and pressure
when
RPV water level i'
<-90".
Caution ¹26 cautions
the operator
about reactor
power
osci llations, but does
not specify
a level at which oscillations
are expected
to occur.
At the time of the inspection,
the
licensee
was performing
an analysis
to determine if -90" is the
limit for anticipated
power oscillations.
B.
RPV Control - Reactor
Power Control
Reactor
Power
< 5/. With More Than
One Control
Rod Not Inserted
The Reactor
Power
Control leg (RC/Q) of RPV Control of the
does not preserve
the logic of the
EPGs for reactor
power
control.
Step
RC/Q-2 of EO-102 is an awareness
decision
step
which provides direction to exit RC/Q when power is <
SFo
~
The
logic of the
EPGs requires
the actions of the
RC/Q leg to
be performed until-all but one control rods are inserted to
position
00 or the reactor is shutdown
and
no boron
has
been
injected.
These conditions
do not correspond to
SX reactor
power.
EO-102 does not direct insertion of control rods if
reactor
power is <55.
Additionally, because
step
RC/Q-2 is an
awareness
step that is applicable while performing the entire
RC/Q leg it provides conflicting direction with steps
RC/Q-13,
which directs that boron
be injected until the
SLC tank level is
<100 gallons or all but one control
rods are inserted,
and
RC/Q-17, which directs
rod insertion until all but one control
rods are inserted.
(The discrepancy
between
5% power and all
but one control rod inserted
was identified by the licensee
prior to the inspection).
~ ~
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Initiation of ARI
E0-102,
step
RC/Q-4 directs initiation of ARI.
This action is
not included in the
EPGs.
EO-102 does
not provide direct-
ion to reset
ARI prior to manual insertion of control rods.
Control rods cannot
be manually inserted
unless
ARI is reset.
The operating
procedure for resetting
a scram directs reset of
ARI, but the operators
are not required to refer to this proce-
dure during emergency
conditions
and, therefore,
could miss the
direction for resetting
ARI.
Boron Injection Usin
Reactor Water Cleanu
EPG,
step
RC/Q-4 directs
use of the Reactor Water Cleanup
(RWCU) system to inject boron.
The
do not address
this action.
Maximizin
CRD Flow
EO-102 provides direction for maximizing
CRD flow to insert
control rods (steps
RC/Q-14,
RC/Q-15 and RC/Q-16).
These
actions
are not included in the
EPGs.
(This item was
identified by the licensee prior to the inspection.)
Restoration
of S stems
Followin
E0-102,
step
RC/Q-20 is not consistent with SSES
EPG,
step
5. 1
for restoring
systems
to normal after venting of the
scram air
EPG,
step 5.1 directs restoration
"when control
rods are not moving inward."
E0-102,
step
RC/Q-20 directs
restoration
when "inward rod motion stops," which implies that
the systems
should
be returned to normal only if rod motion
occurs.
If no rod motion occurred
and the
remained
vented,
manual
insertion of control rods would not be possible.
The bases
for E0-102,
step
RC/Q-20 indicate that restoration
should
be performed
when rod motion stops or if no rod motion
occurred.
Reset of Scr'am With More Than
One Control
Rod Not Inserted
EO"102 is not consistent with SSES
EPG,
step 5.5 for resetting
the scram while attempting to insert control rods.
EPG,
step
5 '
directs reset of the
scram only if control rods
moved
inward following the last scram.
EO-102 directs reset of the
when possible
regardless
of rod movement.
E0-102,
steps
RC/Q-22 and
RC/Q-34 are both awareness
steps that provide
direction if the
can
be reset while attempting to insert
,These
steps
could cause
confusion
when implement-
ing.the
EOPs resulting in failure to reset
the scram in accord-
ance with step
RQ-21.
Additionally; EO-102 does not ensure that
the
valve is closed prior to manually
inserting control
rods in accordance
with step
RC/Q-33.
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C.
RPV Control
Reactor
Level Control
Entr
into Level Restoration
2.
E0-102,
step
RC/L-5 which directs entry into Level Restoration
. if RPV level cannot
be maintained
above -129" is not consistent
with SSES
EPG,
step
RC/L-2 which specifies entry into Level
Restoration if level cannot
be maintained
above -161".
There is
no documented justification for this inconsistency.
(This item
was identified by the licensee prior to the inspection.)
Cold Shutdown
D.
EPG,
step
RC/L-3 provides direction to proceed
to cold
shutdown in accordance
with GO-100-005.
.EO-101 directs cold
shutdown in accordance
with GO-100-011.
GO-100-005
does
not
provide directions for placing the plant in cold shutdown.
Control
Reactor Pressure
Control
Pressure
Control Usin
2.
EPG,
step
RC/P-2 directs that the control switches for each
"OFF" position to assure
that the
valves will not be opened
except for rapid depressurization
or
by the safety
mode of operation.
This direction is not contained
in the Pressure
Control leg (RC/P) of E0-102.
Pressure
Control Usin
Reactor
Water Cleanu
3.
E0-012,
step
RC/P-8 does not indicate
any restriction for using
(RWCU) for pressure
reduction.
This is
not consistent with SSES
EPG,
step
RC/P-2 which specifies
use of
has
been injected.
Additionally, no
procedure exists for operation of
RWCU in blowdown mode
as
specified in these
steps.
Pressure
Control Usin
Deaeratin
Steam
EPG, step
RC/P-2 directs
use of Main Condenser
Deaerating
Steam for pressure
control.
This method is not addressed
in
E0-102,
RC/P.
(This item was identified by the licensee prior
to the inspection.)
Pressure
Reduction
The Pressure
Control leg (RC/P) of EO-102 does not include
an
override to address
pressure
reduction if required to maintain
conditions below the Heat Capacity Temperature
Limit or the
Suppression
Pool
Load Limit as indicated in the
EPGs.
VHK't)hl'hl'\\'Wt
1 ~ W'*E'4
t PTpt
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0 / % t NA
5
P ~ h yl I
8 fl
E0-103,
steps
SP/T-13
and SP/L-19 direct pressure
reduction
and
entry into EO-102 at step
RC-1.
Without an override,
the
direction in E0-102,
RC/P for pressure
control conflicts with
the direction in E0-103.
5.
B
assin
MSIV Isolations
provides instructions for bypassing
the
steam tunnel
high temperature
and low condenser
vacuum
MSIV closure signals
in addition to the low level closure signal.
EPG,
section
PC/P-1 only addresses
bypassing
the low level
MSIV closure.
No
justification is provided for bypassing
the additional isola-
tions.
6.
RPV Cooldown
E0-102,
step
RC/P-10 is
a decision
step which asks if RPV cool-
down is required.
There is no justification for this decision
step in the
EPGs.
The
do not provide specific guid-
ance
on when cooldown is "required."
This step
appears
to be
unnecessary
because
the
EPGs "require" cooldown whenever
an emergency condition exists
and
no other conditions dictate
maintaining the
RPV pressurized.
If no emergency condition
exists,
EO-102 can
be exited without performing
a reactor
cooldown.
E.
Primar
Containment Control
Su
ression
Pool
Tem erature
Control
Monitorin
Su
ression
Pool
Tem erature
2.
The bases
for E0-103,
step
SP/T-1 are not consistent with the
. SSES
EPGs.
EPG, section
SP/T requires
use of SPOTMOS to
determine
suppression
pool average
temperature.
The bases for
E0-103,
step
SP/T-1 allow use of the process
computer to deter-
mine suppression
pool temperature
under certain conditions.
Use
of the process
computer is not justified in the
EPGs.
Initiation of Su
ression
Pool Coolin
The direction for initiation of suppression
pool cooling in step
SP/T-3 of EO-103 is not consistent with the direction in SSES
EPG,
step SP/T-3.
The
EPGs direct operation of available
suppression
pool cooling.
E0-103,
step
SP/T-3 does not indicate
that all available
suppression
pool cooling should
be operated.
Licensee policy is to only operate
one loop of suppression
pool
cooling due to water
hammer considerations.
This policy is not
addressed
in the
t
'
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1 & IW WW 0
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'p'lt
3.
4.
The directions for a reactor
scram in the Suppression
Pool
Temperature
Control leg (SP/T) of EO-103 do not preserve
the
logic of the
EPGs.
Step SP/T-7 of EO-103 directs
a manual
scram if suppression
pool temperature
"cannot
be maintained"
below 110 degrees
F, while SSES
EPG step
SP/T-3 directs
a manual
scram "before" suppression
pool temperature
reaches
110
degrees
F.
These directions
do not have the
same
meaning
when
implementing
EOPs.
"Cannot
be maintained" requires
an evalu-
ation of system
performance
in relation to parameter
trends to
make
a determination.
Based
on operator
judgement
the action
may
be taken before or after the designated
condition is met.
"Before" requires that the action
be performed prior to meeting
.
the specified condition.
Cautions
E0-103,
steps
SP/T-3
and SP/T-10 contain cautions that should
be applicable while performing all subsequent
steps of SP/T.
By including these
cautions
as action steps, it is not apparent
that the cautions
are applicable for all subsequent
steps.
Primar
Containment Control
Su
ression
Pool
Level Control
Actions Not Included in SSES
2.
E0-103,
steps
SP/L-24 and SP/L-27 direct suppression
pool level
control actions if RPV pressure
is below 200 psig
and termina-
tion of suppression
pool sprays.
These actions
are not included
in the
EPGs.
(These
items were identified by the licensee
prior to the inspection.)
Also, Table
PC-1 of EO-103 which
specifies
the preferred
SRVs to be used for rapid depressuriza-
tion with high suppression
pool water level is not addressed
in
the
EPGs.
(Justification for these
steps
and table are
contained
in the Primary Containment Control Bases.)
Termination of RPV Makeu
From External
Sources with Ade uate
Core Coolin
Assured
The direction to terminate injection sources
external
to primary
containment if suppression
pool level
and
RPV pressure
cannot
be
maintained
below the Suppression
Pool
Load Limit (contained
in
step SP/L-3.1 of the
was deleted
from step SP/L-3. 1
of the
EPGs.
The justification for deletion of this
direction was based
on performing steps
SP/L-3. 1 and SP/L-3.2
concurrently.
The Suppression
Pool
Level leg of EO-103 does not
preserve
the logic of the
EPGs for concurrent
performance
of steps
SP/L-3.1
and SP/L-3.2 of the
EPGs.
E0-103,
step
SP/L-21 directs termination of injection sources
external to
g
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w~ '+ 'p
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"'4 g1P'
0>>'I'~W)'%
irregardless if RPV pressure
reduction
was
successful
in maintaining conditions below the Suppression
Pool
Load Limit.
This direction could result in injection sources
being secured
unnecessarily.
G.
Primar
Containment
Control - Primar
Containment
Pressure
Control
Actions Not Included in SSES
2.
E0-103,
step
PC/P-4 directs actions for hydrogen control follow-
ing a loss of coolant accident
(LOCA).
E0-103,
step
PC/P-6
provides direction for termination of primary containment
pressure
reduction.
E0-103,
step
PC/P-7 provides direction for
monitoring suppression
chamber pressure
above
3 psig.
These
actions are not included in the
EPGs.
(These
items were
identified by the licensee prior to the inspection.)
Reduction of Primar
Containment
Pressure
The procedures
referenced
in E0-103,
steps
PC/P-3
and PC/P-5 for
reduction of primary containment
pressure
are not consistent
with the procedures
referenced
by the
EPGs.
EO-103 refer-
ences
OP-173-001
and
RPV Control which are not referred to in
EPG,
step
PL'/P-1.
EPG,
step
PC/P-1 refers to ES-034-
002 which is not referenced
in E0-103.
3.
Pressure
Su
ression
Pressure
The
and
EO-103 bases
refer to Figure
PC-4 of EO-103
as the Pressure
Suppression
Pressure
Limit.
The title of Figure
PC-4 is "Suppression
Pool Pressure
Limit."
RPV Floodin
EPG,
step
PC/P-4 requires
RPV flooding concurrent with
initiation of suppression
pool
and drywell sprays if primary
containment
pressure
cannot
be maintained
below the design
limit.
Pressure
Control leg (PC/P) of
EO-103 directs initiation of drywell sprays, if conditions
allow, instead of RPV flooding. If conditions allow initiation
of drywell sprays,
venting of primary containment
would be
required without attempting to reduce
containment
pressure
by
flooding the
RPV.
H.
Primar
Containment Control - Dr well Tem erature
Control
Actions Not Included in SSES
E0-103,
step
DW/T-3 requires
and cooldown of the
RPV if drywell temperature
is >150 degrees
F.
E0-103,
step
~
~
1
i
'L$~
vr<s
q "
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2.
DW/T-5 directs initiation of suppression
pool sprays before
drywell temperature
reaches
320 degrees
F.
These actions
are
not included in the
EPGs.
(The first of the two items was
identified by the licensee prior to the inspection.)
Maximize Dr well Coolin
3.
E0-103,
step
DW/T-2 directs maximizing drywell cooling when
drywell temperature
exceeds
135 degrees
F.
This direction is
not consistent with SSES
EPG,
step
DW/T-1 which specifies
operating all available drywell cooling when drywell temperature
exceeds
150 degrees
F.
This discrepancy
results
in conflicting
direction in EO-103 for drywell temperature
control.
There is
no direction in SSES procedures
'to maximize drywell cooling at
135 degrees
F, unless
Control is entered
on
a parameter
other
than drywell temperature.
RPV Saturation
Tem erature
4 ~
The
and
EO-103 bases refer to Figure
PC-6 of EO-103
as the
RPV Saturation
Temperature
Limit.
The title of Figure
PC-6 is "Drywell Instrumentation
Temperature Limit."
Initiation of Dr well
S ra
s
The direction to initiate drywell sprays
in the Drywell Tempera-
ture Control leg (DW/T) of EO-103 is not consistent with the
guidance in the
EPGs.
DW/T directs initiation of drywell
sprays if drywell temperature
cannot
be maintained
below 320
degrees
F.
EPG,
step
DW/T-3 directs initiation of drywell
sprays before drywell temperature
reaches
340 degrees
F.
I.
Secondar
Containment Control
Hi
h Area
Tem erature
and Hi
h
HVAC Cooler Differential Tem-
erature
Entr
Condi tions
The entry conditions into EO-104
on high area
temperature
and
high
HVAC cooler differential temperature
isolations are not
consistent with the entry conditions specified in the
EPGs.
The entry conditions for EO-104 are stated
as conditions (isola-
tions) rather than
as
symptoms (temperature
and differential
temperature
values)
as specified in the
EPGs.
There is no
documented justification for not including all areas of second-
ary containment rather than just the areas that have high
temperature
isolations.
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2.
Haximum Safe
0 eratin
Radiation
Levels
E0-104,
step
SC/R-5 directs
a reactor
and entry into
Control before
any area radiation level exceeds
ten times maxi-
mum normal level.
EPG,
step
SC/R-2 directs entry into
RPY
Control before
any area radiation level reaches its maximum safe
operating level.
E0-104,
step
SC/R-6 directs rapid depressuri-
zation if more than
one area radiation level exceeds
twenty
times
maximum normal level.
EPG,
step
SC/R-3 directs rapid
depressurization if more than
one area radiation level exceeds
maximum safe operating level.
There is
no correlation
between
the maximum safe operating radiation levels defined in the
and the multiples of maximum normal operating radiation
levels specified in EO-104.
Additionally the values provided in
Table
SC-3 of EO-104 for the alarm and maximum normal radiation
levels in the
HCU areas
are not consistent with the values
in the
EPGs.
3.
Ra id De ressurization
J.
Level
E0-104,
step
RC/R-6 directs rapid depressurization
of the
if more than
one area radiation level
exceeds
twenty times
maximum normal levels
and secondary
containment integrity has
been lost.
This direction is not consistent with SSES
EPG,
step
SC/R-3 which requires
rapid depressurization if more than
one
area
exceeds
maximum safe operating radiation levels.
Including
the condition for secondary
containment integrity to be lost
prior to rapid depressurization
does not preserve
the logic of
the
EPGs.
There is no documented justification for waiting
until secondary
containment integrity has
been lost before
depressurizing
the
RPV.
Restoration
Lineu
of Alternate In 'ection
Subs
stems
E0-111,
step
LR-2 which directs lining up alternate
injection
subsystems
i s not consistent with SSES
EPB,
step Cl-1.
The
EPGs direct lineup of as
many systems
as possible.
E0-111,
step
LR-2 does
not indicate that all available alternate
injection
systems
should
be lined up.
2.
RPV Floodin
EPG, Contingency
1 requires
RPV flooding if RPV water level
. cannot
be determined at any time during the implementation of
the level restoration
guidelines.
E0-111,
step
LR-3 states that
RPV flooding should not be performed if spray cooling or blow-
down cooling are in progress.
This additional condition does
not preserve
the logic of the
EPGs.
There is no documented
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4
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s r v,W;R 'P,
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e
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11
justification for not flooding the
RPV if spray cooling or blow-
down cooling is in progress.
3.
The directions for spray cooling in EO-104 are
based
on having
three
Core Spray (CS)
pumps injecting into the
RPV.
These
directions
are not consistent with the guidelines in the
EPGs which direct actions
based
on
a
CS subsystem
(two
CS pumps)
injecting.
(This inconsistency
was identified by the licensee
prior to the inspection.)
K.
Ra id De ressurization-
2.
E0-112,
step
RD-2 requires
a manual scram prior to depressur-
izing the
RPV.
This action is not included in the
EPGs.
This step appears
to be unnecessary
because
the
always direct
a manual scram prior to entry into EO-112.
The
direction to'cram the
RPV prior to rapid depressurization
is
included in the
EPGs in all cases
except for the reactor
scram directed
by E0-103,
step SP/L-18.
Control of Injection Sources
With More Than
One Control
Rod
Out
The direction in E0-112,
steps
RD-4 and
RD-5 for control of
injection sources
when more than, one control rod is not inserted
is not consistent with the guidance
in the
EPGs.
EPG,
Step C7-2. 1 directs
manual control of already established
injections
and prevention of any
new injections.
E0-112,
step
RD-4 directs prevention of injection from 'ECCS
systems
only.
There is no direction to prevent injection from other sources
such
as
or Condensate
pumps.
RD-4 directs overriding
pumps (preventing injection) before
RD-5 directs control of
already injecting systems.
As a result,
these
steps
do not
clearly indicate that it is not necessary
to inhibit systems
that are already injecting.
E0-112,
step
RD-5 directs
shutdown
of Core Spray
(CS)
pumps if they are not required for adequate
core cooling.
This action is not addressed
in the
EPGs.
(This item was identified by the licensee prior to the inspect-
ion.)
3.
Pressure
Reduction
Usin
Deaeratin
Steam
EPG,
step C2-1.2 directs
use of Main Condenser
Deaerat-
ing Steam for rapid depressurization.
This method is not
addressed
in E0-112,
step
RD-10.
(This item was identified by
the licensee prior to the inspection.)
~ wn ~
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4 4 V~ p,C'5 PVK'8 6.' Tf'"p ae =79 4 5'~l~t
12
L.
Level
Power Control
Cautions
The cautions
associated
with steps
LQ-4, LQ-5, LQ-9 and
LQ-13 of
EO-113 do not correspond
to the cautions specified in the
EPG for these
steps.
E0-113,
step
LQ-9 which directs restora-
tion of RPV water level to normal, contains
a caution that
inhibiting ECCS operation
may be required.
There is no docu-
mented justification for inhibiting ECCS operation
when restor-
ing level to normal.
2.
Control of RPV Water Level
and
RPV Makeu
Flow
E0-113,
steps
LQ-4 and
LQ-5 do not preserve
the logic of the
EPGs,
steps
C7-1 and C7-2.
EPG,
step
C7-1 provides
limits for maintaining
RPV water level
and
RPV makeup flow rate
and states
that the direction for maintaining level takes
prece-
dence over the direction for maintaining
makeup flow.
EO-113
does not provide direction or'limits for maintaining
RPV makeup
flow rate.
In addition,
the
EOP bases
document provides
a
"preferred band" which is not addressed
in the
EOP flowchart and
EPGs.
3.
Ra id De ressurization
EO-113 does not preserve
the logic of the
EPGs with respect
to performing rapid
RPV depressurization.
EO-113 directs rapid
depressurization
only if RPV water level cannot
be maintained
above -161".
The
EPGs direct rapid depressurization if
required regardless
of RPV water level.
There are other condi-
tions (i.e., exceeding
the suppression
pool Heat Capacity
Temp-
erature Limit) that would require rapid depressurization
regard-
less of RPV water level.
II.
~V
Isolation of RHR Steam
Condensin
Pi in
EPG,
step C6-1.2 addresses
closing the
RHR steam condens-
ing isolation valves.
This action is not. addressed
in E0-114,
step
RF-24.
EPG,
step
C6-2 justifies deleting the direct-
ion to close the
RHR steam
condensing
isolation valves
because
they will be closed
when the
HPCI isolation valve is closed.
The
EPGs contain justification for using
HPCI to assure
adequate
core cooling while problems which required
RPV flooding
are corrected (following step C6-1.2), in which case
the
isolation valves would not be closed.
This could result in
failure to isolate
RHR steam
condensing
piping.
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2.
Minimum RPV Floodin
Pressure
E0-114,
steps
RF-8 and
RF-9 are not consistent with SSES
EPG,
steps
C6-3. 1 and C6-3.2 with respect to the Minimum RPV Flooding
Pressure.
The
EPGs specify ill psig as the Minimum RPV
Flooding Pressure,
while Table
RF-2 of EO-104 provides values
based
on the
number of SRVs that are open.
All of the values in
Table
RF-2 are lower than
111 psig.
3.
Minimum Core Floodin
Interval
E0-114,
step
RF-11 is not consistent with SSES
EPG,
step C6-3.4
with respect
to the Minimum Core Flooding Interval.
The E0-114,
step
RF-11 directs injection for at least
one hour, while SSES
EPG,
step C6-3.4 provides
a table of values
based
on the
number
of SRVs that are open.
All of the values
in the
EPGs are
lower than
one hour.
4.
More Than
One Control
Rod Out
The direction for RPV flooding with more than
one control rod
not inserted
in EO-114 is not consistent with the guidelines in
the
EPG, section
C6-1.
EO-114 provides direction for RPV
flooding if HPCI is not operating or
a primary break exists
and
different direction with HPCI operating
and
no primary break.
The directions with HPCI operating
and
no primary break are not
addressed
in the
EPGs.
The
EPGs contain justification
for using
HPCI to assure
adequate
core cooling while problems
which required
RPV flooding are corrected (following step
C6-1.2), but these actions
are not reflected in the steps
specified in section
C6-1 of the
EPGs.
Additionally,
EO-114 does not provide direction to reduce injection as speci-
fied in SSES
EPG,
step C6-1.1
~
N.
EPG Format
The format of the
EPG makes it difficult to utilize as
a plant
specific technical
basis
(PSTG) document in'the developing of EOPs.
This is because
the
EPG is principally a "differences type"
document
between
the
EPG and the
SSES plant specific informa-
tion.
The intent of the of the
PSTG is to define the accident miti-
gation strategy that can
be used to develop the
EOPs.
If the licen-
see
had developed
the
EPG by placing the plant specific inform-
ation together in logical order, the accident mitigation strategy
could have
been easily determined
and differences
between
the
EPG and
may have
been minimized.
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3.
Technical
Ade uac
of EOPs
A.
Ensure
The
and supporting
procedures
do not contain direction
to ensure that the
Scram Discharge
Volume (SDV) vent and drain
valves close following a reactor
If these
valves
do not
close,
reactor coolant will be released
into secondary
contain-
ment.
B.
RPV Control
Reactor
Shutdown
2.
E0-102,
step
RC-2 directs exit of RPV Control
when the reactor
is shutdown.
No definition of "shutdown" is provided in the
EOPs.
The
EOP bases for E0-102,
step
RC-2 state that
"shutdown" is defined in step
RC/(}-15.
The bases
for step
RC/g-15 do not discuss
the term reactor "shutdown."
Maximizin
CRD flow
3.
E0-102,
step
RC/g-14 directs starting the second
Control
Rod
Drive (CRD) pump if all rods are not inserted.
No direction is
provided to start the other
CRD pump if it is not running.
Both
pumps
need to be started, if possible,
to maximize
CRD flow.
Drain of the Scram Dischar
e Volume
4.
E0-102,
step
RC/g-24 directs
a manual scram after allowing the
Scram Discharge
Volume (SDV) to partially drain.
The
do not define
an acceptable
limit (time or volume) for draining
of the SDV.'This item was identified by the licensee prior to
the inspection.)
'I
Scram of Individual Control
Rods
E0-102,
step
RC/g-27 directs that control rods
be
scrammed
individually in accordance
with Attachment
B of EO-102.
E0-102,
step
RC/g-28 is a decision
step which directs
repeat of step
RC/g-27 if rod motion was observed
or reset of the
scram if no
rod motion was observed.
It is not clear whether step
RC/(}-28
applies after attempting to scram
each control rod,
each
group
of control rods, or all control rods.
Additionally, Attachment
B does
not provide specific direction for manually
scramming
rods.
No direction is provided in EO-102 to close the
test switch after the rod is scrammed
as specified in SSES
step
RC/(}-5.4.
The
scram test switch must
be closed to allow
reset of the scram.
L
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5.
Safet
Relief Valve
C clin
E0-102,
step
RC/P-3 is
a decision
step which directs actions
bas'ed
on whether
(SRV) is cycling.
The
EOP bases
do not provide
a clear definition for "SRV cycl-
ing." It is not clear whether
manual
operation of SRVs for
pressure
control constitutes
"SRV cycling."
C.
Primar
Containment Control
Use of HPCI and
RCIC with Low Su
ression
Pool
Level
2.
E0-103,
step
SP/L-8 directs that
HPCI and
RCIC not be used if
suppression
pool level is below 18.5 feet.
No direction is
provided to override
HPCI and
RCIC in accordance
with the
procedure for overriding
pump initiations.
ES procedures
cannot
be used unless specifically directed
by the
EOPs.
It
would be necessary
to override the initiation signal, if
present,
to prevent automatic
HPCI and
RCIC operation.
E0-103,
step SP/L-9 requires
a manual scram after
HPCI and
RCIC become
unavailable.
If the
scram is delayed until after HPCI and
become unavailable,
and
CRD are the only sources
of
high pressure
feed available
when the reactor is scrammed.
Monitorin
of Su
ression
Chamber
Pressure
There is no suppression
chamber
pressure
indication available
in the Control
Room for suppression
chamber
pressure
above
3
psig.
E0-103,
step
PC/P-7 provides direction for lining up
local indication using the Containment
Atmosphere Monitoring
(CAM) system.
The
CAM system isolates
on high drywell pressure
and the isolation valves cannot
be reopened for 10 minutes
following the isolation signal.
No suppression
chamber
pressure
indication would be available for at least
10 minutes following
a high drywell pressure
signal.
Actions for Primary Containment
Pressure
Control, Drywell Temperature
Control,
Level Restora-
tion,
and
RPV Flooding are dependent
upon suppression
chamber
pressure.
Restoration
RPV Level Indication
EO-114 does not provide direction to restart injection following
termination of injection in step
RF-12 if RPV water level indi-
cation is restored within the time allowed by the
Maximum Core
Uncovery Time Limit.
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ATTACHMENT C
DETAILED WALKDOWN COMMENTS
1.
General
A.
Emergency
Support, Off-Normal, and
Emergency Operating
Procedures
do
not caution operators
to take
an
E127 key along when performing
emergency
lineups in the plant that require unlocking padlocked
valves.
2.
EO-100
Cauti ons
A.
Caution
1 of the
EOPs warns that drywell temperature
affects
water level indication.
The bases for this caution provide
a
detailed discussion
of the temperature
effects
and indicate which
level instruments
are affected.
Specific restrictions for use of RPV
level indicators are provided in Attachment
A of the bases for EO-
100.
Some of the operators
that were questioned
about this caution,
were not familiar with which level instruments
were affected
by dry-
well temperature
and could not easily locate the attachment that
provided the specific restrictions.
3.
-EO-101
4.
EO-102
RPV Contr ol
A.
EO-102
ste p RC/P-6 directs restoration
of Containment
Instrument
Gas
(CIG) in accordance
with ON-159(259)-002.
If the
CIG system is iso-
lated due to a
LOCA signal (-129" reactor water level or 1.72 psig
drywell pressure),
the isolation signal
must
be bypassed
in accord-
ance with ES-134(234)-001
to allow restoration of CIG.
Procedural
direction to use
ES-134(234)-001
is contained
in E0-102,
step
RC/P-9
which directs opening the MSIVs in accordance
with ES-184(284)-001
and E0-103,
step
PC/P-5 which directs bypassing
drywell cooling logic
isolations.
Neither of these
steps
provides specific direction to
bypass isolations
and restore
CIG.
As a result the operators
do not
take prompt action to restore
CIG after it isolates
on
a
LOCA signal
(specifically high drywell pressure)
and the MSIVs are allowed to
drift closed.
No clear direction is provided to reopen
the MSIVs to
utilize the main condenser
as
a heat sink if this occurs.
A.
E0-101,
step
S-12 directs the operator to reset
main generator
lock-
outs in accordance
with ON-193(293)-002.
The only action necessary
to reset the main generator is to operate
the reset lever, which the
, operator would be expected to be able to do without referring to the
procedure.
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B.
Attachments
B and
C are not labeled
on the back of the Control
Room
flow charts in Unit 1.
5.
EO-103
Primar
Containment Control
A.
B.
C.
D.
E0-103,
step
SP/T-10 directs operation of HPCI in accordance
with
EO-032 and
RCIC in accordance
with EO-033 if suppression
pool temper-
ature
exceeds
150 degrees
F.
EO-032
and
EO-033 do not clearly indi-
cate which steps
should
be performed to operate
HPCI and
RCIC with
high suppression
pool temperature.
E0-033,
section
2. 1 directs
use
of ES-152(252)-001
and ES-152(252)-002
to bypass
interlocks to allow
operation of HPCI in full flow test
whether
use of these
ES procedures
is authorized if EO-032 was
entered
due to high suppression
pool temperatures.
Drywell pressure
indication in the Control
Room,
above
3 psig, is in
psia.
Containment
pressure
parameters
are expressed
in psig through-
out the
EOPs.
This could result in confusion
or incorrect
implementation of the
EOPs.
E0-103,
step
PC/P-7 provides direction to lineup and monitor suppress-
ion chamber pressure
locally at the Hydrogen/Oxygen
(H2/02) Monitor-
ing panel
in the reactor building.
The panels
and valves that must
be operated to lineup the indication are located in poorly lit,
contaminated
areas.
The gage
had two scales,
one in inches of water
and psig,
the other in Kpa.
The poor lighting, the size of the gage,
and the dual
scales
made the
gage very difficult to read.
The licen-
see modified the gage face prior to the completion of the inspection
. by removing the inappropriate
scale.
The decision
statements
in E0-103,
steps
PC/P"11,
PC/P"19
and
DW/T-6
require the operator to make two decisions.
Direction to spray the
drywell is dependent
on whether containment
has
been vented
and
whether conditions are
above the Drywell Spray Initiation Limit.
The
majority of the operators
interviewed misinterpreted this step
and
stated that they would not spray the drywell if conditions were below
the Drywell Spray Initiation Limit even if containment
had not been
vented.
E.
E0-103,
steps
PC/P-5
and PC/P-22 both reference
ON-134(234)-001,
"Loss of Reactor Building Chilled Mater'" for reduction of drywell
pressure.
Section 3.4 of ON-134(234)-001
(page
5) directs the opera-
tor to section 3.7 for reduction of containment
pressure.
Pages
1
through
4 of the
ON contain information that is not applicable to
performance of the specified task.
The first two steps of section
3.7 refer to OP-173(273)-001
and ON-159(259)-002 for radiation
monitoring and sampling of containment.
It is not clear whether or
not these
steps
have to be performed'when
venting in accordance
with
E0-103,
step
PC/P-5 or PC/P-22.
ON-134(234)-001
contains
a caution
that
SPING is required
when venting unless directed
by shift super-
vision.
No guidance is provided for shift supervision to determine
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SPING is required.
The next two steps of ON-134(234)-001
address
bypassing
LOCA and high radiation isolation signals.
It is
not clear when these
steps
are authorized to be performed.
The
procedure
then directs pressure
reduction in accordance
with OP-
173(273)-001.
OP-173(273)-001
provides instructions for operating
the entire Containment Atmosphere'Control
system,
which includes
containment
purge
and exhaust,
nitrogen inerting and makeup,
H2/02
monitoring,
and the hydrogen
recombiners.
Section 3.5 of OP-173
(273)-001 provides instructions for primary containment nitrogen
makeup
and pressure
control, including prerequisites
and precautions
for normal operations.
Sections 3.5.5, 3.5.7
and 3.5.9 address
decrease
pressure
depending
on plant condi-
tions.
All of these
sections
require
manual start of Standby
Gas
(SGTS) in accordance
with OP-070-001.
The bases for step
DW/T-1 of EO-103 indicate that subsequent
action
levels in the
DW/T leg are
based
on drywell average
temperature,
which is determined
by performing
a calculation in accordance
with
SO-100(200)-007
or determined automatically by SPDS.
Operators
indicated that, in an emergency,
they would use hard-wired control
room indication to determine drywell temperature
and would not take
the time to calculate drywell average
temperature.
G;-- The Heat Capacity Temperature
Limit curve is difficult to use,
because
the axis for RPV pressure
is labeled at
150 psig,
250 psig,
350 psig, etc.,
instead of at the normal
(even)
100 psig increments.
6.
EO-104
Secondar
Containment
Control
A.
E0-104,
step
SC-2 refers the operator to Emergency
Support procedure
but there is no information to tell the operator
which
section of the procedure
to use.
B.
In Table SC-2,
Secondary
Containment
Maximum Operating
Values,
the
heading
MAX NORMAL is not annotated
to indicate that it also repre-
sents
the Area Isolation Set Point.
Without this information, the
operator
cannot easily determine if an entry condition
has
been
reached.
C.
Differential temperature
alarm and isolation setpoints
are not
included in Table
SC-2 or provided elsewhere
in EO-104.
Without this
information, the operator
cannot easily determine if an entry condi-
tion has
been
reached.
D.
There are eleven additional
Area Radiation Monitors associated
with
the Secondary
Containment that are not listed
on Table SC-3,
Second-
ary Containment
Maximum Operating Values.
High radiation levels in
these
areas
would require entry into Secondary
Containment Control.
Without the information in Table SC-3, the operator cannot easily
determine if an entry condition has
been
reached.
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EO-111
Level Restoration
A.
E0-111,
step
LR-33 requires
the
use of the Suppression
Chamber press-
ure gage located
on Panel
1C226A(B), which is outside
the Control
Room and
may not be available.
This fact is not noted in the step.
8.
EO-114
RPV Floodin
A.
B.
E0-114,
step
RF-4 directs the operator to flood the
RPV in accordance
with ES-152(252)-001
or ES-150(250)-001.
The referenced
procedures
do not clearly indicate which portion of the procedures
should
be
used to accomplish
the desired action.
E0-114,
Table RF-1, Conditions Requiring
RPV Flooding,
does not indi-
cate that the operator
must use the Suppression
Chamber pressure
gage
on Panel
1C226A(B), which is located outside the Control
Room and
may
not be available.
C,
The bases
for E0-114,
step
RF-11 indicate that two level indicators
must be restored
to exit RPV flooding.
This step
on the flowchart
does not indicate that two level indicators
are required.
9.
E0-.100
200 -030
Unit
1 Unit 2
Res
onse to Station Blackout - RPV In ect-
~ ion ~ Usin
Firewater
A.
Several
steps
in the
EOPs direct injection into the
RPV with the
firewater system in accordance
with EO-030.
The entry conditions for
EO-030 do not address
the
EOPs.
Neither the
EOPs nor
EO-030 reference
the section of EO-030 to accomplish
the desired
task.
B.
Step 2.5 which requires
the operator to remove
a unisolable blank
flange to install
a fire hose,
would result in the loss of fire water
from the fire system.
10.
EO-032
S stem 0 eratin
Guidelines Durin
Station Blackout
0 eration With Hi
h Lube Oil
Tem eratures
A.
The valve specified for connection of firewater to provide lube oil
cooling for
HPCI is not easily accessible.
Two other root valves',
downstream of the specified valve, are easily accessible.
No adapters
are readily available for connecting
3 inch fire hose
to the 3/4 inch valve connection to provide lube oil cooling for
HPCI.
The adapters
are supposedly available in a warehouse
on
site, but the operator did not know where to attain
them.
11.
234 -001
B
assin
Dr well Coolin
Lo ic Isolations
A.
In order to reduce primary containment
pressure
in accordance
with
this procedure
CIG, Instrument Air, and Drywell Cooling must be
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restored
"as needed"
in accordance
with the applicable
normal operat-
ing procedures.
These operating
procedures
and ES-134(234)-001
do
not provide direction to open the drywell cooling chilled water in-
board
and outboard isolation valves which close
on high drywell
pressure.
These valves must be open to supply cooling water to the
drywell coolers.
E0-103,
step
PC/P-5 directs
use of ES-134(234)-001
to bypass
drywell
cooling logic isolations
when drywell pressure
is above
1.72 psig.
ES-134(234)-001,
step 4.8 provides direction to run drywell cooling
fans in fast speed if drywell pressure
is less than
2 psig.
The
procedure
does
not refer to section
4. 1 for operation of drywell
cooling fans in slow speed if drywell pressure
is greater
than
2
psig.
It is not clear whether drywell cooling fans should
be run in
fast
speed during emergency
conditions with drywell pressure
above
2
psig.
12.
250 -001
RCIC Turbine Isolation
and Tri
8
ass
A.
Step 4.1.1 refers to the
"RCIC Keylock Switch", but the label for the
switch reads
"RCIC SYS A LOGIC".
B.,
C.
'tep 4.3. 1 refers to the "Reactor Vessel
High Water Level Signal
Sealed-in
& Reset" relay, but the label for the relay reads
" RCIC
The drawings in Attachment
A do not contain the
name of the relays
that they apply to.
13.
250 -002
Bor on Injection Usin
S stem
A.
B.
C.
The removal of piping and its replacement with a 2'- 4" pipe coupling
and
hose
appears
to be
a difficult task due to the physical arrange-
ment of the
SLC piping'dditionally, the 2'-4" pipe coupling,
supplied for use in this step,
might not fit the connection.
This is
due to
a chain link.welded to the pipe that could interfere with a
drain pipe at that location.
Step 4. 1 does not contain instructions to secure
the hose to insure
that the
hose
stays
in place,
This is important due to the long
vertical drop of the hose
from the
The method of clamping the hose to smooth couplings
may not be ade-
quate
when the
hose
becomes filled with water.
14.
252 -001
HPCI Turbine Isolation
Tri
and Initiation B
ass
A.
Steps 4.1.17
and 4.1.19 refer to "STM LINE ISO VLV BPV", but the
label
reads
"WARMUP LINE ISO".
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Step 4.4.5 refers to "INITIATIONSIGNAL HS-E41-S17
RESET", but the
label
reads
"HPCI INTSG RESET".
C.
In Attachment A, page 2, the relay
name is "HIGH DRYWELL PRESS",
but
the label
reads
"RN HIGH WATER LEVEL SIG SEALED IN 8
RESET".
15.
255 -001
Vent
CRD to Insert Control
Rods
A.
There is no caution to tie down the drain tubing at the drain to
prevent kickout.
16.
284 -001
B
assin
MSIV Isol ations
A.
Step 4.8 refers the operator to an operating
procedure,
OP-184(284)-
001, which is the procedure
used for normal
system operation.
Many
of the steps
and cautions
in this procedure
would not be applicable
or necessary
in an emergency situation.
17.
ON-155 255 -007
Loss of CRD Flow - Cross
Connect
CRD from Unit 2
A.
The procedure
does not contain
any directions to assist
the operator
in locating the applicable part of the procedure
to accomplish
the
task specified
by the
EOP.
B.
The procedure
does not contain
a restoration
section.
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ATTACHMENT D
HUMAN FACTOR EXAMPLES
The following examples
are provided to clarify the types of problems identified
in the areas of human factors concerns
described
in Section
7 of this report.
These
examples
are not intended to be viewed as
an inclusive list of all such
problems
found in the
EOPs,
but rather
as
a set of limited examples of the
types of inadequacies
found through the
human factors analysis.
l.
Verification of EOPs
from a
Human Factors
Pers ective
A.
Item 6.3.11 in the
EOP writers guide states
that lists in steps
which
are not identified as logical
AND lists are
assumed
to be
OR lists.
This direction is not followed in
several
places
in the
EOPs.
Step
S-4 in EO-101 states
that the operator
must ensure
several
items.
From the writers guide, this is assumed
to be
an
OR list; however, it
is an
AND list.
Step S-7 is another
AND list and step
S-10 is an
list and all are formatted the
same.
B..
Item 6.2.10.d.
states that conditional
statements
shall not
appear
in decision
steps.
In Step
RF-18 in EO-114
a conditional
AND appears
in a decision
diamond.
Steps
DW/T-S, PC/P-ll and PC/P-19 of EO-103
are decision
diamonds that contain conditional
statements.
C.
D.
Item 6.3.10.c.
states
that
THEN is optional after
WHENs.
The imple-
mentation of this item in the flow charts is inconsistent.
In some
places
THEN appears after
WHENs and in places it does not
(See
Steps
RC/P-ll, RC-2,
and Lg-9).
Item 6.2.10.b.
states that "Yes" and "No" answers
shall
be placed
consistently
on 'the sides of decision
diamonds.
The main flow path
in EO-112
has three "Yes" answers
on the right side of the decision
diamonds
and then
a "No" on the right.
Consistent
placement of the
"Yes" and "No" answers
minimizes the potential for human error in the
use of flow charts.
2.
Action Verbs
A.
B.
"Slowly" in step
Lg-15 in EO-113 is used
as
an action verb, but is
not'defined in the writers guide.
"Observe" is defined in the writers guide
as "watch for an expected
occurrence
and does not require follow up."
However, in Step
EO-101 "Observe" is used
as
"Ensure."
"Ensure" requires
a follow-up
to cause
the action to occur if it has not already occurred.
"Verify" is also
sometimes
used
as "Ensure."
C.
Action verbs
used in the procedures
that are not defined in the
writers guides include <<Inhibit"
nInsertw, and>>Inform
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Cautions
and Notes
A.
Item 6.2.15 states that cautions shall
be located in the lower left-
hand corner.
In E0-113, the caution
box appears
in the upper right-
hand corner.
B.
C.
D.
E.
What is defined
as
a note in the writers guide (see
Step
S-27; the
box connected
by the dashed line) contains actions.
Cautions
and notes
are contained
in the
same
box, titled "Cautions
and Notes" (see all flow charts).
Cautions
are not placed before the steps to which they apply (see
Steps
S-27,
RC/P-8,
and Lg-13).
Statements
in various steps
read like cautions or notes,
but are.
formatted
as steps
(see
Step
RD-8 in E0-112).
4.
Writers Guide
A.
Steps
LR-6 through
LR-38 are contained
in a large decision
box.
However, the writers guide does not contain direction for construct-
ion of decision
boxes.
Step
S-27 in EO-101 is also
a decision
box.
- NUREG-5228 provides
examples
on
how to format decision
boxes.
B,
Step SP/L-4 is a "case" type decision
diamond.
Although the writers
guide does
not prohibit its use, it does not provide proper formatt-
ing techniques.
C.
The dashed
lines around
steps
LR-24 through
LR-29 and
LR-31 through
LR-34 in EO-111 are not defined in the writers guide.
D.
The formatting of steps
involving time are not presented
in the
writers guide.
However,
steps
RF-8 and RF-12 utilize time dependent
information.
E.
The format of ES-149(249)-001
does
not follow the writers guide
direction to begin each section of the procedure
on
a
new page.
5.
Transitions
A.
Examples of the
IAW (in accordance
with) transitions
are steps
RC/P-9
in E0-102,
PC/P-3
and PC/P-4 in EO-103
and
RR-4 in EO-105.
The
definition for IAW appears
in the procedures
writers guide (OI-AD-
055).
This definition states that .judgement
should
be used
as to
which steps
should
be performed in the procedure.
In emergency
situations
human error could result if judgement is allowed to any
great degree.
This is illustrated by PC/P-3
and PC/P-4.
Both steps
require actions
but require actions
in two different
sections of ES-134-001.
If steps
are critical to mitigate the tran-
sient then the transition should clearly identify the section of the
procedure
to enter.'
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IAW is not clearly defined in the
EOP writers guide (AD-(A-330).
A format consistent with the
EOP writers guide would be to use the
concurrent exit and to list the section of the procedure to be
entered.
B.
Examples of the "perform" transitions
are steps
S-22 in EO-101
and
RC/g-43 in EO-100-102.
Perform is not defined in the writers guides
as
a transition method.
A format consistent with the
writers guide would be to use the concurrent exit and to list the
section of the procedure
to be entered.
C.
Numerous
examples exist in which the operator is directed
from an
EOP to an
ES,
ON, or
OP procedure
and then to another
OP or
ON
procedure.
(See Attachment
C for examples.)
D.
In step
RF-15
an exit arrow is used to direct the operator to step
RF-22.
In this case,
a flow path should
be used
and not a transition
arrow.
6.
Ste
and Table Wordin
A.
B.
A'number of steps
were contingent
on "adequate
core cooling", but
adequate
core cooling is not clearly defined in the basis
documents.
The definition is not provided in quantitative
terms that the opera-
tor can observe.
This could lead to confusion or inconsistent
interpretation
by the operators
(see
steps
PC/P-18,
PC/P-20,
and
DW/T-9 in E0-103).
Step
RC/g-26 in EO-102 tells the operator to partially drain the
SDV.
"Partially",is not defined
and could be interpreted differently by
each operators,
C.
D.
Step
S-27 in EO-101 is
a hybrid step.
It contains
a decision
box,
an undefined
step attached
by a dashed line,
and
an
imbedded action
step.
The subdivisions of the step are also not uniformly sized.
The curves presented
in EO-103 are not the
same curves that are
on
the
SPDS.
E.
Steps
SC/R-3
and SC/T-4 in EO-104 and step
RR-3 in EO-105. say to
maintain
PC integrity or prevent
PC failure.
The definition of
this is not found in the bases.
F.
The wording on the Heat Capacity Temperature
Limit Curve,
Figure
PC-1
of EO-103 does not clearly define when the upper curve is
applicable.
0
I ~
'
h
.)
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