ML20207M359
| ML20207M359 | |
| Person / Time | |
|---|---|
| Site: | Braidwood |
| Issue date: | 01/07/1987 |
| From: | Burdick T, Reidinger T NRC OFFICE OF INSPECTION & ENFORCEMENT (IE REGION III) |
| To: | |
| Shared Package | |
| ML20207M304 | List: |
| References | |
| 50-456-86-03, 50-456-86-3, 50-457-86-03, 50-457-86-3, NUDOCS 8701130155 | |
| Download: ML20207M359 (129) | |
See also: IR 05000456/1986003
Text
,
_
.
- _.-
- - - - . - .
.
-
,
,
)
!
.
U.S. NUCLEAR REGULATORY COM1ISSION
REGION III
Report No. 50-456/50-457/86-03
Docket Nos. 50-456/50-457
Licensee:
Commonwealth Edison Company
ATTN:
Mr. Cordell Reed
Vice President
Post Office Box 767
Chicago, IL 60690
Facility Name:
Braidwood Nuclear Station
Examination Administered At:
Braidwood Nuclear Station
Examination Conducted: October 27, November 11-14, 18-22, 1986
Examiners:
B. C. Haagensen, Sonalysts
T. P. Guilfoil, Sonalysts
G. D. Weale, Sonalysts
I. J. Kingsley, Sonalysts
"
K. L. Parkinson, Sonalysts
F. W. Victor, Sonalysts
g
R
I
7
Chief Examiner
Da'te '
,
I
t 1 [f7
Approved By:
T. M. Burdick, Chie
Operator Licensing Section
Date
i
kokIIj00gK05000456
5 870108
-
V
--
_ - _ _ - - - - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
j
-
'
.'
,
Examination Summary
Examination administered on October 22, 1986, and during the period of
November 11-14 and November 18-22, 1986, (Report No. 50-456/0L 86-03
Examinations were administered to 17 senior reactor operators, and 7 reactor
operators.
Results:
All but 2 of the 17 senior reactor operations passed the examination.
All but 1 of the 7 reactor operators passed the examination.
2
,
,
'
,
REPORT DETAILS
Examination Review Meeting
Licensee coments and their resolutions are attached to this report.
Exit Meeting
a.
On November 21, 1986, an exit meeting was held. The following personnel
attended:
Eugene E. Fitzpatrick, Ceco, Braidwood Station Manager
K. C. Kofron, CECO, Production Superintendent
Kevin Bartes, Ceco, Training Supervisor
C. W. Schroeder, CECO, Services Superintendent
Thomas M. Tongue, NRC, Senior Resident
Ronald L. Higgins, NRC, Licensing Examiner, Region III
Paul R. Sunderland, NRC, Region III
Brian C. Haagensen, NRC/Sonalysts, Lead Examiner
Francis W. Victor, NRC/Sonalysts, Licensing Examiner
Ivan J. Kingsley, NRC/Sonalysts, Licensing Examiner
b.
The Lead Examiner discussed the following comments with the licensee
representatives:
(1) The candidates exhibited a tendency to race through procedural action
and verification steps at the expense of accurately completing the
steps.
In several instances, operator candidates missed steps in
the emergency and abnormal procedures because of excessive haste
to complete the procedure.
(2) Many candidates did not demonstrate sufficient knowledge of basic
radiation and exposure monitoring practices. They did not understand
proper frisking techniques and the allowable count rates above
background levels to constitute personnel contamination, they did
not know how to read RWP survey maps and they did not have a solid
understanding of personnel dosimetry equipment and its uses.
(3) Many licensing candidates did not demonstrate knowledge of valve
lineup and verification requirements. They did not know how to
conduct valve lineup checks on locked manual valves, manual throttled
valves and automatically operated valves.
(4) Many candidates did not demonstrate effective control of axial flux
difference (AFD) during simulator exams. Confusion existed regarding
the use of the iconic display, the computer data table display and the
AFD meters on the main control boards. When the process computer was
not operating correctly, some candidates had difficulty tracking AFD
using control board indicators and could not keep track of AFD penalty
points per tech specs.
3
.
,
,
.
(5) Although the overall trend shows improvement from previous exams, the
candidates' operation of the plant from the remote shutdown panel is
still weak. The candidates did not demonstrate familiarity with the
procedure for operating from the remote shutdown panel (PRI-5) and in
several cases, did not carefully verify that all local / remote switches
were selected to the local position.
(6) Many candidates did not have sufficient knowledge of GSEP procedures
and had difficulty classifying events and completing the NARs forms
correctly.
In many cases, tha candidates did not understand the
selection of protective action recommendations and were unaware that a
default set of PARS existed at the initial classification of a general
emergency event.
Additionally, many candidates would classify the
events by finding the first match between the EAL table events and
actual plant conditions, but would never check other EAL table events
to determine if a higher classification was appropriate under a
different event.
(7) Many candidates showed confusion over the use of the steam dump valves
in the steam pressure mode of operation.
(8) Many candidates lacked detailed knowledge of the rod control system
alarms, components and effects of malfunctions.
(9) The use of " orange dots" to identify tripped protective bistables was
not documented by an administrative procedure and each shift used the
" orange dots" differently.
(10) Many candidates had difficulty discussing the reactivity effects on
flux level, startup rate, shutdown margin and coefficient variation.
c)
Although it was not discussed at the exit meeting, the Braidwood Nuclear
Station Training staff is requested to provide a copy of their plant
specific modification of the Knowledges and Abilities Catalog for Nuclear
Power Plant Operators: Pressurized Water Reactors (NUREG-1122) to the
region.
This will facilitate the region with the development of site
specific examinations for the Braidwood Nuclear Plant.
It is requested
prior to the next scheduled examination.
,
4
_ -
-.
- - _ - _
- _ .
- _.
- -
-
- -
.
- - - _ - -
- _ _ _ _ _ _ _ _ _ _ _ _ - _ _
_
s
,.
.
QUESTION 1.03 (2.00)
Considering their production and removal rates, explain why:
a.
Equilibrium concentration of Xenon increases as reactor power increases.
(1.0)
NRC ANSWER 1.03 (2.00)
a.
For equilibrium, Xenon removal by decay must increase as power increases
(0.5).
Xenon removal by decay is proportional to Xenon concentration (0.5).
(Therefore, Xenon concentration increases as power increases - optional.)
(1.0)
BRAIDWOOD CONTENTION:
1.03 a.
Westinghouse Reactor Theory Text, Chapter 4, Fission Product Poisoning
Effects describes Xenon characteristics.
These characteristics at
equilibrium conditions indicate that the rate of change of Xenon
concentration is equal to the production rate minus the loss rate.
As power is increased from an equilibrium condition, eventually Xenon
production exceeds Xenon removal due to the higher flux level
(production terms).
However, as Xenon concentration increases
the decay of Xenon and Xenon burnup become more significant and
establish a new equilibrium condition at a higher Xenon concentration,
since burnup is a function of Xenon concentration and flux, while
decay is a function of Xenon concentration only.
REFERENCE:
Westinghouse Text Fundamentals of Nuclear Reactor Physics
Pages 4-11 through 4-14.
1.03a
Resolution
The facility contention provides additional information concerning the
relationship between power level and xenon concentration.
Candidate answers
that provided similar amplifying information plus the cause-and effect
relationship stated in the NRC answer were not graded wrong.
QUESTION 1.05 (2.75)
a.
Select / match one equation from the right-hand column that applies to each
of the following heat transfer rates in a steam generator (SG).
(0.75)
(1) Rate of heat gain by feedwater/ steam
(a) h = [nCp At
(b) h=UAAH
(c) h=mCpAH
.
.
.
.
(d) Q = wf AH (wf = Wp)
(e) h=UAAT
5
%
,
.
b.
Define the following symbols / terms used in the above equations as they
apply to a steam generator.
(0.25)
.
.
(7) Wf = Wp
NRC ANSWER 1.05 (2.75)
a.
(1) (d)
(0.25 each)
b.
(7) Wf feed flow rate or steam flow rate or secondary coolant flow rate
or mass flow rate.
(0.25)
BRAIDWOOD CONTENTION:
hfisnotastandardsymbolatBraidwoodforfeedflowrate.
The symbol used
for feed flow rate is mf or mfeed.
The us2 of Wf may cause some candidates to
be unable to recognize "(d)" as the correct match for "(1)" in Part a. and
unable to define Wf in "(7)" of Part b.
REFERENCE:
Thermal-Hydraulic Principles
1.05
Resolution
The equation Pwr = Wf Ah appears on the standard NRC license exam equation sheet
that was provided to the candidates with this exam.
Full credit was awarded to
answers that provided the Braidwood equation (Q = mf Ab) for " Rate of heat gain
by feedwater/ steam" and to definitions of m as feed flow rate or steam flow rate.
QUESTION 1.06 (.75)
In a simple " closed" cooling water system (similar to the CCW system, but with
just one centrifugal pump, a surge tank, and a heat exchanger loop), the
isolation valve in the line to the surge tank is inadvertently shut and the pump
discharge flow-control valve is fully opened.
Soon afterward the pump starts
operating noisily and vibrating excessively due to cavitation.
In this situation:
b.
What is one reason why opening the surge tank isolation valve halfway
open will stop the pump vibrations / noisy operations?
(0.25)
NRC ANSWER 1.06b.
b.
Restores the source of required NPSH.
(0.25).
BRAIDWOOD CONTENTION:
1.06b.
Answer should be " restores the source of NPSH available."
REFERENCE:
Thermal-hydraulic Principles, Volume II, Page 10-55.
6
,
,.
.
1.06
Resolution
Candidate answers that stated opening the surge tank isolation valve halfway
I
open restores the source of required or available NPSH were awarded full credit.
QUESTION 3.07 (2.25)
For the following actions / occurrences, state the:
(1) Steam dump control system response,
(2) The plant response, and
(3) The resulting method of RCS temperature control.
Assume all systems operate normally except as stated and that no operator action
is taken.
Consider each case separately.
c.
The Train B Reactor Trip Breaker fails to open on a reactor trip signal
while at 78% power.
NOTE:
The Train A breaker opens properly.
(0.75)
NRC ANSWER:
c.
(1) Normal shift to the Turbine Trip controller will not occur.
(0.75)
(2) Plant will cooldown because Load Rejection controller will open
steam dumps.
(0.25)
(3) The Load Rejection controller will maintain RCS temperature near "No
Load" Tref (+4F deviation /deadband).
(0.25)
REFERENCE:
BW SYST TRNG MAN FIG 24-7, 9
BRAIDWOOD CONTENTION:
3.07 Part c.
C-8 is picked up and the turbine trip controller is activated
and will control the steam dumps to reduce Tave to no load value.
Since an actual Rx trip did occur the STM DUMP SYSTEM will
function normally.
REFERENCE:
BW SYST TRNG MAN.
ATT. A Page 24-32
Figure 24-9
3.07c
Resolution
The detailed circuit and logic diagrams needed to confirm the facility
contention were not included in the provided reference material package.
Since the provided reference material dose not contradict the facility
contention, full credit was awarded to candidate answers that stated the
following:
7
,'
,
(1) Steam dump control shifts to the Turbine Trip (Plant Trip)
controller.
(2) Plant temperature decreases to "no-load" Tavg.
(3) Steam dumping maintains RCS temperature near no-load Tavg.
QUESTION 3.15 (1.00)
Identify the control, protective, and permissive functions which use
individual loop Tave signals and NOT auctioneered Tavg.
ANSWER 3.15 (1.00)
1.
OT Delta-T calculator
(0.25)
2.
OP Delta-T calculator
(0.25)
3.
P-12 circuitry (Hi Stm. Flow SI permissive, Stm. dump block)
(0.25)
4.
Feedwater isolation circuitry
BRAIDWOOD CONTENTION 3.15:
List of setpoints vice names should be acceptable.
Part 3 Tave 550 = P-12
Part 4 Tave 564 = FW isolation setpoint
3.15 Resolution
The question requested " control, protective, and permissive functions," not
setpoints.
In Part 3 full credit was awarded to candidate answers that stated
P-12 or its equivalent functions (Steam Dump Block, Lo-Lo Tavg, or Hi Steam
Flow SI Permissive).
In Part 4 full credit was awarded to candidate answers
that stated feedwater isolation.
QUESTION 4.15 (1.50)
According to the BW Precautions, Limitations, and Setpoints book, all reactor
trip and safeguard actuation channels, except three, shall be placed in the
trip mode when the channel is out of service for any reason.
List the three
excepted circuits / trips that may be bypassed for maintenance.
(1.5)
ANSWER 4.15 (1.50)
1)
Source range hi flux trip
2)
Intermediate range hi flux trip
3)
Containment pressure hi-2 spray actuation (0.5 each)
REFERENCE:
BW PLS PG 7
8
__ ________ ___
_ _ ________ __-_____ - ______
_
_ _ _ __
.
,
BRAIDWOOD CONTENTION:
Answer key Part 3
3.
Containment pressure hi-3 spray actuation.
REFERENCE:
BW PLS PG-10
,
BW SYST TRNG MAN. 59-Page 21
,
t
4.15 Rasolution
'
Paragraph A.11.b of PRECAUTIONS, LIMITATIONS, AND.SETPOINTS FOR NUCLEAR STEAM
SUPPLY SYSTEMS (Revision 6, March 1986) for Braidwood Station Units 1 and 2
states, in part,
"The reactor trip and safeguards actuation circuits noted below may
be administrative 1y bypassed for maintenance on a single channel.
3)
Containment high-high pressure spray actuation."
,
Full credit was awarded to candidate answers that stated
3)
Containment pressure Hi-3 spray actuation.
!
NOTE:
The facility should designate the correction / resolution of
Section A.11.b.3) as an open item.
i
Question 5.06 (1.50)
Compare the calculated Estimated Critical Rod Position (ECP) for a startup 15
hours after a trip to the Actual Critical Rod Position (ACP) if the following
events / conditions occurred.
Consider each independently.
Limit your answer
to:
-
I
a.
b.
.
c.
ACP is unchanged.
1.
Actual RCS temperature is 551*F at criticality.
(0,5)
NRC ANSWER 5.06
1.
b.
i
L
BRAIDWOOD CONTENTION:
!
!
The question does not state the temperature at which the ECP was calculated
s
for.
Prerequisite number of one of BwGP 100-2 states that to perform a plant
startup, the plant must be in a Hot Standby (Mode 3) condition with all RCS
loop temperatures greater than 550'F.
Therefore, an ECO could be calculated
'
l
with Tavg equal to 551*F and the reactivity effects would be corrected for the
1
i
l
l
l
9
l
- . - _- - - - -
- -
-
.
- - -
. - - . . .
- , - - -
,
_ _ _ _ - _ _ _ _ _ -
'
,'
.
deviation form 557'F by the ECP calculation, BwGP 100-A8.
Therefore the ACP
could be equal to the ECP or even higher than the ECP if 550 F were used for
ECP calculation.
Reference:
BwGP 100-2, BwGP 100A8
5.06 Response
The Braidwood ECP (BwGP 100-A8) Item B.3 provides the operator with a step to
adjust the TAVE expected at startup if it is different from 557*F.
The
question explicitly did not provide this adjustment because part of the full
credit answer was to understand that the default TAVE for calculating the ECP
was 557'F. With no valve of "TAVE expected at Startup
provided,
"
the candidate should use the default value of 557*F for comparison in arriving
at the correct answer.
If the candidate assumes a TAVE at startup that is different than 557 F, then
full credit will be given for the correct answer based on his assumed value.
Answer scores indicate that 13 of 14 candidates provided the correct response
and therefore, most candidates were not confused by the question.
QUESTION 5.11 (2.5)
b.
When natural circulation is established in the RCS, mass flow rate of the
coolant is proportional to:
(0,5)
1.
(delta-T)
2.
(delta-T)2
3.
(delta-T)3
4.
1/(delta-T)
c.
The reactor is producing 100% rated thermal power at a core delta-T of 60
degrees and a RCS mass flow rate of 100% when a station backout occurs.
Natural circulation is established and core delta-T goes to 28 F.
If
decay heat is 2%, what is the core mass flow rate (in %)?
(1.0)
NRC ANSWER 5.11
b.
2.
(0,5)
c.
To determine flow in NC:
h=acpdelta-T
h = M1 cp1 (delta-T)
1
m2 cp2 (delta-T)
Q2
b2 = h ml cp1 (delta-T)
2
h
cp2 (delta-T)
3
10
.
-
-
-
-
-
-
-
-
.
'
.
,
If the candidate assumes cp1 = cp2 then:
m2 = 2% x 100% x 60'F = 4.3% flow
100%
x
28"F
If the candidate determines cp1 and cp2 from the figure provided, then:
'
m2 = 2% x 100% x 145 x 60'F = 3.9% flow
100%
x
1.60 x 28"F
(accept - or - 0.2% from answer)
BRAIDWOOD CONTENTION:
5.11.b.
No correct answer is given.
Correct answer is (delta-T)b.
As
shown in the question reference (Thermal-Hydraulic Principles,
Volume II, Page 14-25),
.2
m a (delta-T)
Therefore m a (delta-T)b
Part b. of Question 5.11 should either be eliminated or any response
accepted.
REFERENCE:
Thermal-Hydraulic Principles, Volume II, Page 14-25.
5.11.c.
An alternative method for solving the problem should also be
accepted.
A commonly used thumb rule derived from natural
circulation testing is that decay heat equal to 6% full power
causes a stable natural circulation mass flow rate of approximately
6% of full flow (Page 14-23 of Thermal-Hydraulic Principles,
3
Volume II).
The correct relationship is that Q o m , however since
the candidates were forced to select an incorrect relationship in
Part b, a calculation consistent with the selected Part b answer
should be accepted.
REFERENCE:
Thermal-Hydraulic Principles, Volume II, Page 14-23.
5.11 Response
1.
Part b.
A typographical error in the set of matching answers
provided to the candidate caused none of the correct
answers to appear.
Part "b" of the question is deleted.
2.
Part c.
The proposed alternative method provided by the supporting
documentation in the Braidwood contention is theoretically
valid.
However, this alternative method requires the
candidate to assume a set of initial conditions that were
not provided as part of the answer key.
The set of
i
initial conditions that was provided to the candidates did
not allow the use of the alternative method because these
conditions were for forced circulation flow where the
Qm relationship does not apply.
3
I
11
i
.
,
Based on a review of the response, the examiner concluded
that the candidates were taught the proposed alternative
method and a thumb rule of "6% decay heat yields 60*F
delta-T and 6% natural circulation flow" to provide initial
conditions for rationing the equation.
Based on the
validity of the method and the clear preference to reach
this alternative answer, full credit will be given if the
answer given in the Braidwood contention is used.
However, the licensee should note that the figure
(FN0-0PS-12) provided in the contention to support the
alternative method only supports the thumb rule and
3
Q
m relationship for the theoretical curve.
The actual
4 loop test results appear as a linear relationship (Q m)
and 4.78% decay heat yields 6% flow (27% error between the
thumb rule and test results) instead of the 6% decay heat
'
yielding 6% flow thumb rule.
Additionally, the material
provided does not make reference to this thumb rule as a
convention that is accepted (or validated) for Braidwood
and it is not clear that all candidates are held
responsible for knowing the thumb rule.
3.
The purpose of this question was to test the candidate's
understanding of the natural circulation thermal
hydraulics and, specifically, the sensible heat equation
Q = m cp 'T.
The initial conditions provided did not
allow solving this problem any other way.
The
relationship in Part "b" could not be used to solve
Part "c" because the initial conditions were given for
forced circulation flow and the m2 AT relationship does
not apply to forced circulation conditions.
Hence, the
candidate who attempted to use the relationship in
Part "b" with the initial conditions provided to solve
Part "c" would automatically arrive at an incorrect
I
answer.
QUESTION 6.02 (2.00)
a.
Describe an IR instrument response if the circuitry in undercompensated
while performing a reactor startup, including any effects on SR
instrumentation.
Include any applicable setpoints.
(1.0)
NRC ANSWER 6.02 (2.00)
l
Undercompensating results in a higher than actual reading, (0.50) and if
!
a.
I
IR instruments read > 1.0E-10 amps (P-6 set point) upon entering the
source range, then P-6 will prevent the SR detectors from energl2,ing and
providing high SR trip protection when high in the SR.
(0.5)
l
l
12
.
- - - -
-
-
--
- -
-
--
_ _ _ _ _ _ _ _
.
_
.
.-
o
,
BRAIDWOOD CONTENTION:
6.02
Answer in the Key is incorrect.
The questions asks for IR instrument
response during a reactor Startup, not a shutdown as answered in the
key.
With an IR instrument undercompensated during a reactor startup, the
a.
P-6 setpoint (10 10 amps) will be reached early as a result of
counting neutrons and gammas.
The operator may secure the source
range instruments when P-6 comes in which results in no indication
of neutron flux below the IR range.
6.02
Response
The proposed response in the Braidwood contention is correct.
This
change was inadvertently omitted from the copy of the answer key
provided to the utility but was made to answer key prior to
administering the exam and all candidates were graded on this
basis.
QUESTION 6.06 (2.50)
List FOUR signals (that are not generated from the same protective
a.
bistable) which will initiate a motor driven Auxiliary Feedwater Auto
Start (AFAS) signal.
NRC ANSWER 6.06 (2.50)
a.
1.
Manual
2.
S/G Iow-low level on 1 steam generator
3.
Safety Injection sequence signal
4.
Undervoltage on Bus 141 (sequenced on)
5.
Undervoltage on 2/4 RCP buses (loss of offsite power)
(any four at .25 each)
(0.50)
BRAIDWOOD CONTENTION:
6.06
a.
There are not five Auto start signals, only four.
1.
2/4 Low-Low Steam Generator
level in any SG.
2.
UV on 2/4 RCP Buses (Loss of offsite power).
3.
(IA only) UV on Bus 141 (Sequenced only).
4.
SI signal
REFERENCE:
6.06
Response
The documentation provided to support this contention underlines
the confusion.
" Manual initiation (1/2 coincidence)" appears to
be separated from the three other safety injection signals.
Upon
13
f
,*
.
,
closer review, the " " mark instead of a "0"
shows that " manual"
-
is a cause of the SI signal, not the AFAS signal.
Logic diagrams
provided in the STM do not show which signal is the AFAS signal and
further confuse the answer.
Only one of 15 candidates listed
" manual" as a cause of an AFAS signal and therefore, the examiner
concluded that the training program provided sufficient
clarification on this answer.
Therefore, the answer " manual"
is deleted from the answer key.
The candidates must provide
4/4 signals that cause an AFAS signal for full credit.
QUESTION 6.08
b.
How is the minimum CST water volume required by Technical Specifications
ensured to be available at all times considering that several systems
take suction on the CST?
(0.5)
NRC ANSWER 6.08
b.
Other systems which use the CST have evaluated suction nozzles (which tap
in above the minimum required level).
(0.5)
BRAIDWOOD CONTENTION:
6.08 Part b.
By the T/S surveillance.
The CST does not have elevated nozzles supplying other systems.
REFERENCE: T/S 4.7.1.3.1.
General plan drawing of Equip Nos. ICD 01T.
t
6.08
Response
Tech spec basis 4.7.1.3 for the condensate storage tank implied
that there were elevated discharge lines or other " physical
characteristics" that cause water to be not usable for supply to
some systems.
It is typical throughout the industry for CST suction
lines to be elevated to ensure sufficient water volume will be
available to supply AFW to meet tech spec requirements for
operability.
Indeed, some discharge lines do have elevated
nozzles in the CST as shown in general DrawTrig ICD 01T.
However, based on general Drawing 1 CD01T recently supplied by the
licensee to support the contention (a drawing not included in the
references provided to prepare the exam) the answer is modified to
state:
b.
"By Tech Spec surveillance."
14
.
.
_
_
-
.
,
.
It should be noted that three of 15 candidates stated that the
CSF had elevated suction nozzles to ensure sufficient water was
available for AFW operability.
QUESTION 7.01 (2.25)
a.
18wEP.0 foldout lists three conditions (or sets of conditions) that
together require the operator to trip one or more RCPs.
What are these
conditions:
(1.25)
b.
What are the ERG bases for tripping the RCPs under these conditions (1.0)
(during a small break LOCA)?
ANSWER 7.01 (2.25)
a.
1.
Component cooling water to RCP lost (affected pump only)
(0.25)
2.
CNMT Phase B is actuated
(0.25)
3.
Both of the following conditions exist:
a.
RCS pressure is less than 1370 psig (1670 psig for adverse
containment)
(0.25)
and
b.
Coolant charging pump flow is greater than 200 gpm
(0.25)
or
Safety injection pumps have positive flow
(0.25)
BRAIDWOOD CONTENTION:
7.01
The question asks for " conditions that taken together require the
operator to trip RCPs".
This combined with the clarification of Part b. (that being the
'
small break loca) could have misled the examinee to believe the
answer to Part a would only be.
1. - RCS Pressure < 1370 (167C adverse)
and
'
2. - charging pump flow > 200 gpm
or
!
3.
positive SI flow
!
i
4
15
_- _.
_ . _ _ _ _ _ _
_ . _ . _ _ . . _ _ . _ - - _
_ _ _ _ _ _ _ _ - . _ _ _ _ - . _
._
. - -
_
1
.-
,.
7.01
Response
A large majority of the candidates did not find this question to be
confusing.
12 out of 14 candidates achieved full credit on Part "a"
of this question.
Of the two remaining candidates, one had initially
listed a full credit response and then lined our Answers 1 and 2.
-
Full credit has been given for his answers because:
1.
It is clear that he knew Parts 1 and 2 to the question answer
key.
2.
The word "together" probably did not cause confusion and he
lined out the answers after reading Part "b" of the question.
Deleting the first two answers to Part "a" would only penalize the
candidates unnecessarily.
QUESTION 7.03 (4.00)
a.
List four Mode 1 situations or conditions which require the operator to
commence EMERGENCY B0 RATION of the RCS.
(2.0)
NRC ANSWER 7.03 (4.00)
a.
1.
Failure of more than one RCCA to fully insert following a
2.
CRH below RIL
3.
Inadequate shutdown margin
4.
Unexplained or uncontrolled reactivity increase.
5.
Inability to borate normally.
(any four at .5 each)
BRAIDWOOD CONTENTION:
7.03
A sixth choice is an uncontrolled cooldown.
REFERENCE:
18w0A PRI-2 B.
SYMPTOMS OF ENTY CONDITIONS
7.03
Response
An " uncontrolled cooldown" is part of Answer 4, an " uncontrolled
reactivity increase."
Credit will be given of the operators provide specific conditions of
situations that are subsets of the general conditions in the answer
key provided these specific situations are not redundant.
The
16
1
.*
,
question did not require the candidate to list the six entry
conditions from the 18w0A Pri 2 B foldout and latitude will be
allowed for answers which are subsets of the general situation.
In addition, it should be noted that the Braidwood Systems
Training Manual Volume 2, Chapter 15b Appendix A does not include
uncontrolled cooldown as a separate situation or condition which
requires emergency boration.
QUESTION 7.07 (2.00)
a.
Complete the following statements regarding a reactor startup.
3.
Shutdown margin shall be greater than
delta k/k tech
spec limit) prior to commencing a startup.
(0.5)
NRC ANSWER 7.07 (2.00)
3.
1.3 delta k/k
(0.5)
REFERENCE:
BwGP 100-2, Pages 1, 2, 5, and 9
BRAIDWOOD CONTENTION:
7.07 a.3. Answer should be 1.3% ^k/k
REFERENCE:
BwGP 100-2, Page 1
Braidwood Tech. Spec. 3.1.1.1
7.07
Response
The "%" sign was omitted from the answer key by a typographic
error.
The answer key has been modified to accept the contention.
the correct answer is 1.3% ^K/K.
QUESTION 7.12 (2.00)
During a loss of all AC power, the operator must depressurize the RCS using
steam generator atmospheric relief valves at Step 16 of 18wCA-0.0.
How should these valves be operated without AC power and control air?
a.
(0.5)
NRC ANSWER 7.12 (2.00)
They have backup nitrogen accumulators and can be positioned from the
a.
control room.
(0.5)
17
.-
' ,.
,
BRAIDWOOD CONTENTION:
7.12
a.
By using the hand pump loss of AC Procedure BwCA-0.0
Step 16-b.
locally dump steam using PORV per Bw0A Pri 5.
Bw0A Pri 5 Step 20-b directs you to Bw0P MS-6.
Bw0P MS-6 Step 5, operate the remote hand pump to move to
Atmospheric Steam Pump.
7.12
Response
During a loss of all AC power, the steam generator atmospheric
relief valves may be operated in the emergency mode to fast close
the valve with a nitrogen accumulator as stated in the answer key
referenced in the Systems Training Manual Volume 3 Page 23-33.
The
Braidwood contention provides an alternative method of handpumping
the valve closed or open from a local operating station.
The answer
key has been revised to accept the following answer based on the
information supplied:
Remote manual mode --- If the atmosphere relief valves were to lose
power they could be manually opened with a hand pump in the safety
valve rooms.
(0.5)
QUESTION 8.03 (2.00)
a.
How many members per shift are required on the fire brigade.
(0.5)
b.
Who may NOT be included as members of the fire brigade?
(1.0)
NRC ANSWER 8.03 (2.00)
a.
five
(0.5)
b.
The fire brigade shall NOT include the minimum shift crew required'for
safe shutdown of Unit 1 (0.5) and any personnel required for essential
functions during the fire.
(0.5)
REFERENCE: BwAP 1100-1
BW Technical Specifications, Section 6
BRAIDWOOD CONTENTION:
8.03
a.
Answer should be five, or cognizant Shift Foreman and remaining
four members composed of four of the following personnel:
Equipment Attend?nts, Equipment Operators.
Reference:
BwAP 1100-1, Rev. O, Page 7.
,
b.
Another answer that should be allowed is:
1-SE, 2-NSP's,
3-EA's, and 1 SCRE/STA.
REFERENCE:
BwAP 320-1, Page 2
18
_
__.
_ _ - _ - _
_
--
_ .__
. _ _ _ _ _ _ _ . _ _ _
_ . . _ _ _ .
f
,.
. . , ,
8.03
Response
The Braidwood contention is a subset of the more general answer
provided.
If the candidate provides the specific list by job
title, full credit will be give. However this information is
neither required nor asked for to receive full credit.
QUESTION 8.07 (3.00)
List SIX conditions or occurrences that require notification of the NRC within
ONE hour.
NRC ANSWER 8.07 (3.00)
1.
Declaration of any emergency classification.
2.
The initiation of any plant shutdown required by Technical
Specifications.
3.
Any authorized deviation (10 CFR 50) from Technical Specifications.
4.
Any event or condition during operation that results in the condition of
the plant or safety barriers being seriously degraded, or results in the
plant being:
a.
In an unanalyzed condition that significantly compromises plant
safety, or
b.
In a condition that is outside the design basis of the plant, or
c.
In a condition not covered by the plant's operating and emergency
procedures.
5.
Any natural phenomenon or external condition that poses an actual
threat to safety of plant or significantly hampers site personnel
while performing duties required for safe operation of the plant.
6.
Any event that results or should have resulted in ECCS actuation on a
valid signal.
7.
Any event that results in a major loss of emergency assessment
capability.
.
8.
Any event that poses an actual threat to the safety of the plant of
significantly hampers site personnel while performing duties necessary
for safe operation of the plant including fires, toxic gas releases, or
radioactive releases.
9.
Any violation of a safety limit.
(any six at 0.5 each)
!
(No. 4 counts as four separate conditions)
19
,
'l
j
.
,
BRAIDWOOD CONTENTION:
8.07 Addition correct answers should include:
10.
Exposure of the whole body of any individual to 25 rems or more of
radiation; exposure of the skin of the whole body of any individual of
150 rems or more or radiation; or exposure of the feet, ankles, hands or
forearms of any individual to 375 rems or more of radiation; or
11. The release of radioactive material in concentrations which, if averaged
over a period of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, would exceed 5,000 times the limits specified
for such materials in Appendix B, Table II of this part; or
12.
A loss of one working week or more of the operation of any facilities
affected; or
13.
Damage to property in excess of $200,000.
REFERENCE:
8.07
Response
The 10 CFR 20.403 events require "immediate notification" of the
NRC not notification within one hour.
However, it is clear from
the candidate responses that the 10 CFR 20.403 conditions were
emphasized in the training program.
Based on the candidate response
and the documentation provided, the 10 CFR 20.403 events have been
included in the answer key for this question.
QUESTION 8.08 (1.00)
Complete the following statement with one of the provided terms.
Seal leakoff from the RCP No. 2 seal which is collected in the RCDT is
classified as
leakage.
a.
Controlled
b.
Pressure Boundary
,
c.
Identified
d.
Unidentified
i
NRC ANSWER 8.08 (1.00)
a.
(1,0)
BRAIDWOOD CONTENTION:
8.08
Tech Spec's define controlled leakage as that seal water flow
supplied to the RCP seals.
The No. 2 seal leakoff is collected in
the RCOT, which infers that it is Identified Leakage in recordance
with the Tech Spec. definition.
Therefore, the appropriate answer
is "c" - identified leakage.
20
. - . -
- . . -
.---
. - - . - - - - - .
. -
. . - - - - _ . . - . - . -
- -
.
-
._-
-
.
--
-.
-
.
.. ,t,*.
REFERENCE:
Braidwood Tech Spec's Braidwood STM Chapter 13 Page 18.
>
8.08
Response
4
The term, " controlled leakage" is specifically reserved for the
seal water from reactor coolant pump seals because the leakage is
predetermined and controlled by ensuring that the gap between the
seal ring and runner is maintained constant.
The seal water
supplied to reactor coolant pump seals is also the same seal water
that lubricates and leaks by these seals. No distinction should be
4 -
drawn between the water going into the coming out of the seal
!
boundary (or else you will count this leakage twice).
The RCP No. 2 seal leakoff, although collected in the RCDT, cannot
.
{
be identified leakage because the definition of identified leakage
specifically excluded controlled leakage. The licensee has
'
interpreted the tech spec definition too literally.
The answer is
correct as provided in the answer key.
1
Reference:
BW Tech Spec Definition 1.8 and 1.15
j
BW STM Vol 2 Page 13-15 Paragraph 2
]
QUESTION 8.12 (1.00)
1
!
The Acting Station Director declares a general emergency event based on LOCA
l
into containment with a failure of ECCS to actuate.
No releases of
l
radioactive materials has occurred.
a.
What protective actions, if any, would the Acting Station Director
recommend to the offsite civil authorities?
(0.5)
1
NRC ANSWER 8.12 (1.00)
il'
a.
Shelter the two mile radius and five mile downwind sectors.
(0.5)
!
j
BRAIDWOOD CONTENTION:
)
>
At Braidwood we enforce that is it of the utmost importance that the SR0 be
aware of the fact that a plan exists for protective actions to be taken in the
i
event of a general emergency, and tnat he be able to locate and implement this
4
plan in a timely manner. We do not, however, believe or instruct that the
candidate should be required to commit to memory the chart in our BwZP's which
outlines the protective action guidelines for a general emergency.
Therefore,
we contend that this portion of the question is beyond the scope of required
material for SRO knowledge and the question should be deleted,
f
8.12
Response
l
The declaration of a general emergency classification at Braidwood
i
automatically requires that the SR0 assumes the role of Acting
Station Director, activate the GSEP and recommend protective
'
actions to the general public. The BWZP 380-4A2 Appendix B
Figure 6.3-1 flow chart provides detailed guidance, as mentioned in
!
4
21
E-_...,______._..____.___________
.
. .
.* 1 f
,
the contention, to determine protective action recommendations (PARS)
and certainly should not be committed to memory.
The correct answer
does not require the candidate to memorize this complicated flow
chart.
However, the intent of this question was to determine if the
candidate know that:
1.
Upon declaring a general emergency, there is only one set of
PARS that should be recommended immediately, and
2.
These PARS are to shelter the two mile radius and five mile
downwind sectors.
This basic level of knowledge is required for SR0s to demonstrate
adequate familiarity with the emergency plan.
The correct answer
did not require the candidate to specifically detail the NARs
paragraph numbers from the flow chart.
Instead, the candidate was
tested on his understanding of the basic concepts of protecting the
general public from exposure to accident release levels of radiation
by immediate sheltering of population at the general emergency
declaration.
NUREG-1122, Knowledges and Abilities Catalogue, assigned one of
to the candidates " ability
thehighestimportanceratings(4.7/5.0)tyEmergency
to take actions called for in the Facili
including . . . acting as the Emercency Plan Coordinator"
Acting Station Director) (Plant-Wice Generic K/A 36, Page 2-3)..e., The
candidate must have more than a cursory knowledge of PARS to meet
this ability and, therefore, this level of knowledge is appropriate
for SR0s.
QUESTION 8.14 (2.50)
When conducting valve lineups, the valve position must be determined by the
operator. How would the operator verify valve position on the following types
of valves?
e.
Manual valve in a throttled position.
(0.5)
NRC ANSWER 8.14 (2.50)
i
!
e.
Close valve counting the number of turns until the valve seats, restore
the valve to its proper position by pening it the same number of turns
that is was closed (check at facilit ).
(0.5)
BRAIDWOOD CONTENTION:
8.14
As requested, the reference for Answer "e" is BwAP 340-2 Rev. 0,
Page 3.
l
l
l
22
,
L
. .* );
8.14
Response
IBWAP 340-2 Page 3 Item 6 does not provide an explicit statement of
action to the operator conducting the value line up regarding how to
check the position of a throttled valve.
This was pointed out to
the licensee is both the answer key provided and in person to the
training department.
The examiner requested that the licensee
provide an explicit answer that paralleled the phraseology used
in BWAP 340-2 Page 3 Items 1, 2, 3, 4 and 5.
Instead, the training
department response was to provide a copy of the page of the
administrative procedure that the examiner had already referenced
in the answer key and had considered an inadequate answer to the
question.
Further discussions with the licensee have indicated that the
following answer is correct.
Answer:
1.
If the throttled valve position is listed on the valve line up
sheet by number of turns, then . . . (use answer key provided
to facility).
2.
If the throttled valve position is listed by stem position (%
travel on other indication) then the operator should compare
the indicated position with the valve line up sheet valve.
The operator should not operate the valve.
The key element required in 'this question was to see if operators
understood when to operate a throttle valve to check its position.
The examiner does not expect that the operators have memorized the
sentence in BWAR 340-2 Page 3 Item 6.
The successful answer should
have an action statement regarding how to check throttle valve
position that demonstrates their knowledge of the required actions
analogous to the action statements for manual valves.
If the candidate assumed that valve position was given by the number
of turns, then full credit was given for Answer 1.
If the candi gte
-
assumed that valve position was given by a stem position indicatig'n,
then full credit was given for Answer No. 2.
23
/
r
B99 AN C. Hm6ENsaJ
- T
. T
$ g4.g( } }l
..
,
,
,
r
'
b
'
.
U. S. NUCLEAR REGULATOR
'
,
SENIOR REACTOR OPERATOR LICENSE EXAMINATION
,m,[ Q
FACILITY:
BRAIDWOOD 182
6
REACTOR TYPE:
PWR-WEC4
\\
= ped smocle, DATE ADMINISTERED: 86/10/22
-
b
EXAMINER:
HAAGENSEN, B./REIDIN
eErde. traole.
-
M w 4so. y. CANDIDATE:
INSTRUCTIONS TO CANDIDATE:
Use separate paper for the answers. Write answers on one side only.
Staple question sheet on top of the answer sheets.
Points for eac'.
question are indicated in parentheses af ter the question. The passi :
grade requires at least 70% in each category and a final
grade of at
least 80%. Examination papers will be picked up six (6) hours after
the examination starts.
% OF
CATEGORY % OF
CANDIDATE'S CATEGORY
VALUE
TOTAL
SCORE
VALUE
CATEGORY
674.S~o .zy.c zt
M
25:00
5.
THEORY OF NUCLEAR POWER PLANT
"
OPERATION, FLUIDS, AND
THERMODYNAMICS
25"I3%
25.00
.2&:00
6.
PLANT SYSTEMS DESIGN, CONTROL,
AND INSTRUMENTATION
75.G%
25.00
JLOG
7.
PROCEDURES - NORMAL, ABNORMAL,
EMERGENCY AND RADIOLOGICAL
CONTROL
-
A5.)3$
l
25.00
,,2kCD
8.
ADMINISTRATIVE PROCEDURES,
CONDITIONS, AND LIMITATIONS
9750
,,100:07
Totals
,
Final Grade
All work done on this examination is my own.
I have neither given
nor received aid.
Candidate's Signature
._ -
_
. _ .
--. .-
__
_-
r
..
.
'
.
NRC RULES AND GUIDELINES FOR LICENSE EXAMINATIONS
.
.
.
o
- During the administration of this examination the following rules apply:
1.
Cheating on the examination means an automatic denial of your application
and could result in more severe penalties.
2.
Restroom trips are to be limited and only one candidate at a time may
leave. You must avoid all contacts with anyone outside the examination
room to avoid even the appearance or possibility of cheating.
3.
Use black ink or dark pancil only to facilitate legible reproductions.
4.
Print your name in the blank provided on the cover sheet of the
examination.
5.
Fill in the date on the cover sheet of the examination (if necessary).
6.
Use only the paper provided for answers.
7.
Print your name in the upper right-hand corner of the first page of each
section of the answer sheet.
8.
Consecutively number each answer sheet, write "End of Category
" as
appropriate, start each category on a new page, write only on one side
of the paper, and write "Last Page" on the last answer sheeE
9.
Nunt>er each answer as to category and number, for example,1.4, 6.3.
10. Skip at least three lines between each answer.
11. Separate answer sheets from pad and place finished answer sheets face
down on your desk or table.
12. Use abbreviations only if they are connonly used in facility literature.
13. The point value for each question is indicated in parentheses after the
question and can be used as a guide fer the depth of answer required.
14. Show all calculations, methods, or assumptions used to obtain an answer
to mathematical problems whether indicated in the question or not.
15. Partial credit may be given. Therefore, ANSWER ALL PARTS OF THE
QUESTION AND 00 NOT LEAVE ANY ANSWER BLANK.
16. If parts of the examination are not clear as to intent, ask questions of
the examiner only.
17. You must sign the statement on the cover sheet that indicates that the
work is your own and you have not received or been given assistance in
l
completing the examination. This must be done after the examination has
been completed.
.
,
-.
-
.
-
-
I
.
.
NRC RULES AND GUIDELINES FOR LICENSE EXAMINATIONS
.
During the administration of this examination the following rules apply:
.-
, ,
1.
Cheating on the examination means an automatic denial of your application
and could result in more severe penalties.
l
2.
Restroom trips are to be limited and only one candidate at a time may
leave. You must avoid all contacts with ayone outside the examination
room to avoid even the appearance or possibility of cheating.
3.
Use black ink or dark pencil only to facilitate legible reproductions.
4.
Print your name in the blank provided on the cover sheet of the
examination.
1
'
5.
Fill in the date on the cover' sheet of the examination (if necessary).
6.
Use only the paper provided for answers.
7.
Print your name in the upper right-hand corner of the first page of each
section of the answer sheet.
8.
Consecutively nunber each answer sheet, write "End of Category
" as
appropriate, start each category on a new page, write only on oni side
of the paper, and write "Last Page" on the last answer shee't7
9.
Number each answer as to category and number, for example,1.4, 6.3.
10. Skip at least three lines between each answer.
11. Separate answer sheets from pad and place finished answer sheets face
down on your desk or table.
'
12. Use abbreviations only if they are cosanonly used in facility literature.
13. The point value for each question is indicated in parentheses after the
question and can be used as a guide for the depth of answer required.
14. Show all calculations, methods, or assumptions used to obtain an answer
to mathematical problems whether indicated in the question or not.
15. Partial credit may be given. Therefore, ANSWER ALL PARTS OF THE
QUESTION AND DO NOT LEAVE ANY ANSWER BLANK.
16. If parts of the examination are not clear as to intent, ask questions of
the examiner only.
17. You must sign the statement on the cover sheet that indicates that the
work is your own ar.d you have not received or been given assistance in
completing the examination. This must be done after the examination has
been completed.
- _ . - _ _ _ _ _ . _
.
.
.
.
_
_-
'
'
-
3
-
,
,
1
18. When you tompIete ko*ur examination, you shall:
'
-
-
.
a.
Assemble your examination as follows:
(1) Exam questions on top.
(2) Exam aids - figures, tables, etc.
(3) Answer pages including figures which are part of the answer.
b.
Turn in your copy of the examination and all pages used to answer
the examination questions.
,
c.
Turn in all scrap paper and the balance of the paper that you did
not use for answering the, questions.
d.
Leave the examination area, as defined by the examiner.
If after
leaving, you are found in this area while the examination is still
in progress, your license rey be denied or revoked.
1
,
- -. .
- - . - - -
- -
. . -
5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE
2
,,
THERMODYNAMICS
-
.
.
4
QUESTION 5.01
(1.00)
During a reactor startup, the first reactivity addition caused count rate
to increase from 20 cps to 40 cps. The second reactivity addition caused
count rate to increase from 40 cps to 80 cps. Which of the following
statements is CORRECT?
a.
The first reactivty addition was larger,
b.
The second reactivity addition was larger.
c.
The first and second reactivity additions were equal.
d.
There is not enough data given to determine relationship of reactivity
values.
QUESTION 5.02
(1.50)
TRUE or FALSE?
a.
As Keff approaches unity, a smaller change in neutron level will result
frora identical changes in Keff.
(0.75)
b.
With Keff greater than unity, a constant positive startup rate with
increasing neutron level will occur only if net REACTIVITY is NOT
changing.
(0.75)
QUESTION 5.03
(2.00)
a.
List the three most significant contributors to total power coefficient
in order of INCREAS M ma nitude at BOL.
(1.5)
b.
How does total power coefficient vary from beginning to end of core
life?
(0.5)
70&dunTA gmyn,
-
CWL :
1.
O.
m
3. M
(***** CATEGORY 05 CONTINUED ON NEXT PAGE *****)
.-.
..
. - - - - - . . - - -- - - - - - -
--
. . . -
- - - -
- - - -
- '
__
,
.
5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE
3
.
THERMODYNAMICS
.
,
.
4
QUESTION 5.04
(1.50)
i
a.
List TWO reasons why critical boron concentration decreases over core
life.
(1.0)
b.
How does moderator temperature coefficient vary as boron concentration
decreases? ( Assome qIlother R(,$ Parame,Y ers 4rg held (0.5)
f.On$t, trit) ,
QUESTION 5.05
(3.00)
For the following situations, indicate whether the final stable
power level will be HIGHER, LOWER, or THE SAME as the initial
power level. EXPLAIN your answers. List coefficients if applicable.
Assume the initial power level is at approximately 5% following a normal
reactor startup at the end of life and the steam dumps are open. Consider
each situation separately,
a. Steam dump pressure setting is lowered by 20 psig while in Steam
Pressure mode.
(1.0)
b. A small (500,000 lbm/hr) main steam leak develops inside containment
that is insufficient to initiate SI.
(1.0)
c. RCS boron concentration is increased by 20 ppm.
(1.0)
1 % O h 8 ---. kTQ
'
4 6 - 4 - - m , ex g ?
.p
3. cm sov, A d
p
(***** CATEGORY 05 CONTINUED ON NEXT PAGE *****)
_,
-
.
.
.
- - . _
_
- - - - ~ . . _
5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE
4
.
THERMODYNAMICS
-
.
-
1
~
\\
.
4
QUESTION 5.06
(1.50)
Compare the calculated Estimated Critical Rod Position (ECP) for a
startup 15 hours1.736111e-4 days <br />0.00417 hours <br />2.480159e-5 weeks <br />5.7075e-6 months <br /> after a trip to the Actual Critical Rod Position
(ACP) if the following events / conditions occurred. Consider each
independently. Limit your answer to:
c. ACP is unchanged.
1. Actual RCS temperature is 551 F at critical
ty.
(0.5)
2. The steam dump pressure setpoint is increased to a value just
below the steam generator atmospheric relief setpoints.
(0.5)
3. The startup is delayed 2 more hours.
(0.5)
QUESTION 5.07
(?.00)
State the definition of Shutdown Margin \\ ptv7tek $pecs,
(1.0)
a.
b.
The plant is operating at 85% power with all systems in automatic.
The operator inadvertently aligns charging pump suction to the RWST.
How is shutdown margin affected PRIOR to a reactor trip?
(1.0)
(Increase, decreape, remains the same)
8' O * p M ' %
wk } ----# /T)g
QUESTION 5.08
(1.50)
The plant is operating at 100 % power with RCS Tave at 587 F
and a steam pressure of 98Qito in order to maintain th J. _g T n ; with 10 % of the tubes
What must TAVE be changed
..
any applicable formulas. [k' /
in each steam generator p ugged? SHOW ALL WORK, including
e
t
s
(***** CATEGORY 05 CONTINUED ON NEXT PAGE *****)
._
__~
. _ -
-_
. _
- . - -
- -
5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE
5
.,
THERMODYNAMICS
.
,
l
.
.
QUESTION 5.09
(1.00)
.
Choose the CORRECT response.
In order to maintain a 200 F subcooling
margin in the RCS when reducing RCS pressure to 1600 psig, steam generator
pressure must be reduced to approximately:
a.
405 psig
b.
325 psig
c.
245 psig
d.
165 psig
QUESTION 5.10
(2.00)
Will the Departure from Nuclear Boiling Ratio (DNBR) INCREASE,
DECREASE, or REMAIN THE SAME if the following plant parameters
INCREASE during power operation? Consider each parameter
independently,
a.
Reactor Coolant System (RCS) Pressure
(0.5)
b.
RCS Temperature
(0.5)
c.
RCS Flow
(0.5)
d.
Reactor Power
(0.5)
.
(***** CATEGORY 05 CONTINUED ON NEXT PAGE *****)
.
_ . - - . . - . - _ _ , ,
- . . - _ . _ _ - _ . - , , ,
-
--.__y,.
,,
_ _ _ - . - . - - ,__,, , . , _ . - - - , . - , ,
, , _ , . - - - -
-
,
-
5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE
6
-
THERMODYNAMICS
.
.
~
.
,f. O
QUESTION 5.11
M
a.
Describe how natural circulation causes flow in the RCS. Explain
thermal driving head (delta-P driving head) is created in the RCS.(1.0)
"
Z.;r, ,;tur:1 ci. ;;1; tier i; ;;t bli;t.cd ir, tt,; "CS, w fle., . et; e'
..
t;e ewler.t i; pr:pe-t'aa=1
+a-
4
(0.5)
1.
(delta-T)
g
2
2.
(delta-T)
3.
(delta-f)
- CO*2
%
4.
1/(delta-T)
c.
The reactor is producing 100% rated thermal power at a core delta-T
of 60 degrees and a RCS mass flow rate of 100% when a station blackout
occurs. Natural circulation is established and core delta-T goes to
28 F.
If decay heat is 2%, what is the core mass flow rate (in %)?
(1.0)
QUESTION 5.12
(2.00)
Indicate whether the following situations result in SUBC00 LED, SATURATED,
or SUPERHEATED fluid conditions.
-
a.
Steam from pressurizer PORY relieving to the PRT.
(0,5)
b.
Steam from a steam ger.erator safety valve relieving to atmosphere.
(0.5)
c.
Steam from a Moisture Separator Reheater entering a low pressure.
turbine
(0.5)
d.
Condensate exiting the condenser hotwell.
(0.5)
QUESTION 5.13
(1.0)
It is observed that reactor coolant flow through a stean generator is
aphroximately 10 TIMES the feedwater flow into the same steam generator.
)
Hcwever, the feedwater delta-T in that steam generator is only twice the
-
RCS delta-T. What accounts for this apparent heat transfer mismatch?
(***** CATEGORY 05 CONTINUED ON NEXT PAGE *****)
_
.
--
_
_
_ . _ . - _ . - _ _ _ , , .
..
5.
THEORY OF NUCLEAR POWER PL ANT OPERATION, FLUIDS, AND
PAGE
7
.
-
-
THERMODYNAMICS
.'
.
QUESTION 5.14
(2.50)
a.
The reactor is subcritical by 2500 PCM. The count rate is 115 CPS.
After a positive reactivity insertion, the count rate increases
to 345. How much reactivity was added to the core?
(1.5)
b.
Why does it take longer, after each reactivity addition, for the
neutron population to reach equilibrium as Keff approaches 1.07 (1.0)
.
(***** END OF CATEGORY 05 *****)
!
-
.
-
.
~ -
- _ - - -------- -
- - - - - - - - - - -
- - - -
6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUENTATION
PAGE
8
..
.
.
.
.
.
QUESTION 6.01
(1.50)
The plant is operating at 100 % steady state power with
containment pressure channel IV (PB 934A) failed high. A
technician troubleshooting the trip bistables inadvertently
de-energizes the instrument power for containment pressure
channel II. Will a Containment Spray Actuation occur?
(0.5)
,
'
WHY or WHY NOT?.
(1.0)
G4WL : .i _2RM4
QUESTION 6.02
(2.00)
7
Q
"f
(, 2. G
l .I R
i
a.
Describe an IR instrument response if the circuitry is
undercompensated while performing a reactor startup, including any
effects on SR instrumentation.
Include any applicable
setpoints.
(1.0)
b.
Operator action is required to continue a reactor
shutdown if one IR channel has failed high .
(1.0)
1.
List the actions that are required.
2.
Why are these actions necessary?
QUESTION 6.03
(2.50)
State how the following components respond (FAIL OPEN, FAIL CLOSED, REMAIN
FUNCTIONAL, DIVERTS TO .... ETC.) when instrument air pressure is lost with
the plant at 100% power.
a.
Letdown pressure control valve (PCV-131)
(0,5)
b.
Volume control tank level control valve (LCV-112A)
(0.5)
c.
Steam generator atmospheric relief valves
(0.5)
d.
Pressurizer PORVs
(0.5)
e.
Auxiliary feedwater regulating control valves
(0.5)
(***** CATEGORY 06 CONTINUED ON NEXT PAGE *****)
-
-
- , _ - _ - . _ _ . - - . _ . - . _ - - - - -
- _ -
-
_
.
6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUMENTATION
PAGE
9
,,
-
.
.
~
.
QUESTION 6.04
(2.00)
Indicate which of the Excore Nuclear Instrumentation Ranges
(SOURCE, INTERMEDIATE, or POWER), will correctly match with
the following statements. More than one may apply to each.
a. Provides signal input to generate P-10 permissive
b. Provides signal input to generate C-1 control signal
c. Utilizes a Boron-10 coating in it's detectors.
d. Operates in the " Ion Chamber" region of the " Gas Filled
. Detector Characteristic Curve".
QUESTION 6.05
(2,50)
The following questions concern the CVCS.
a.
What are the TWO functions (purposes) of the Letdown Pressure
Control Valve (PCV-131)?
(1.0)
b.
If lef t in automatic control, what position should PCV-131
be found in two minutes after a safety injection initiation?
(0.5)
c.
Why is letdown flow limited to 120 gpm?
(0.5)
d.
With only the positive displacement pump operating at power, which
valve (s) is/are utilized to control RCP seal injection flow? (Noun
name(s) or number (s) is/are acceptable.)
(0.5)
QUESTION 6.06
(2.50)
a.
List FOUR signals (that are not generated from the same protective
bistable) which will initiate a motor driven Auxiliary Feedwater Auto
Start (AFAS) signal.i,),
M
- gh ,
)
%
With an AFAS signal initiated, HOW and WHEN is the Auxiliary Feed pump N
b.
water supply shif ted from the Condensate Storage Tank to the Essential
Service Water System by operator action?
(.0. 5 )
c.
What signals would cause the Condensate Storage Tank suction shif t
automatically to the Essential Service Water System if operator action
was not taken?
(2.0)
(***** CATEGORY 06 CONTINUED ON NEXT PAGE *****)
- - _ .
_ _ _ _ .
_
.
6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUMENTATION
PAGE 10
-
.
.
.
.
.
QUESTION 6.07
(1.60)
Match the following symptoms or causes in column "B" to the specific Rod
Control System failure or error in column "A".
"A"
"B"
a.
Logic Cabinet Urgent Failure
1. Caused by simultaneous zero
current order to stationary and
movable grippers.
b.
Regulation failure
2. Unselected rod (s) having current
flow in movable or lift coils,
c.
Phase failure
3. Caused by failure of redundant
power supply module.
d.
Logic error
4. Caused by oscillator or slave
cycler failure
5. Caused by full current being
applied for excessive time.
(There is only 1 correct numerical
6. Occurs when voltage to coils has
answer for each lettered error or
excessive ripple.
failure at 0.4 each)
QUESTION 6.08
(1.50)
a.
Describe the safety-related function (tech spec basis)
of the Condensate Storage Tank.
(1.0)
b.
How is the minimum CST water volume required by Technical
Specifications ensured to be available at all times considering that
several systems take suction on the CST?
(0.5)
QUESTION 6.09
(2.00)
a.
List two trending indications or symptoms which will be observed in the
control room if a tube leak occurs in a RCP thermal barrier heat
exchanger. Assume NO alarm setpoints are reached,
g,
- u .u r
b.
If the tube leak
action will occur,gntinues to increase in severity, what AUTOMATIC
.d6 wi"
w ,,, ; . . . .. ; ,. c ;0; cff ;t r. th '
w,
r;;t Of th: CC" ;;;t:"
-
(1,0)
(***** CATEGORY 06 CONTINUED ON NEXT PAGE *****)
-.
- -_.
._ _
6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUMENTATION
PAGE 11
.
.
.
.
.
.
.
.
QUESTION 6.10
(1.00)
Following a loss of offsite power with a safety injection signal, which of
the following abnormal conditions, if occurring separately, will result in
a diesel generator trip? (More than one answer may be correct.)
a.
Excessive vibration
b.
High generator differential current
c.
Generator reverse power
d.
Low lube oil pressure
e.
f.
High jacket water temperature
QUESTION 6.11
(1.50)
Select from the following list of electrical loads, THREE loads which would
automatically deenergized following the loss of the 156 bus,
a.
Centrifugal charging pump #1A
b.
Reactor coolant pump #1B
c.
Steam generator feedwater pump 1A
d.
Containment spray pump #1A4
e.
Heater drain pump IB
f.
Circulating water pump 1B
g.
Service air compressor #1
(***** CATEGORY 06 CONTINUED ON NEXT PAGE *****)
. _ _ .
__
. _ _
_
._ __._ -
.
_ - -
.
_ --
.
6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUE NTATION
PAGE 12
i
.
.
.
.
.
.
.
QUESTION 6.12
(2.00)
The plant is operating at 100% power with all control systems in automatic.
Bank D rods are at 200 steps. Given the following conditions / situations,
how will rod height be affected (INCREASE, DECREASE, NO CHANGE)? Assume no
operator action and consider each case separately. Assume the reactor does
NOT trip.
a.
C-5 control signal actuates.
(0.5)
b.
C-3 control signal actuates.
(0.5)
c.
C loop narrow-range Tcold instrument fails low.
(0.5)
d.
Turbine load is reduced to 80%
(0.5)
QUESTION 6.13
(1.40)
The reactor is critical at the point of adding heat. List SEVEN reactor
trips which are DISABLED in this condition.
QUESTION 6.14
(1.00)
The plant is critical at the point of adding heat during a reactor startup.
A malfunctioning steam header controller (air signal to SDYs failed to FULL
OPEN value) causes six stesm dump valves to fully open. Assuming no
operator action and the reactor does not trip;
What average temperature will the reactor stabilize to?
(0.5)
Explain why the plant will stabilize at this temperature.
(0.5)
$ $ (Aa,$ 8 60c m GOL.
= m RTQ
1, e m r
0
-H, x_
- - , , . .
..
.
,
(**** * END OF CATEGORY 06 ***** )
-_
. _
_ -
. -
.-
-- - .-
-
-
- ___ .__-_
.
_ - _ _ - _
-
.
._-
-
.
-
7.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 13
RADIOLOGICAL CONTROL
,
,
.
.
QUESTION 7.01
(2.25)
a.
IBWEP.0 foldout lists three conditions (or sets of conditions) that
together require the operator to tripM1 RCPs. What are these
conditions?
04 er mort
(1.25)
b.
What are thf ERG bases for tripping the RCPs under these
(1.0)
conditions %kors*n
smg)) h go,h, LotA}P
e k Con M m M Q,
[#
58A
I
"
N
hRb h
'
QUESTION 7.02
(1.00)
m.Jei
M .hu.4 % '
List four (4)4 entry conditions from the emergency procedures which require
transitioning to IBWEP-3, Steam Generator Tube Rupture?
C A $ a h r A g.r K C A m h l, 6 u # t @ x e -
7An. v G Ta -A.P t d a% AWJEF0*
k
r
(L.00)
QUESTION 7.03
% Jet
List FOUR situations or conditions which require the operator to
a.
4
commence EMERGENCY B0 RATION of the RCS.
(2.0)
b.
List the borated water sources and flow paths to be used during
EERGENCY B0 RATION.
(2.0)
i
!
QUESTION 7.04
( .50)
Select the group of indications / parameters which provide verification of
j
natural circulation flow in the RCS.
CORE EXIT
SUBC00 LING
PRESSURES
Thot
Tcold
THERMOCOUPLES
3074t GPTNnstant
Decreasing
Decreasing
Increasinj
a.
b.
AS-E
Decreasing
Constant
Constant
Increasing
c.
.30-f
Constant
Decreasing
Constant
Decreasing
d.
26-F
3,
Decreasing
Increasing
Decreasing
Increasing
e .
--0-f'
Constant
Constant
Constant
Decreasing
W Accghtscr
(***** CATEGORY 07 CONTINUED ON NEXT PAGE *****)
- -__. .
-_ -
_ . - - _ .
- -
. - .
. - - -
-
-
.
7.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 14
,
RADIOLOGICAL CONTROL
.
,
,
.
.
~
.
QUESTION 7.05
(1.00)
'
TRUE or FALSE?
a.
The boron concentration monitoring system readout on the main control
board may be used for verifying proper dilution or boration operations.
(0.5)
b.
Operation in the ALTERNATE DILUTION mode should be limited to
approximately 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> to prevent hydrogen depletion in the RCS.
(0.5)
QUESTION 7.06
(3.00)
Supply the following which must be observed during plant operation in
accordance with Braidwood OPERATING PROCEDURES.
a.
Maximum RCS heatup rate (tech specs)
b.
Maximum RCS cooldown rate (tech specs)
c.
Administrative limit for RCS heatup rate
d.
Administrative limit for RCS cooldown rate
e.
Maximum boron concentration differential between RCS and pressurizer
f.
Maximum differential temperature between pressurizer and spray fluid
(0.50 each answer)
d
M2 %- d!'f;rci,t:ai
..ys. .tue
,s i
ss.. pce. art::. or.d ;prg #}f{
nu.m
QUESTION 7.07
(2.00)
a.
Complete the following statements regarding a reactor startup.
1.
Manually tripping reactor trip breakers will cause a feeditater
isolation if RCS tegerature is less than
F.(0.5)
2.
The water hammer flush should not be initiated until two conditions
are met. List those conditions (from BWGP 100-2).
(0.25each)
3.
Shutdown margin shall be greater than
delta k/k tech
spec limit) prior to comencing a startup.
(0.5)
b.
What alarm is(are) expected to clear AS A RESULT OF Group A control rods
reaching 6 steps. (0.5)
(***** CATEGORY 07 CONTINUED ON NEXT PAGE *****)
. - -
-
_ _
__ ._
__
,
.
7.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 15
RADIOLOGICAL CONTROL
.
.
.
.
-
.
QUESTION 7.08
(1.50)
a.
List the TWO criteria to reinitiate safety injection after SI has been
terminated in IBWCA-2.lgUncontrolled Depressurization of all Steam
Generators.
f.Qeo(;,
(0.5 each)
b.
IBWFR-H.1, response to Loss of Secondary Heat Sink, should be
implemented if a total feed flow capability of
gpm is
not available at any time during an Uncontrolled Depressurization of
all Steam Generators.
(0.5)
QUESTION 7.09
(1.00)
Which of the following operator actions i
among the immediate actions
of-CO O.0, Reactor Trip or Safety Injection?
SIDEMmay be more than one)
a.
Check if steam generators are not faulted.
b.
Check if main steamlines should be isolated.
c.
Verify diesel generators running.
d.
Verify containment spray not required.
e.
Verify ECCS flow.
Y
AY
.
QUESTION 7.10
(2.50)
a.
List the tech spec limits for RCS specific activity.
(2 limits) (1.0)
b.
are
entry conditions for IBWOA PRI-4 High Reactor Ckolant
liittJ 6 elm. Fr// in fhe 1/<
(1.5)
activity " ^^ ""
)
I. Ap rad Ak.o /ert er ./.em f, a. A
(og)
A r.Jigtian aled: or a l4*m or in c.r e
'm
,
o, ni,Jibac.tidty fi..m Sny
(0.f)
-
r*
3. Ostly bds gsmms ssmple grtdtr. % _
0E.
,
c14J~
L.A p#r#2: % .J,,JJ.6,.fL e 4 4
(***** CATEGORY 07 CONTINUED ON NEXT PAGE *****)
.
.
.
.
. =
,
-
.
_
. _ _ . .
7.
PROCEDURES - NORMAL, ABNORMAL, EMERGENCY AND
PAGE 16
.,
RADIOLOGICAL CONTROL
.
.
.
.
.
.
.
QUESTION 7.11
(3.00)
1.
Fill in the emergency dose limits on your answer sheet for the
following situations:
a.
Whole body dose to save a life
?
(0.5)
b.
Whole body dose to protect facilities,to stop serious relense of
effluents or to control fires
?
(0.5)
)
,
2.
Whenver possible, the prior approval of three individuals shall be
obtained prior to exposing personnel to emergency limits. List these
three persons by title.
(0.5 each)
3.
TRUE or FALSE?
Emergency exposure limits may only be imposed for personnel who have
volunteered for the emergency task.
(0.5)
QUESTION 7.12
(2.00)
During a loss of all AC power, the operator must depressurize the RCS
using steam generator atmospheric relief valves at step 16 of IBWCA-0.0.
.
a.
How should these valves be operated without AC power and control air?
'
(0.5)
b.
Why must the RCS be depressurized?
(0.5)
c.
Why shouldn't the RCS be depressurized below
hgsig?
(0.5)
j
d.
Regarding the depressurization, how should the operator respond if
pressurizer level is lost or vessel head voiding occurs?
(0.5)
4
QUESTION 7.13
(1.25)
Bw0A PRI-9(Loss of Shutdown Cooling) instructs the operator to establish
alternate decay heat removal if BOTH RHR trains should fall and NOT be
capable of restoration to operability.
a. List the two alternate decay heat removal methods provided in the
procedure if RCS temperature is 300 F, RCS pressure is 300 psig and
all other systems are operable.
(0.5)
b. List three alternative decay heat removal methods provided for if the
vessel head is removed.
(0.75)
(***** END OF CATEGORY 07 *****)
!
_
..
- - -
-
.- __- __ -__ _
-
- - - - .
.
.
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 17
.
.
.
.
.
.
.
QUESTION 8.01
(2.00)
The concentration of the boric acid solution in the Boric
Acid Storage System must be verified once a week in
accordance with Technical Specification 4.1.2.5.
The
chemist sampled the boron concentration on the following
schedule.
(All samples taken at 1200 hours0.0139 days <br />0.333 hours <br />0.00198 weeks <br />4.566e-4 months <br />).
Mar 1 --- Mar 8 --- Mar 16 --- Mar 24 --- Mar 31
a.
Explain why surveillance time interval requirements
WERE or WERE NOT exceeded on Mar 16.
(1.0)
b.
Explain why surveillance time interval requirements
WERE or WERE NOT exceeded on Mar 24.
(1.0)
_
QUESTION 8.02
(1.50)
What is the TECHNICAL SPECIFICATION basis for the requirement to
reduce Tavg to less than 500 degrees when specific activity limits
on the RCS are exceeded?
QUESTION 8.03
(2.00)
a.
How many members per shift are required on the fire brigade.
(0.5)
b.
Who may NOT be included as members of the fire brigade?
(1.0)
c.
Who is normally respon.ible to function as the fire chief?
(0.5)
(***** CATEGORY 08 CONTINUED ON NEXT PAGE *****)
.
-__
-
_
. ...- -. .
.
..
__
. . .
--
.-
- - - - -
-.
..
.
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 18
,
i
-
.
.
.
.
~
.
QUESTION 8.04
(2.00)
1N ar 7.20-1
a.
List the minimum & requirements for shift manning:
Position
Mades 1,2,3 or 4
Modes 5 or 6
<
SF (licensed)
NSO
,
RAD and CHEM
(0.1 each)
personnel
(total of 1.2)
b.
If an unexpected absence of' an on-duty shift crew member occurs,
the shift crew composition may be one less than the minimum for
a period of time not to exceed
hours provided action is
taken to restore the shift crew composition.
(0.5)
c.
What areas must the Shift Technical Advisor provide technical
support to the Shift Supervisor by tech specs?
(0.3)
.
QUESTION 8.05
(2.50)
a.
Assume that it is 0300 on 2-19-86 and the reactor is presently at 45%
power. Considering the Delta-I target band history listed below,
calculate the associated Delta-I penalties.
(1.5)
Date
Time (out)
Time (in)
Power (%)
Penalty (min)
1.
2-18-86
0300
0318
85
2.
2-18-86
1557
1633
65
3.
2-19-66
0138
0300
45
b.
When may power be increased above 50%?
(1.0)
,
QUESTION 8.06
(2.00)
/. n
!
%
a.
During a Mode 1 valve alignment, it is reported that the discharge
valve for No.1 Centrifugal Charging Pump is closed and cannot be
physically opened. Is No.1 Centrifugal Charging Pump OPERABLE?
(0.5)
b.
2 Centrifugal Charging Pump but it fails Jo start.The Shift Supervisor orders an o
Does NONCOPFLIANCE
q
with any Tec ical Specificat 'n exist? ,(/6 P =M
(0.5)
a
n: YGS HO W
%
mW
v
c
What should he Control Room perator actions (required by Technical
Specifications) be during the next 1 HOUR?
(1.0) g l
g
g
cudL
M 7h
4
(
b!
g
(***** CATEGORY 08 CONTINUED ON NEXT PAGE *****)
/
-
$
% , k % ann.
h O k-
.
u.
- .-
-. --- --.
- -
- -
,_
_
_
_
_
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 19
,
.
.
.
.
.
~
.
QUESTION 8.07
(3.00)
List SIX conditions or occurrences that reautre notification of the NRC
within ONE hour,
a
QUESTION 8.08
(1.00)
Complete the following statement with one of the provided terms.
Seal leakoff from the RCP (2 seal which is collected in the RCDT is
classified as
leakage,
a.
Controlled
b.
Pressure Boundary
c.
Identified
d.
Unidentified
QUESTION 8.09
(2.50)
When an emergency event is declared in the control room prior to
a.
activation of the TSC, the offsite civil authorities must be notified
within
minutes and the NRC within
minutes.
(0.5 each)
b.
TRUE or FALSE?
If the NRC Senior Resident Inspector is notified of the emergency
events, NRC notification has been completed.
(0.5)
c.
How often must the station provide update messages to the offsite
civil authorities (state emergency response organization)?
oceannig%fon
(0,5)
d.
Activation of the GSEPa%sFoccur within
minutes from
activation of the station emergency plan.
(0.5)
L. GS E P = p @ _ Q
l
QUESTION 8.10
(1.00)
,
The Shift Engineer declared an unusual event at 10:00 based on a loss
of all offsite AC power. At 10:05 offsite power is restored prior to
sending the initial notification message to offsite civil authorities.
Can the Acting Station Director cancel the unusual event and not send the
message if no further potential exists for emergency response actions?
(1.0)
(***** CATEGORY 08 CONTINUED ON NEXT PAGE *****)
!
-
-
. -
. -
.
- - - .
. - - - - - - .
- -
. - - . . .
.
. - - - . . , - - - - - - .
, - - . -- - ,- ,- ..-..--
.
.
.
8.
ADMINIS,TRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 20
-
.
.
-
~
.
QUESTION 8.11
(1.00)
The station has declared a Site Area Emergency because of a primary system
leak exceeding the capacity of the charging punps. Offsite civil
authorities have been notified and the GSEP is being activated. 30 minutes
after event declaration, a helicopter carrying a news crew that has reacted
to the story crashes into the protected area injuring a security guard and
killing the crew. The Acting Station Director determines that this
occurance meets the EAL requirements for an Unusual Event. SELECT the
proper action to be taken by the Acting Station Director,
a.
Declare an Unusual Event but specify its cause.
b.
Do not make any additional event declarations but notify authorities of
events.
c.
Downgrade the Site Area Emergency to an Unusual Event.
d.
Declare an Unusual Event concurrent with the Site Area Emergency.
QUESTION 8.12
(1.00)
The Acting Station Director declares a general emergency event based on
LOCA into containment with a failure of ECCS to actuate. No release of
radioactive materials has occurred.
a.
What protective actions, if any, would the Acting Station Director
recommend to the offsite civil authorities?
(0.5)
b.
List the protective actions that can reduce dose exposure to the
general public inside the 10 mile EPZ.
(0.5)
QUESTION 8.13
(1.00)
The following critical safety function status trees are indicated:
Color
Containment
green
Core Cooling
red
o%
Heat Sink
orange
Integrity
yellow
%
CSg
%
Inventory
red
Subcriticallity
green
Which CSF has operator priority?
Plc, ATJON
4%
A
.
(***** CATEGORY 08 CONTINUED ON NEXT PAGE
- )
.
-- --
-
.
. -
- - - - - - -
,-r
,
-- -
. - , - - - - , , , .
- - . - - , - - - - - . . . . ,--
-,-- ---
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 21
.
.
.
. . . .
,
,
,
-
,
.
-
\\
'
QUESTION 8.14
(2.50)
When conducting valve lineups, the valve position must be determined by
the operator. How would the operator verify valve position on the
following types of valves?
a.
manual valve in the open position
(0.5)
b.
sunual valve in the locked open position
(0.5)
c.
manual valve in the closed position
(0.5)
d.
MOV in AUTO
(0.5)
'
e.
manual valve in a throttled position
(0.5)
1
(***** END OF CATEGORY 08 *****)
( ***** *** *** * * END OF EX AMI N AT I ON ***** * * * *** * * * * )
i
_
-
_ _ -. _ . . _ _ _ - _ _ . _
_-.
. _ - .
.
. -
.
.
-
-u-
-
--
-
.
.
.
.
.
.
.
.
.
. .
A
BTU
SPECIFIC HEAT (Cp)
Ibm 'F
--
se
O
O
'
es
o
o
..
.
.
,
i
.,
.
.
.
.
.
.
.. .
.. .
.
. .
.
.
.
.
,
.
.
.
.
.
..
...
.
.
.
.!
...
..
.
.
.
.
.
.
.
.
.
Oo
.
.
.
.
.
.e.
.
.l
.,
.,.
t.
.
s.
.
.
.
.
.
.
..
s
.
..._,.. . . . . . _ _ . . . . . . . . . .
. . . . . . . . . . .
. _ _ _ .
.,
..
..g.
.[
..
.
,.
.
.
.
.
.
.
e.
..
8
.
I-
'.!. .
,
.
.;
. .
.
..
..
. .,. ..
_.9,_..
!
..
.
_ . . _ . .
.
. . . . _ . . _ . . . . . . .
.
.,
.
l.
.
..
g
-
- -
1
t
-
.
100 PSI A -
s-
e
.
.
g
E
.
>
.
.....J.
. . . .
e.
..
1e
. . . . . .
t
-1c
.
.-
- n
.
m *
=
- . .
o
- 8
C
t
-
wi
.
,
.
j
.
.
.s
s
,
i.
.
.
.
8
.
.. .
l
1000 PSIA
- *
.
..;
.
..
.,.
.. ......
-
,
,
.,
.
...
.
.
....
.
..... ..
.
.. .
..
... ..
.
.g.
.
.
.
.
. ..
.I
.
..
o
-.
.
o
.
.
2000 PSIA
.
.,
s.
,
,
.
-
..
. . _ _ _
_..___ .
. . . . . . ...
'
. ' . .-
3000 PSIA
-
.
.g
.
..
,,
.
....
...
.g
.
8
. ..
.$
j.
. . . _ . . .
. .
.
. .
. ..
...
.
.
.I.
.
.
.
. . . _ _ _ . . _ . . . .
_ . _ .
. _
. . . . . . . . . . _ . . . . . . .
.
...
i
e
i
s.
.
l
.
I
.
.
FIGURE FND-THM-105:
SPECIFIC HEAT OF WATER AT DIFFERENT
PRESSURES (REV. 1)
-
- .
.
.--
.
i
-
.
EQUATION SHEET
..
.
,
'
-
,
f = ma
v = s/t
Cycle efficiency = (. Net work
'
out)/(Energy in)
2
w = og
s = V ,t + 1/2 at
2
E = sc
KE = 1/2 av
a = (Vf - V,)/t
A = AN
A = A ' At
2
-
O
PE = ogn
v = V, + at
w = e/t
1 = an2/t.1/2 = 0.693/t1/2
f
if2*ff = [(tur)(t )3
2
t
m
w . , g.
,o
A=
[(t1/2) * I*b)3
4
aE = 931 am
[n = V,yAo
7 , g , -D
9
.
.
Q = mCpat
6 = UAa T
I*I'"
o
g
pwr = W ah
I"I 10
f
o
TV1. = 1.3/u
sur(t)
HVL = -0.693/u
P = P 10
P = P e*/
o
SUR = 26.06/T
SCR = S/(1 - K,ff)
CRx " 3/II ~ Keffx}
CR (1 - K ,ffj) = CR (I ~ eff2)
SUR = 26p/t* + (a - p)T
j
2
l
T = ( t*/s ) + [(8 - o V Io]
M = 1/(1 - K,ff) = CR /CR,
j
T = s/(p - s)
M = (1 - K,ff,)/(1 - K,ffj)
T = (s - o)/(Io)
SDM = ( - K ,ff)/K ,ff
a=(K,ff-1)/K,ff=aK,fgK,ff
t* = 10
seconds
I = 0.1 seconds"I
o = [(t*/(T K,ff)] + [a,ff (1 + IT)]
/
I d; = I d
2 ,2 2
l
P = (I4V)/(3 x 1010)
Id
gd
jj
22
2
I = oN
R/hr = (0.5 CE)/d (meters)
2
R/hr = 6 CE/d gf,,g)
Water Parameters
Miscellaneous Conversions
1 gal. = 8.345 lem.
1 curie = 3.7 x 1010dps
,
'
I ga]. = 3.78 liters
1 kg = 2.21 lbm
1 ft3 = 7.48 gal.
I hp = 2.54 x 10 Stu/hr
Density = 62.4 lbm/ft3
1 mw = 3.41 x 10 6tu/hr
Density = 1 gm/cn.3
lin = 2.54 cm
Heat of vaoorization = 370 3tu/lom
"F = 9/5*C + 32
< test of fusion = i44 Btu /lem
- C = 5/9 (*F-32)
l
1 Atm = 14.7 psi = 29.9 in. Hg.
1 BTU = 778 ft-lbf
I ft. H O = 0.4335 lbf/in.
2
I
-
.
.
.
'
'
.
v
.
.
..
.
l
Table 1.
Saturated Steam: Temperature Table
Abs Press.
Specific Volume
Enthalpy
Entropy
Temp
Lb per
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Temp
Fahr
SqIn.
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Fahr
i
I
p
vi
vig
vg
hl
h is
h
se
sig
s
t
r
g
32 I
O08859
0 016022
33047
33043
0 0179
1075 5
1075.5
0 0000 2.1873 2.1873
32 I
34.8
0 09600
0 016021
3061.9
3061.9
1.996
1074.4
1076.4
0 0041
2.1762 2.1802
34 5
,
36 0
0 10395
0 016020
2839 0
2839.0
4.008
1013.2
1077.2
0 0081
2.1651
2 1732
36 8
!
30 0
0.11249
0 016019
26341
2634.2
6.018
1072.1
1078.1
0.0122
2.1541
21663
38 5
40 I
I.12163
0 016019
2445.8
2445.8
8.027
1071.0
1079.0
0 0162
2 1432 2.1594
40 0
42 8
0.13143
0 016019
2272.4
2272.4
10 035
1069 8
1079.9
0 0202
2.1325 2.1527
42 0
44 3
0 14192
0 016019
2112 8
2112.8
12.041
10683
10801
0 0242 2.1217 2.1459
44 0
46 I
O15314
0.016020
19651
19653
14.047
1067.6
1081.6
0 0282 2.1111
2.1393
46.8
48.0
0.16514
0.016021
1830.0
1830.0
16.051
1066.4
1082.5
0.0321
2.1006 2.1327
48 I
58.8
0 17796
0 016023
1704 8
1704 8
18 054
1065.3
1083.4
0.0361
2.0901
2.1262
50.0
-
52 I
0.19165
0 016024
1589 2
1589 2
20 057
1064.2
1084.2
0.0400 2.0798 2.1197
52.I
!
54 0
0 20625
0 016026
1482.4
1482.4
22 058
1063.1
1085.1
0 0439
2 0695 2.1134
54 I
!
56 I
O22183
0.016028
1383 6
1383.6
24 059
1061.9
1086.0
0 0478 2.0593 2.1070
56 8
58.0
0 23843
0.016031
1292.2
1292.2
26.060
1060.8
1086.9
00516
2 0491
2.1008
58.I
$8 I
O25611
0.016033
1207.6
1207.6
28 060
10591
10873
0.0555
2.0391 2.0946
II.I
$2 0
0.27494
0.016036
1129.2
1129.2
30.059
1058.5
1088.6
0.0593
2 0291
2.0885
62.8
'
64 3
0 29497
0 016039
1056.5
1056.5
32.058
10574
1089.5
0 0632 20192 2.0824
64 5
ss e
031626
0 016043
989 0
989.1
34.056
1056.3
1090.4
0 0670 2.0094 2.0764
66.0
68 8
0.33889
0 016046
926.5
926.5
36.054
1055.2
1091.2
0.0708
1.93 % 2.0704
68.0
70 0
0.36292
0.016050
868.3
868.4
38 052
1054.0
1092.1
0.0745
1.9900 2.0645
70 I
i
72 8
0 38844
0 016054
814.3
814.3
40 049
1052.9
1093 0
0 0783
1.9804 2 0587
72.8
1
74 0
0 4l550
0 016058
7641
764.1
42.046
1051.8
1093.8
0 0821
1.9708 2.0529
74 3
76 8
0.44420
0 016063
7I74
717.4
44 043
10501
10941
0 0858
1.%I4 2.0472
76.8
78.8
0 47461
0 016067
673.8
673.9
46.040
1049.5
1095.6
0 0895
1.9520 2.0415
78.0
1
00 0
0 50683
0.016072
633 3
633.3
48.037
1048.4
1096.4
0 0932
1.9426 2.0959
80.0
!
I? 8
054093
0.016077
595 5
595.5
50 033
1047.3
1097.3
0 0969
1.9334 2.0303
82.0
i
84.8
057702
0 016082
560 3
560.3
52.029
1046.1
1098 2
0 1006
1.9242 2.0248
84.8
86 8
0 61518
0 016087
227.5
527.5
54 026
10450
1099 0
0.1043
1.9151
2 0193
O6 I
88 0
0 65551
0016093
4%8
496 8
56 022
1043 9
1099 9
0.1079
1.9060 2.0139
80.0
98 0
0 69813
0 016099
4681
468.1
58 018
10427
1100 8
0.1115
1.8970 2 0086
98 8
92 0
0 74313
0 016105
441.3
441.3
60 014
1041 6
1101 6
01152
I8881
2 00J3
32.s
34 0
G79062
0 016111
416 3
416 3
62 010
1040 5
l102 5
0 1188
1 8792 1.9980
94.0
96 3
0 84072
0016117
392 8
392.9
64.006
1039 3
1103 3
0 1224
1.8704 I9928
96 I
90 0
0 89356
0 016123
370 9
370 9
66 003
10382
11042
0 1260
18617 I9876
98 0
.
I
i,
.
.-
.
Abs Press.
Specific Volume
Enthalpy
Entropy
.
Temp
Lb per
Sal.
Sal.
Sat.
Sal.
Sat.
Sal.
Temp
Fahr
SqIn.
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Fahr
I
p
vi
vig
vg
hg
h ig
h
s,
s ,,
s,
t
g
Ice 3
0.94924
0016130
350.4
350 4
67.999
1037.1
1105.1
0.1295
1.8530 1.9825
100.0
l
182.8
100789
0 016131
331.1
331.1
69 995
1035.9
1105.9
0.1331
1.8444 1.9775
102.8
184 8
1 06 % 5
0016144
313.1
313.1
71.992
1034.8
1106 8
0.1366
1.8358 1 9725
184.8
~
.
Iss O
1.1347
0 016151
296.16
296.18
73 99
1033.6
1107.6
0.1402
1.8273
I.% 75
108.8
Igg I
1.2030
0 016158
280.28
280.30
75.98
1032.5
!!08.5
0.1437
1.8188 1.9626
180.0
-
113.0
1.2750
0 016165
26537
265.39
77.98
1031.4
1109.3
0.1472
1.8105 1.9577
110.0
112 3
1.3505
0 016173
251.37
251.38
79.98
1030.2
1110.2
0.1507
1.8021
1.9528
112.8
1148
14299
0 016180
238 21
238 22
81 97
1029I
1111.0
0.1542
13938 1.9480
114.0
11s.3
1.5133
0 016188
225 84
22585
83.97
1027.9
1111.9
0.1577
13856 1.9433
115.0
113.8
1.6009
0.016196
214.20
214.21
85.97
1026.8
11123
0.1611
13774 1.9386
118.0
t
120 I
1.6927
0 016204
203.25
203.26
87 97
1025.6
1113.6
0.1646
13693 1.9339
120.0
122 8
1.7891
0 016213
192.94
192.95
89.%
1024.5
1114.4
0.1680
13613 1.9293
122.0
1248
1.8901
0 016221
183 23
183.24
91.%
1023.3
1115.3
0.1715
13533 1.9247
124.0
125.1
1.9959
0 016229
174.08
174.09
93.%
1022.2
1116.1
0.1749
13453 1.9202
128.0
'
128.9
2.1068
0 016238
16545
165.47
95.%
1021.0
1117.0
0.1783
13374 1.9157
128.0
130.0
2.2230
0 016247
157.32
157.33
97.%
1019.8
1117.8
0.1817
13295 1.9112
130.0
'
132.0
2.3445
0 016256
149.64
149.66
99.95
10183
1118 6
0.1851
13217 1.9068
132.0
134.0
2.4717
0 015265
142.40
142.41
101.95
1017.5
1119 5
0.1884
13140 1.9024
134.g
135 0
2.6047
0 016214
135 55
135.57
103.95
1016.4
1120.3
0.1918
13063 1.8980
136.3
1388
2.7438
0 016284
129.09
129.11
105.95
1015.2
1121.1
0.1%1
1.6986 1.8937
133.t
148 8
2.8892
0 016293
122.98
123.00
107 95
1014.0
1122.0
0.1985
1.6910 1.8895
140.0
.
142.5
3.0411
0.016303
117.21
11732
109.95
1012.9
1122.8
0.2018
1.6534 1.8852
142.0
'
144.s
3.1997
0 016312
I1134
IIi16
111.95
10113
1123 6
0.2051
1.6759 1.8810
144.s
,
l
146 8
3.3653
0 016322
106.58
106.59
113 95
1010.5
1124.5
0.2084
1.6684 1.8769
145.1
!
148.0
3 5381
0.016332 - 101.68
101.70
115.95
1009.3
1125.3
0.2117
1.6610 1.8727
148.0
i
j
150.0
3.7184
0 016343
97.05
97.07
117.95
1008.2
1126.1
0 2150
1.6536 1.0686
150.0
1
152.5
3.9065
0 016353
92.66
92.68
119.95
1007.0
1126.9
0 2183
1.6463 1.8646
152.8
154.3
4.1025
0.016363
88 50
88.52
121 95
1005.8
11273
0.2216
1.6390 1.8606
154.8
'
156.8
4.3068
0 016374
84.56
84.57
123.95
1004.6
1128.6
0 2248
1.6318 1.8566
158.0
158.8
4.5197
0 016384
80.82
80.83
125.%
1003.4
!!29.4
03281
1.6245 1.8526
158.0
F
168.8
43414
0 016395
77.27
77.29
127.96
1002.2
1130.2
0 2313
1.6174 1.8487
108.0
152 8
4 9722
0016406
/3 90
73.92
129 96
1001.0
1131.0
0 2345
1.6103 1.8448
162.0
164.5
5 2124
0 016417
70.70
7032
131.96
999.8
1131.8
0.2377
1.6032 1.8409
164.0
164 8
54623
0 016428
67.67
6768
133 97
998.6
1132.6
0 2409
1.5%1 1.8371
188.8
168.8
53223
0 016440
64.78
64.80
13597
997.4
1133.4
0.2441
1.5892 I.8333
154.0
170.0
5 9926
0 016451
62.04
62.06
137.97
996 2
1134.2
0.2473
1.5822 1.8295
170.0
172 I
6 2736
0016463
59.43
5945
139 98
995.0
1135 0
0 2505
1.5753 1.8258
172.0
174I
6 5656
0016414
56 95
5697
141.98
993 8
1135.8
0.2537
1.5684 1.8221
174 e
tilO
6 8690
0 016486
54 59
54 61
143 99
992.6
1136 6
0 2568
1.5616 1.8184
175.3
'I O
71840
0 016498
52.35
5236
- 15 99
991.4
1137.4
0 2600
1.5548 1.8147
878.I
_ _ - -.
.- .
. - - - - -
.
. . _ _ . .
-
--.
.
'
'
..
'
.
i
.
t
!
!
I
-
Abs Press.
Specific Volume
Enthalpy
Entropy
!
Temp
tb per
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Temp
l
Fahr
SqIn.
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Fahr
i
i
i
p
v,
vfg
vs
h,
h it
hg
s,
sig
s
l
!
g_
i
j'
130.0
7.5110
0.016510
50 21
50 22
148 00
990.2 - 1138.2
0 2631
1.5480 1.8111
III0
1g2 0
7.850
0.016522
48.172
18.189
150 01
989.0
1139.0
0.2662
1.5413
1.8075
182.0
IM.8
8.203
0.016534
46 232
46.249
152 01
987.8
1139.8
0.2694
1.5346- I8040
184 5
les e
8.568
0.016547
44.383
44.400
154.02
986 5
1140.5
0 2125 1.5279
1.8004
ISEI
.
!
133.s
8.947
0.016559
42.621
42.638
156 03
985 3
1141.3
0.2756
1.5213 13 % 9
IIII
!
19eI
9.340
0.016572
40.941
40.957
158.04
984.1
1142.1
0.2787
1.5148 13934
Its 8
i
192.0
9347
0.016585
39337
39.354
160.05
982 8
1142.9
02818 1.5082 13900
1926
194 8
10.168
0.016598
37.808
37.824
162 05
9816
11433
0.2848
1.5017 13865
1948
.
!
ItsI
10.605
0016611
36 348
36364
164.06
980.4
1144.4
03879 1.4952 13831
195 8
19s e
11.058
0016624
34.954
34.970
166.08
979.1
1145 2
03910 1.4888 13798
190 0
l
!
200.0
11.526
0.016637
33.622
33.639
168 09
977.9
1146 0
0.2940
1.4824 1 7764
200 8
!
294.0
12.512
0.016664
31.135
31.151
172.11
975 4
11475
03001
1.4697 13698
204 8
23e e
13.568
0 016691
28.862
28.878
176.14
9 72.8
1149 0
03061
1.4571
17632
200 0
212.s
14.6 %
0.016719
26382
26399
180.17
9703
1150.5
0.3121
1.4447 17568
212 0
215.0
15.901
0.016747
24.878
24.894
184.20
%7.8
1152.0
03181
1.4323 1.7505
215.8
220.0
17.186
0.016775
23.131
23.148
188.23
965.2
1153.4
0 3241
1.4201
13442
229.I
l'
224.8
18.556
0.016805
21.529
21.545
192.27
962.6
1154.9
0 3300
1.4081
13380
224 I
I
228 8
20.015
0.016834
20.056
20.073
196 31
960.0
1156.3
0 3359
13 % I
13320
228 0
1
232.0
21.567
0.016864
18.701
18318
20035
957.4
1157.8
03417
13842 13260
232 8
l
236.0
23.216
0.016895
17.454
17.471
204.40
954.8
!!59.2
03476
13725 13201
236.8
.
I
24e 8
24.% 8
0.016926
16304
16321
208.45
952.1
1160.6
03533
13609 13142
240 0
!
244.I
26.826
0.016958
15.243
15.260
212.50
949.5
1162.0
0 3591
13494
13085
244I
248.9
28396
0.016990
14.264
14.281
216.56
946 8
1163.4
03649
13379
1.7028
240 0
-
252.s
30.883
0.017022
13358
13 375
220.62
944.1
11643
03706 1.3266 16972
252.0
,
l
255.0
33.091
0.017055
12.520
12.538
224.69
941.4
1166.1
0.3763 - 13154 1.6911
256 B
!
200.0
35.427
0.017089
11345
11362
22836
938.6
1I67.4
03819
13043 1.6862
268 8
264 s
37.894
0.017123
11.025
11.042
232.83
935.9
11683
0 3876
1.2933
16808
254 0
258.8
40.500
0.017157
10 358
10375
236 91
933.1
1170 0
0 3932
1.2823 16755
258 8
'
212.8
43.249
0 017193
9 738
9355
240.99
930 3
1171.3
03987
l2115 1.6702
272.0
I
276.0
46.147
0 017228
9.162
9.180
245 08
927.5
1172.5
0.4043
13607 1.6650
275 I
l
200.0
49.200
0 017264
8.627
8 644
249.17
924.6
1173 8
0.4098
1.2501
1.6599
200 8
284.0
52.414
001730
8.1280
8.1453
253 3
9213
11750
04154
12395
1.6548
FM.O
200.0
55395
0 01734
76634
1.6807
257.4
918 8
1176 2
0 4208
1 2290
1.6498
288 0
292 8
59.350
0.01738
7.2301
7.2415
261.5
915 9
1I71.4
0 4263
12186 1.6449
292.0
!
2968
63.084
0 01741
6 8259
6.8433
265 6
913.0
II 78.6
0.4317
I2082 16400
296 8
,
t
i
,
. -
- - - -
-
-
- - -
- - - _ _ _ _ _ _ _ _ _ _ _ _
_
_ - _ _ _ _ _ _ _ _ _ _ _ _ _ _
- _ - _ _ _
. _ _ _ _
_.
-
_
.
.
'
.
.
.
.
I
Abs Press.
Specific Volume
Enihalpy
Entropy
Temp
Lb per
Sal.
Sat.
Sat.
Sat.
Sat.
Sat.
Temp
Fahr
SqIn.
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Fahr
i
p
vi
vig
vg
he
h rg
h
sg
sig
sg
t
g
l
30t8
67.005
001745
6.4483
6.4658
269 7
9100
1179.7
0 4372
11979
I6351
-
300 e
'
304.0
71.119
0.0l749
60955
6 1130
273 8
907.0
1180.9
0.4426
1.1877
16303
304 s
300.0
75.433
001753
5 7655
5 7830
278 0
904.0
1182.0
0 4479
1.1776
I6256
300 e
312.0
79 953
0 01757
54566
5.4742
282 1
9010
1183.1
04533
1.1676
1 6209
312.0
'
318.8
84.688
00l761
5.1673
5 1849
286.3
897.9
1184.1
0.4586
1.1576
1616:
316.0
320 0
89.643
001766
48%1
4.9138
290 4
894.8
1185 2
0 4640
1.1417
1.6116
320 e
324.s
94 826
0.01770
4 6418
4.6595
294 6
891 6
1186 2
04692
1.1378
16071
324.0
323.0
100 245
0.01774
4.4030
4.4208
2987
8885
1187.2
0.4745
1.1280
1.6025
370 0
332.0
105.907
0.01779
4.1788
4.1%6
302.9
885.3
1188.2
04798
1.1183
I5981
332.s
336 e
111.820
0.01783
3.9681
3.9859
307.1
882.1
1189.I
0 4850
1.1086 1.5936
336.5
340.0
I17.992
0.01787
3.7699
3.7878
311.3
878 8
1190.1
04902
1.0990 1.5892
343 e
344.s
124.430
0.01792
3 5834
3.6013
315.5
875 5
1191.0
04954
1.0894 1.5849
344.0
'
343.0
131.142
0.01797
3 4018
3.4258
319.7
872.2
1191.1
0 5006
1.0799 1.5806
343 e
,
352.0
138.138
0 01801
3 2423
3.2603
323 9
868.9
1192.7
0.5058
1.0705 1.5763
352.3
1
358.0
145.424
0 01806
3 0863
3.1044
3281
865.5
1193.6
0 5110
10611
1.5721
356.8
l
360.8
153.010
0.01811
2.9392
2.9573
332.3
862.1
1194.4
0 516l
I.0517 1.5678
360.3
384.8
160.903
0 01816
2.8002
2.8184
336 5
858 6
1195.2
0 5212
1.0424
1.5637
364 I
'
358.0
169.113
0 01821
2 6691
2.6873
340 8
855.1
1195.9
0 5263
1 0332 1.5595
363 3
t
372.0
177.648
0 01826
2.5451
2.5633
345 0
851 6
11 %.7
0 5314
1.0240 1.5554
3728
375.0
186.517
0.01831
2.4279
2.4462
349 3
848.1
!!97.4
0 5365
1.0148
1.5513
375.0
1
338.0
195.729
0.01836
2 3170
2.3353
353 6
844.5
1198.0
0 5416
1 0057
1.5473
333.s
'
384.s
205 294
0.01842
2.2120
2.2304
357 9
840.8
1198.7
0 5466 09%6
1.5432
394.0
348.3
215.220
0 01847
2.1126
2.1311
362 2
837.2
1199 3
0 5516 0 9876
15392
30s e
I
392.s
225.516
0.01853
2.0184
2.0369
366.5
833.4
1199.9
0 5567 09786
1.5352
392.s
395.0
236.193
0.01858
I.9291
1.9477
370 8
829.7
1200.4
0.5617 0 9696
1.5313
396 I
l
40se
247.259
0.01864
1.8444
I.8630
375.1
825.9
1201.0
0.5667 0.9607
1.5274
4gg a
!
404.s
258.725
0.01870
1.7640
1.7827
3794
822.0
1201.5
0 5717 09518
1.5234
484.0
1
400.0
270.600
0 01875
1.6877
1.7064
383.8
818 2
1201.9
0 5766 0 9429
1.5195
438.3
412.0
282.894
0.01881
16152
1.6340
3881
814 2
1202.4
0.5816 09341
1.5157
412.3
'
41s.g
295 617
0.01887
1.5463
1.5651
392.5
810.2
1202.8
0.5866 0.9253
1.5118
4IE I
,
J
423.0
308.780
0.01894
1.4808
1.4997
396.9
806 2
1203.1
0 5915 0 9165
1.5080
420 8
'
424.8
322.391
0 01900
1.4184
1.4374
401.3
802.2
1203.5
0 5964
0 9077
1.5042
4248
428.5
336 463
001906
1.3591
13782
4057
798 0
1203.7
06014
0 8990
15004
428 e
432e
351.00
0 01913 1.30266
1.32179
410.1
793 9
1204.0
0 6063 0 8903
1.4966
432e
l
436.3
366.03
0 01919 1.24887
1.26806
414 6
769 7
1204.2
0 6112
0 8816
1.4928
43E g
448 8
381.54
0 01926 1.19761
1.21687
419 0
185 4
1204 4
0 6161
0 8729
1.4890
443 9
i
!
dad 3
397.56
0 01933 1.14874
116806
423 5
781.1
1204 6
0 6210 0 8643 14853
444e
.
1
414 09
0 01940 1.10212
1.12152
10
176 7
1204.7
06259
0 8557
14815
"9
?
.J
431 14
0 01947 1 05764
1 07711
5
172 3
1204 8
0 6308
0 8411
14778
455 g
44873
0 01954 1 01518
1 03472
- J70
767 8
1204 8
0 6356 0 8385
14741
. . . .
!
,
.
-
s
,
'
.
.
.
!
I
Abs Press.
Specific Volume
Enthalpy
Entropy
Temp
Lb per
Sat.
Sat.
Sat.
Sat.
Sat.
Sal.
Temp
Fahr
SqIn.
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Fahr
t
p
V:
Vit
vg
he
h ig
h
s,
sl8
S
I
g
t
46e e
466 87
0.01 % 1
0.97463
0.99424
441.5
763.2
1204.8
0.6405 0.8299 1.4704
480.0
4640
485 56
0 01 % 9 0 93588
0.95557
446.1
758 6
12043
0.6454 0.8213
1.4667
464.0
468 8
504 83
0.01976 0.89885
0.91862
4503
754.0
1204.6
0.6502 0.8127
1.4629
484.0
472 8
524.67
0.01984 0 86345
0.88329
455.2
7493
1204.5
(L6551
0.8042
1.4592
4 72.0
l
416 8
545.11
0.01992 0.82958
0.84950
459.9
744.5
12043
0.6599 01956 1.4555
475.0
'
Age a
566 15
0 02000 039716
0 81717
464.5
739.6
1204.1
0.6648 0.7871
1.4518
480.0
'
484 e
587 81
0.02009 036613
038622
469.1
7343
1203.8
0.6696
0 7785
1.4481
484.0
438 s
610.10
0.02017
033641
0.75658
473.8
7293
1203.5
0.6745 03700 1.4444
438.9
492 0
633.03
0 02026 030794
032820
478.5
724.6
1203.1
0.6793
0.7614
1.4407
492.5
496 8
656 61
0 02034 0.68065
010100
483.2
719.5
12023
0.6842
03528 1.4370
496.0
,
'
5000
680.86
0 02043 0.65448
0 67492
487.9
7143
1202.2
0.6890
03443
1.4333
500.9
i
504.0
705 78
0 02053 0.62938
0 64991
4923
709 0
12013
0.6939
03357 1.42 %
504.0
508 8
731.40
0 02062 0 60530
0 62592
497.5
7033
1201.1
0 6987
03271
1.4258
500.8
!
512 0
757.72
0 02072 0 58218
060289
5023
698.2
1200.5
0.7036
03185 1.4221
512 0
j
516.8
784.76
0 02081
0 55997
0.58079
507.1
6923
1199.8
0.7085
03099 1.4183
516.0
528.s
812 53
0 02091
0 53864
0 55956
512.0
687.0
1199.0
0.7133
0.7013
1.4146
$20.0
5248
841.04
0 02102 0.51814
0 53916
516.9
6813
1198.2
03182
0 6926 1.4108
524.0
578 0
870 31
0 02112 0 49843
0 51955
521.8
675.5
1197.3
01231
0.6839 1.4070
520 0
537 8
900 34
0 02123 0.47947
0.50070
526 8
669.6
11 % 4
03280 0.6752 1.4032
532.0
535 0
931.17
0 02134 0 46123
0.48257
5313
663.6
1195.4
01329
0.6665 1.3993
536.0
540 e
962.79
0.02146 0 44367
0 46513
536.8
657.5
1194 3
0 7378
0.6577 13954
540.0
5440
995.22
0 02157 0 42677
0.44834
541.8
6513
1193.1
0 7427
0 6489 13915
544.0
548 e
1028 49
0 02169 0.41048
0.43217
546 9
645.0
1191.9
03476
0.6400 1.3876
548.0
552 s
1062.59
0.02182 0 39479
0 41660
552 0
638.5
1190.6
03525
0.6311
13837
552.8
556 e
1097.55
0 02194 0 37966
0.40160
557.2
632.0
1189.2
03575
0.6222 13797
556.8
560.8
1133 38
0.02207 0 36507
038714
562.4
625.3
11873
0.7625
0.6132 1.3757
500.0
554 0
1170.10
0 02221
0 35099
0.37320
567.6
618.5
1186.1
0.7674
0.6341
13716
564.0
568 0
1207.72
0 02235 0 33741
035975
572.9
611.5
1184.5
03725
0.5950 13675
568.8
!
512 8
1246 26
0 02249 0 32429
0 34678
578 3
604.5
11823
0.7775
0.5859 13634
572.8
!
515.0
128534
0.02264 0 31162
0 33426
5833
597.2
1180.9
0.7825
0.5766 1.3592
578.8
5000
1326.17
0 02279 0.29937
032216
589.I
589.9
'1179.0
03876
0.5673 13550
500.0
584 5
13673
0 02295 0 28753
0 31048
594 6
582.4
1176.9
03927
0.5580 13507
584.0
508 8
1410 0
0.02311
0 27608
0 29919
600.1
5743
1174.8
03978
0.5485 13464
588.I
597 0
1453 3
0 02328 026499
0.28827
6053
566.8
1172.6
0.8030
0.5390 1.3420
592.0
596O
14978
0 02345 0 25425
0 27770
611.4
558.8
11703
0.8082
0.5293 13375
595.0
2
i
.
'
'
6
i
.
~
a
.
.
,
Abs Press.
Specific Volume
Enthalpy
Entropy
Temp
Lb per
Sal.
Sal.
Sal.
Sal.
Sal.
Sal'
ten
Fahr
SqIn.
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Fa
!
I
p
vg
vgg
vg
hg
h gg
he
sg
sig
se
I
~
age.s
1543 2
0.02364 0.24384
026747
617.1
550.6
1167.7
0.8134
0.5196 1.3330
000.8
se4.s
1589 7
0.02382 0.23374
0.25757
622.9
542.2
1165.1
0.8187
0.5097 13284
884.0
,
808 8
16373
0.02402 0.22394
0.247 %
628.8
533 6
1162.4
0.8240 0.4997 13238
808.O
E12 3
16861
0.02422 0.21442
0.23865
634 8
524.7
1159.5
0.8294
0.4896 1.3190
$12.0
Els.s
1735 9
0.02444 0.20516
0.22960
640.8
515.6
1156.4
0.8348
0.4794 1.3141
816.8
828 8
1786.9
0.02466
0.1 % 15
0 22081
646 9
5063
1153.2
0.8403
0.4689 1.3092
820.8
824.I
1839 0
0.02489 0.18737
0.21226
653.1
406.6
1149.8
0 8458
0.4583 1.3041
524.0
$28I
18924
0.02514 0.17880
0 20394
659.5
486.7
1146.1
0.8514
0.4474 1.2988
628.8
832.8
1947.0
0.02539 0.17044
0.19583
665.9
476.4
1142.2
0.8571
0.4364 1.2934
532.0
$36.8
2002.8
0.02566 0.16226
0.18792
672.4
465.7
1138.1
0.8628
0.4251
1.2879
636.0
548 8
2059.9
0.02595 0.15427
0 18021
679.1
454.6
1133.7
0.8686
0.4134 1.2821
640.0
.
'
544 e
2118 3
0.02625 0.14644
0.17269
685.9
443.1
1129.0
0.8746
0.4015 1.2761
sea.s
$48 8
21781
0.02657 0.13876
0.16534
692.9
431.1
1124.0
0.8806
03893 1.2699
548.0
552.8
22392
0.02691
0.13124
0.15816
700 0
418.7
1118.7
0.8868
03767 1.2634
652.0
!
$56 8
2301.7
0.02728 0.12387
0.15115
707.4
405.7
1113.1
0.8931
03637 1.2567
656.8
568.8
2365.7
0.02768 0.11663
0.14431
714.9
392.1
1107.0
0.9995
03502 1.2498
000.0
564.8
2431.1
0.02811
0.10947
0.13757
722.9
377.7
1100.6
0.9064
03361 1.2425
664.0
561.8
2498.1
0.02858 0.10229
0.13087
731.5
362.1
1093.5
0.9137
03210 1.2347
668.0
1
572 0
2566 6
0 02911 0.09514
0.12424
740.2
345.7
1085.9
0.9212
03054 1.2266
872.8
ETE 8
2636 8
0.02970 0.08799
0.11769
749.2
328.5
1077.6
0.9287
02892 1.2179
576.0
$30.8
2708 6
0.03037 0.08080
0.11117
758.5
310.1
1068.5
0.9365
0.2720 1.2006
see.s
584.8
2782.1
0.03114 0.07349
0.10463
768 2
290.2
1058.4
0.9447
0.2537 1.1984
604.0
688.I
2857.4
0.03204 0.06595
0.09799
778 8
268.2
1047.0
0.9535
0.2337 1.1872
588.8
<
592.0
2934.5
0.03313 0.05797
0.09110
790 5
243.1
1033.6
0. % 34
0.2110 1.1744
092.0
S9E.I
3013.4
0.03455 0.04916
0.08371
804.4
212.8
1017.2
0.9749
0.1841 1.1591
595.0
138.8
3094 3
0.03662 0.03857
0.07519
822.4
172.7
995.2
0.9901
0.1490 1.1390
700.0
7s2 s
3135.5
0.03824 0 03173
0.06997
8350
144.7
979.7
1.0006
0.1246 1.1252
782.0
.
'
104 I
3177.2
0.04108 0.02192
0.06300
854 2
102.0
956.5
1.0169
0.0876 1.1046
704.0
785.8
3198 3
C.04427 0.01304
0.05730
873.0
61.4
93E
l.0329
0.0527 1.0856
785.0
135.47*
3208.2
0.05078 0.00000
0.05078
906 0
0.0
90l
1.0612
0.0000 1.0612
705.47'
~
m
_ _ _ _ _ _
. _ _ _ _ _ _ . - . _ _ _ - .
- - - - _ -
--
--
- - - -
-
-
,,
-
,
,l,
w
.
.
l
l
Table 2: Saturated Steam: Pressure Table
i
!
Specific Volume
Enthalpy
Entropy
!
Abs Press.
Temp
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Abs Press.
l
lb/Sq In.
Fahr
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Lb/Sq In.
V
V
hg
h
h
s,
s g,
s
j
p
i
V I
ig
g
ig
g
e
P
l
g.00865
32.018
0.016022
3302.4
3302.4
0.0003
1075.5
1075.5
0.0000
2.1872
2.1872
eg0065
e 25
59 323
0.016032
1235.5
1235.5
27.382
1060.1
1087.4
0 0542
2.0425
2 0967
e 25
333
79 586
0 016071
641.5
641.5
47.623
1048.6
1096 3
0.0925
1.9446
2.0370
8 58
1e
101.74
0.016136
333 59
333 60
69 73
1036.1
1105 8
0.1326
1.8455
1.9781
ie
i
5e
162.24
0.016407
13.515
73.532
130 20
1000.9
1131.1
0 2349
1.6094
1.8443
5e
i
Ig g
193 21
0 016592
38 404
38.420
161.26
982.1
1143.3
02836
1.5043
!.7879
les
i
!
14 096
212.00
0 016719
26 782
26.799
18017
970.3
1150.5
0.3121
1.4447
1.7568
14 596
l
15.s
213.03
0 016726
26.274
26 290
181.21
%9.7
1150.9
0.3137
1.4415
I.7552
15 e
i
!
2ee
227.96
0.016834
20.070
20 087
196.27
9601
1156.3
0.3358
1.3%2
1.7320
23 g
,
30 3
250.34
S.017009
13.7266
13.7436
218.9
945 2
1164.1
0.3682
1.3313
1.6995
38 9
i
'
40.0
267.25
0.017151
10.4794
10.4965
236.1
933 6
1169 8
0.3921
1.2844
1.6765
de e
5e e
281.02
0.017274
8.4%7
8.5140
250.2
923 9
1174I
O.4112
1.2474
1.6586
53 s
50.s
292.71
0.017383
7.1562
7.1736
262.2
915 4
1177.6
0.4273
1.2167
1.6440
Eg g
-
i
7e e
302.93
0.017482
6.1875
6.2050
272.7
907.8
1180 6
0 4411
1.1905
1.6316
7e e
i
!
ge 3
312.04
0.017573
5.4536
5.4711
282.1
900.9
1183.1
0.4534
1.1675
16208
se e
!
ges
320.28
0.017659
4.8779
4.8953
290.7
894.6
1185.3
0 4643
1.1470
1.6113
ge s
j
1
I
180.0
3??.82
0.017740
4.4133
4.4310
298.5
888.6
1187.2
0.4743
1.1284
1.6021
Igg e
{
110.3
334.79
0.01782
4.0306
4.0484
305.8
883.1
1188.9
0.4834
1.1115
1.5950
Ils s
.
12e e
341.27
0 01789
3.7097
3.7275
312.6
877.8
1190.4
0.4919
1.0960
1.5879
12e g
130.0
347.33
0.01796
3.4364
3.4544
319.0
872.8
1191.7
0.4998
1.0815
1.5813
13ee
,
14g.e
353.04
0.01803
3 2010
3.2190
325 0
868.0
1193.0
0 5071
1.0681
1.5752
140.0
'
150.s
358.43
0.01809
2.9958
3 0139
330.6
863.4
1194.1
0 5141
1.0554
1.56 %
15eI
163.0
363.55
0.01815
2.8155
2.8336
336.1
8590
1195.1
0 5206
10435
1.5641
Ils s
,
173.s
368.42
0 01821
2.6556
2.6738
341.2
854 8
11 %.0
0 5269
1.0322
1.5591
17e e
les.g
373 08
0 01827
2.5129
2.5312
346.2
850.7
1196.9
0 5328
1.0215
1.5543
Igg e
i
19e.0
377.53
0.01833
2.3847
2.4030
350.9
846.7
1197.6
0 5384
1.0113
1.5498
190s
,
I
Igg.g
381.80
0.01839
2.2689
2.2873
355 5
842.8
1198.3
0.5438
1.0016
1.5454
feee
210.3
385.91
0.01844
2.16373
2.18217
359.9
839.I
1199 0
0.5490
0.9923
1.5413
218 e
223.8
389.88
0.01850
2.06779
2.08629
364.2
835 4
1199.6
0 5540
0.9834
1.5374
220 0
3
233.s
393.70
001855
I.97991
1.99846
368.3
831.8
I2001
0 5588
0 9748
1.5336
230 8
{
248 0
397.39
0.01860
1.89909
1.91769
372 3
828 4
1200.6
0.5634
0 9665
1.5299
243 g
i
253.s
400.97
001865
1.82452
1.84317
376.1
825 0
1201.1
0.5679
0.9585
15264
258 e
i
25e e
404 44
0 01870
I75548
I.77418
379.9
821 6
1201.5
0 5722
09508
1.5230
253 g
j
278.e
407.80
0 01875
169137
1.71013
383 6
818.3
1201.9
05764
0 9433
1.5197
270 0
4
2Og e
411.07
0.01880
1.63169
I65049
387.1
815 1
1202.3
05805
0 9361
1.5166
2eg e
'
290.0
414 25
0 01885
1.57597
1.59482
390 6
812.0
1202.6
0.5844
0 9291
1.5135
290 s
3egI
417.35
001889
1.52384
1.54274
394 0
808 9
1202.9
05882
09223
1.5105
30s e
353 g
43173
0 01912
1.30642
1.32554
409 R
194 2
1204 0
0 6059
0 8909
I4%8
350 g
4gg g
444 60
0 01934
1.14162
1.16095
424 2
780 4
1204 6
0 6217
0 8630
14847
400 g
-
.
.
- -
-
.
--.
-
-
.
'
r
a._f
=
Specific Volume
Enthalpy
Entropy
Abs Press.
Temp
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Abs Press.
Lb/Sq In.
Fahr
Liquid
Evap
Vapor
Lic uid
Evap
Vapor
Liquid
Evap
Vapor
tb/Sg in.
h
h
v
t i
ig
g
si
s gg
s
p
p
t
vg
vig
g
g
45e g
456.28
0.01954
1.01224
1.03179
437.3
767.5
1204.8
0 6360
0 8378
1.4738
454 8
See e
46701
0 01975
0.90787
0.92762
449.5
755.1
12043
0 6490
0 8148
1.4639
SeeI
550 8
476.94
0 01994
082183
0 84177
460.9
743.3
1204.3
0.6611
0 1936
1.4547
558 9
$se 3
486 20
0 02013
0 74 % 2
0.76975
471.7
732.0
12033
0 6723
01738
14461
sega
658 8
494.89
0 02032
0 68811
030843
481.9
720.9
1202.8
0.6828
03552
14381
558 8
700 e
503 08
0.02050
0.63505
0.65556
491.6
710.2
1201.8
0.6928
03377
1.4304
70s e
758 s
510.84
0 02069
0.58880
0 60949
500.9
699 8
12003
03022
03210
1.4232
758 I
509 8
689 6
1199.4
01111
0 7051
14163
sees
ges 8
518.21
0 02087
054809
0.568 %
-
850 0
525 24
0.02105
0 51197
0.53302
518.4
679.5
1198 0
03197
0 6899
1.4096
350 5
See e
531.95
0 02123
0.47968
0.50091
526 7
6693
1196 4
03279
06753
1.4032
ges e
958 3
538.39
0 02141
0 45064
0.47205
5343
660 0
11943
0 7358
06612
1.3970
358 e
legeI
544.58
0.02159
0.42436
0.445 %
542.6
650.4
1192.9
0.7434
0.6416
1.3910
legee
1958 8
550.53
0.02177
0.40047
0.42224
550.1
640 9
1191.0
03507
0.6344
1.3851
1950 e
llte s
556 28
0 02195
0 37863
0 40058
557.5
631.5
1189.1
03578
0 6216
1.3794
lige s
115s.8
561.82
0 02214
0.35859
0.38073
564 8
622 2
1187.0
03647
0.6091
1.3738
1158 8
1290 I
567.19
0.02232
0.34013
0.36245
571.9
613.0
1184.8
03714
05%9
1.3683
12000
1258 I
572.38
0.02250
0 32306
0 34556
578 8
603.8
1182.6
03780
0.5850
1.3630
1250e
138eI
577.42
0.02269
0.30722
0.32991
585 6
594 6
1180 2
03843
0 5733
1.3577
13se e
13588
582.32
0 02288
0 29250
0 31537
592 3
585 4
1177.8
0.7906
0.5620
1.3525
135e e
l4gg 8
587.07
0 02307
027871
0.30178
598 8
576.5
1175.3
03966
0.5507
1.3474
1400 8
1458 8
59130
0 02327
0 26584
0 28911
505 3
567.4
1172.8
0 8026
0 5397
1.3423
14500
1500 0
5 % 20
0 02346
0 25372
0 21719
611.7
558.4
11701
0 8085
0.5288
1.3373
1500 g
15500
600.59
0 02366
024235
026601
618 0
549.4
1167.4
0 8142
0 5182
1.3324
15589
16e0 0
604.87
002387
0 23159
0 25545
624 2
540.3
1164.5
0 8199
0.5076
1.3274
Isse e
1658 8
609.05
0 02407
022143
0.24551
630 4
531.3
1161 6
0 8254
0 4971
1.3225
1650 s
I700 8
613.13
0 02428
0.21178
0 23607
636.5
522.2
1158.6
0.8309
0.4867
1.3116
IFee g
17588
617.12
0.02450
0 20263
0.22713
642.5
513.1
1155.6
08363
0.4765
1.3128
1754 8
1000 I
621.02
0.02472
0 19390
0 21861
648 5
503 8
1152.3
0 8417
0.4662
1.3079
Iges e
1858 8
624 83
0 02495
0 18558
0.21052
654 5
494 6
!!49.0
0.8470
0.4561
13030
1858 e
lese 8
628.56
0 02517
0.17761
0 20278
660 4
485 2
1145 6
0 8522
0 4459
13981
Iges e
1958.8
632.22
0.02541
0.16999
0.19540
666.3
475.8
1142.0
0.8574
0.4358
1.2931
Itse e
2000.8
635.80
0 02565
0 16266
0.18831
672.1
466 2
1138.3
0 8625
0.4256
12881
2ses a
2100.0
64236
0.02615
0.14885
0.17501
683 8
4463
IJ 30.5
0 8727
04053
1.2780
2I0e e
220s.0
649.45
0 02669
0.13603
0.16272
695 5
4263
1122.2
0.8828
0.3848
1.2616
2200 3
230s.8
655.89
0 02727
0.12406
015133
707.2
406 0
1113.2
0.8929
0.3640
1.2569
23e8 8
2400.8
662.11
0 02790
0.11287
0.14076
719 0
384.8
11033
0.9031
0.3430
1.2460
2480 e
2500 8
668.11
0.02859
010209
0 13068
7313
361 6
1093.3
0 9139
0.3206
12345
2500 0
25ee s
673 91
0 02938
0.09172
0 12110
744 5
331.6
1082.0
09247
02977
12225
2sse e
2700 3
679.53
0 03029
0 08165
0.11194
757.3
312.3
10693
0 9356
0 2741
1.2097
2798 8
20e00
684.96
0 03134
0 07171
0.10305
770 7
285.1
1055.8
0.9468
02491
1.1958
28eg 8
2900e
690 22
0 03262
0 06158
0 09420
785 1
2543
1039 8
0 9588
0 2215
1.1803
29ee e
3000 8
695 33
0 03428
0 05073
0 08500
801.8
218 4
1020 3
0 9728
01891
1.1619
3ses e
3108 0
100 28
0 03681
0 03771
0.07452
824 0
169 3
993.3
0 9914
01460
11373
31sse
3700 8
705 08
0 04472
0 01191
0 0 % 63
875 5
56 I
931.6
1.0351
0 0482
1.0832
32ss e
98.2*
70547
0 05078
0 00000
0 05078
9F 'l
00
9060
1.0612
0 0000
1.0612
1733 2-
' Critical pressure
s
.
' . 5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE 22
THERMODYNAMICS
'
i
l
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIDI
j
BCl AN N AA6ENSN
,,
(tB STEg2.
CDP Y
- '
MASTER COPY
"
'
^" " "
.
REFERENCE
BW Westinghouse Reactor Theory Review Text,(I - 4.28)
ANSWER
5.02
(1.50)
a.
False
(0.75)
b.
True
(0.75)
REFERENCE
BW Westinghouse Reactor Theory Review Text (I-4.26)
ANSWER
5.03
(2.00)
a.
1.
Void coefficient
(0.4 each, 0.3 for correct order)
2.
Moderator temperature coefficient
3.
Doppler power (or fuel temperature) coefficient
b.
Total power coefficient becomes more negative from BOL to EOL.
(0.5)
REFERENCE
BW Westinghouse Reactor Theory Review Text (I-5.27) Figure I-5.22 (I-5.29)
ANSWER
5.04
(1.50)
a.
1.
Fission poison buildup
2.
Fuel depletion
(0.5 each)
b.
MTC becomes more negative as boron concentration decreases
(0.5)
REFERENCE
BW Westinghouse Reactor Theory Text, (I-5.31) (I-5.10)
. _ .
__-
_
_ _ _ - . _ _ - _
_ _ _ _
_ _ . _ . - - . - - -
.
-
. , 5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE 23
'
THERMODYNAMICS
'
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIDI
j
.
i
ANSWER
5.05
(3.00)
l
a. HIGHER (0.50) steam dump pressure setting decrease causes
RCS temperature to decrease. MTC and FTC both add positive
reactivity to increase pcwer. (0.50)
b. THE SAME (0.50) the steam dump system will compensate for
steam leak by shutting valves to maintain demanded steam
generator pressure. (0.50)
c. LOWER (0.50) the negative reactivity will cause power and TAVE to
decrease. Steam dumps will reduce steam flow to maintain a constant
steam pressure. . MTC and FTC will add positive reactivity to offset
boration (0.50)
.
REFERENCE
yM y
BW PWR Operations Systems D riptions, (24-21)
/ gg '
I
Westinghouse Reactor Theory ext (I-5.32) (I-5.49)
-
ANSWER
5.06
(1.50)
1. ? M 4
2. a (ACP higher)
3. b (ACP lower)
(0.5 each)
REFERENCE
BWGP 100-A8
ANSWER
5.07
(2.00)
a.
The instantaneous amount of reactivity by which the reactor is sub-
critical or would be subcritical from its present condition assuming
all full-length RCCAs are fully inserted except for the single RCCA of
highest reactivity worth which is assumed to be fully withdrawn.
(1.0)
(Full credit if paraphrased)
b.
It increases.
(1.0)
REFERENCE
BW Technical Specifications
BWGP 100-A8 Table 1
BW STM VOL 8 (58-8)
__
. _-
_ .
. ._
.
_
. . _ _ _
_ ____
. ' , 5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE 24
THERMODYNAMICS
,,
ANSWERS -- BRAIDWOOD 142
-86/10/22-HAAGENSEN, B./REIDI
-
'
'
t.
'
ANSWER
5.08
(1.50)
S/G heat transfer = Q = UA(Tavg - istm)
.
Q, U, and Tstm remain constant;
A1(Tavg1 - Tstm) = A2(Tavg2 - Tstm)
(0.5)
Given: A2 = 0.9 x Al
From Steam Tables: Tsat for 995 psia = 544 F
(0.5)
A1(587 - 544) = 0.9A1(Tavg2 - 544)
Tavg2 = 591.8 F (591 to 592.5 F acceptable)
(0.5)
REFERENCE
Steam tables
BW Thermal-Hydraulic Principles, VOL I (5-21, 22, 23)
ANSWER
5.09
(1.00)
c
REFERENCE
Steam tables
l
BW Thermal-Hydaulic Principles YOL I (5-21, 22, 23, 24)
ANSWER
5.10
(2.00)
I
a.
Increase
b.
Decrease
c.
Increase
d.
Decrease
(0.5 each)
REFERENCE
BW Thermal-Hydraulic Principles, VOL II pages (13-23, 24)
L
I
_
. . _ . - _ . _ _ _ _ _ _ _ - -
-
.
-- - - -
- - - -
- - - - -
- - - - - - - - -
--
- --- -
--
-
5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE 25
.
THERMODYNAMICS
,
.
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN,R./REIDI
.
.oS
{g;)
ANSWER
5.11
- .
a.
Natural circulation flow is produced by a PRESSURE DIFFERENTIAL
existing between two columns of water of DIFFERENT DENSITIES at
DIFFERENT HEIGHTS. Establishing natural circulation requires that a
HEAT SOURCE (decay heat from the reactor core) and a HEAT SINK (steam
generators) be present in the system, that the elevation of the heat
sink be higher than the heat source and that the heat sink capacity
match or exceed the heat source. As the coolant absorbs heat in the
reactor. coolant temperature and density decreases.
In the steam
,
i
generator, the coolant transfers its heat to the secondary system and
the colder, more dense water returns to the reactor vessel.
(Candidate should provide an explanation that discusses each of
the capitalized elements above. 0.20 points will be given for
each capitalized element of the answer.)
U$-e$*$htk
- b.
2.
.
c.
To determine flow in NC:
h=m'cpdelta-T
El cp1 (delta-TI)
i
.
>
g, .
.----------------
%
m2 cp2 (delta-T2)
h ml cp1 (delta-TI)
m2 =
4
.
Q
cp2 (delta-T2)
g
If the candidate assumes cp1 = cp2 then:
'
2% x 100% x 60 F
.
m2 = ----------------
4.3% flow
=
100%
x
28 F
If the candtdate determines cp1 and cp2 from the figure provided, then:
2% x 100% x 1.45 x 60 F
.
3.9% flow
m2
=
100%
x
1.60 x 28 F
(accept = or - 0.2% from answer)
(1.0)
.
REFERENCE
i
BW Thermal-Hydraulic Principles, VOL II pages (14-16, 17, 24, 25)
k ge
$ $ bt
N:: k A f85#
.
,
-
.
.
.
( (
j
eS
.$
g
U
O {'
h
M
Q,
"3
\\
N
Ea r9./Q)
--
. - .
- -
, 5.
THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE 26
THERMODYNAMICS
';
.
.
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN,B./REIDI
..
ANSWER
5.12
(2.00)
a.
Saturated
8.
Superheated
c.
Suparheated
d.
Subcooled
(0.5 each)
REFERENCE
Steam Tables
ANSWER
5.13
(1.0)
The delta-T of the fee &ater is not a true indication of heat transfer
through the U-tubes. Most of the HEAT ADDED TO A STEAM GENERATOR PROVIDES
THE HEAT OF VAPORIZATION NECESSARY TO CHANGE THE FEEDWATER INTO STEAM
at a constant temperature, and therfore is not accounted for in the
temperature rise of the feedwater.Almost all of the HEAT ADDED TO THE
REACTOR COOLANT IS SENSIBLE HEAT AND CAUSES A PROPORTIONAL RISE IN TEMP-
ERATURE in the RCS across the core.
(Candidate should provide minimum of capitalized information for full
credit. 0.5 points for latent heat concept and 0.5 points for
sensible heat concept.)
.
- 0.I J M
4 Q ,
t
a les
>
SW Thermal-Hydraulic Principles, Chapter 2-42 g
g
en .
_.
_. - - _ - _ _ _
- ._
_
-
- - -
-
_ - _ - _ - _ - _ . . - - - _ _ _
. - _ -
5.
THE0RY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND
PAGE 27
.
,
THERMDDYNAMIC5
s
.
.
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIO!
,
%
ANSWER
5.14
(2.50)
'
a.
Rhol = -2500 PCM = 0.025 delta k
Keffl = 1/(1-rho) = 1/(1-( .025)) = 0.9756
(0.5)
CR1/CR2 = (1-Keff2)/(1-Kef f1)
115/345 = 1/3 = (1-Keff2)/(1.9756)
(0.5)
,
Keff2 = 0.992. Rho 2 = -806 pcm
Reactivity added = -806 pcm - (-2500 pcm) = 1694 pcm
(+ or - 50 ppm)
(0.5)
b.
More neutron generations will be required for the neutron level to
reach equilibrium.
(1.0)
REFERENCE
Westinghouse Reactor Theory Review Text I-4.14
1
.
'
i
. - - _
_ _ _ _ _ - _ _ _ _ _ _ _ _ __
. _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ , _ _ _ _ .
. _ _ _ - _ _ . _ ,
_ _ _ _
. ---
_
.', 6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUENTATION
PAGE 28
' ;
AN,5WERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN,8./REIDI
,
.
ANSWER
6.01
(1.50)
NO.
(0.5)
Channel II must energize to actuate for an unsafe
condition (to avoid inadvertent spray actuation in the event
of a loss of instrument power).
(1.0)
REFERENCE
ANSWER
6.02
(2.00)
a.
Undercompensation results in a higher than actual reading, (0.50) d
With an IR instrument ndercompensated during a reactor
e,Chg
1 the P-6 setpoint (10-1 amps) will be reached early as
I--
%
' " * * "
j of counting neutrons and gamas. The operator may secu
source range instruments when P-6 comes in which result
b. 1.1 indication of neutron flux below the IR range,
the Source
I
channel
drops below the P-6 setpoint (0.50)
E
8
T V0L 4 (3 -5
-$,T DNk AeQ
cl &
4
-
4A
t
'@~g
N.
ANSWER
6.03
(2.50)
J
a.
Fail open
b.
Goes to VCT
Remain functional, closed')(O atuyd
3 ele ><
c.
d.
Remain functional, closed
g
e.
Fall open
'
4 tg ,,
(0.5 each)
N
REFERENCE
(pu
T
l
_ _ . .
.-
.-_
- , _ , - .
-
. . _ - , _ - - - - -
-
. -
- .
- _ - -
. - .
--
--
_ _ .
-
--
_
.
_6 . PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUENTATION
PAGE 29
-
1
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN,B./REIDI
.
..
ANSWER
6.04
(2.00)
a. POWER
b. INTERMEDIATE
c. INTERMEDIATE and POWER
d. INTEREDIATE and POWER
(0.5 each)
REFERENCE
BW STM VOL 4 (608 - 37/38)
BW STM VOL 4 (31 - 46)
,
ANSWER
6.05
(2.50)
1
a.
- Maintain backpressure on orifices to prevent flashing.
- Maintain RCS pressure when solid.
(0.5 each)
b.
SHUT
(0.5)
I
c.
Prevent (resin channeling due to) excess flow through demin
resin.
(0.5)
,
d.
HCV-182 (Charging flow control valve, Back pressure regulator or
RCP Labyrinth Delta-P Control Valve).
(0.5)
~
REFERENCE
ANSWER
6.0(C
(2.50)
1.k Sbow-low 5evel on 1 steam generatorL t:f,J irr, d
Nmk
_ .
.
p
C" * %
-
.r.%.
Safety Injection sequence signal
2. t Undervoltage on bus 141 (sequenced on)
g,h Undervoltage on 2/4 RCP busses (loss of offsite power)
>
(;;;, i :t .25 each)
b.
Manually by the operator at a CST level of 3%
(0.50)
Automatically shifts on low AFW oump suction pressure =
c.
with a setpoint of
1n Hg vacuum coincident witW: .I
.
1.
1gg.lcw
level stanals from any S/G
2. g RCP but undervoltane
/,l g
~
.g / . t f
3. Safety iniection saoueiice ,slignal
2.f
(0.25 for each signal - total of 1.0)
!
'd ur. d k
l.2.2"M b ANPMk
REFERENCE
g
BW STM YOL 3 CH 26 (26 - 40, 42) 4 gmg, A
g,ggMMMd
BWEP 0 foldout
b
{
8[4 A
.
p 4.
__
-
.
- _ _ _
.
- _-
6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUMENTATION
PAGE 30
,
'
ANSWERS -- BRAIDWOOD 182
-C6/10/22-HAAGENSEN, B./REIDI
.
s
ANSWER
6.07
(1.60)
a. 4
b. 5
c. 6
(0.4 each)
d. 1
REFERENCE
BW STM VOL 4 CH 28 PAGES 64, 65, 66
ANSWER
6.08
(1.50)
a.
Store a sufficient volume of water to maintain the RCS in Hot Standby
for 9 hours1.041667e-4 days <br />0.0025 hours <br />1.488095e-5 weeks <br />3.4245e-6 months <br /> while discharging steam to the atmosphere concurrent with
,
(1.0)
,
b.
0 0. . ;,et; ;; di d 2:: +% m h2ua alavated wrHaa =r::?;; i ..ss
'
ter i,. e k ;; the a,; ,;.. .. ,;;;fr:d ' :
g y g g g 0.5)
.
REFERENCE
BW Technical Specifications, section 3.7.1.3
ANSWER
6.09
(2.00)
,
a.
1.
Rising surge tank level
2.
Increasing CCW system radioactivity
3.
Increasing thermal barrier heat exchanger outlet temperature
(any two at 0.5 each)
b.
The CCW return valve (MOV 0685)for the RCP thermal barrier heat
exchanger will shut (0.5) on a high flow signal from the flow
indicating switch in that ifne.
(0.5)
REFERENCE
>
.-.
_ . _ . , - . - - _
.__.--____,.-m-
_ . _ _ _ _ _ . . . _ _ . . . . . , . , . ,
, . _ . . . - . . . _ _ _ .
6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUMENTATION
PAGE 31
-
,
' . -
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN,B./REIDI
,
,
ANSWER
6.10
(1.00)
b
(0.5 for each correct answer)
e
REFERENCE
ANSWER
6.11
(1.50)
b.
c.
e.
(0.5 each)
REFERENCE
ANSWER
6.12
(2.00)
a.
NO CHANGE
b.
DECREASE
c.
NO CHANGE
d.
DECREASE
(0.5 each)
'
REFERENCE
BW STM VOL 4 CH 28 (Figure 30b and page 28-70)
ANSWER
6.13
(1.40)
1.
Source range high flux
2.
RCP breaker tripped
3.
RCP low voltage
4.
RCP underfrequency
l
S.
Pressurizer low pressure
6.
Pressurizer high level
7.
Loop low flow
3
8.
(0.2 each - 7/8 required)
REFERENCE
i
BW STM Y0L 8 CH 60b Appendix A
- . -
'
. 6.
PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUMENTATION
FAGE 32
.
.'
ANSWERS -- BRAIDWOOD 142
-86/10/22-HAAGENSEN,8./REIDI
.
'
.
ANSWER
6.14
(1.00)
550 F (0,5); The six open steam dumps will cause Tave to decrease. At the
low low Tavg (P-12) setpoint, positio11ng air will be vented and all
steam dump valves will close (0.25). The six affected steam dump valves
will open when decay heat increases Tave above the P-12 setpoint and
reclose when the RCS temperature decreses below the P-12 setpoint thus
maintaining Tave around the P-12 setpoint. (0.25)
b8Sb !*g5td
l'% P % %i
stildy
REFERENCE
BW STM V0L 8 CH 60b Appendix A
b It, dlpreM hokInrthrtA(g
BW STM VOL 3 CH 24 (page 24-14)
C
y/
y
f, >L}'
) }y-
d,
T
ycl<f;v~lJ',
ph"
' " '
4' ,
, ,
$1
b 2
'
f+u/
gl
ya r
.
.sp g
de
.
p
y
Y
7p
)
G)e,
I
i
V
p
-
. - - - . - - -
.
, . ~ - . . . _ _ _ . . . - _ _ _ _ .
. . . . _ , - _ . . . _ _ . _ _ _ _ _ _ _
-____.-_-.__ _ _
,____,
_ .- _ _._. _ _____._ ____ .- -
__
,- --..___ - - -
7.
PROCEDURES - NORMAL, A8 NORMAL, EERGENCY AND
PAGE 33
,
RADIOLOGICAL CONTROL
,
.
'
ANSWERS -- BRAIDWOOO 182
-86/10/22-HAAGENSEN,B./REIDI
i
ANSWER
7.01
(2.25)
a.
1. Cogonent cooling water to RCP lost (affected pump only)
(0.25)
2. CNMT phase B is actuated
(0.25)
3. Both of the following conditions exist:
a. RCS pressure is less than 1370 psig (1670 psig for adverse
containment)
(0.25)
and
b. Coolant charging pump flow is greater than 200 gpm
(0.25)
'
or
Safety injection pumps have positive flow
(0.25)
b.
1. To prevent continued mass loss from a break (LOCA) (0.5) which may
result in prolonged core uncovery if RCPs were subsequently lost. (0,5)
,;
REFERENCE
,
i.
!
ANSWER
7.02
(1.00)
<
,
!
1.
Ur. controlled increase in steam generator level
2.
SJAE radiation abnormal
3.
SG blowdown radiation abnormal
.:
4.
Main steam line radiation
.
p
5.
SG radioactivity abnormal
(any 4 at 0.25 each)
REFERENCE
IBWEP-3
..
b
..
>
e
7.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 34
RADIOLOGICAL CONTROL
,
'
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIDI
..
ANSWER
7.03
(4.00)
a.
1.
Failure of more than one RCCA to fully insert following a reactor
trip.
2.
CRH below RIL.
3.
Inadequate shutdown margin.
4.
Unexplained or uncontrolled reactivity increase.
5.
Inability to borate normally.
,
'
!
(any four at 0.5 each)
b
1.
BATP through CV-8104.
2.
BATP and BORATE or MANUAL RMCS mode.
3.
The RWST through CV-1120/E and a charging pump.
4.
BATP through CV-8439.
(0.50 each)
REFERENCE
BW STM VOL 2 CH 15b Appendix A
ANSWER
7.04
( .50)
C'
n
t
REFERENCE
f;
BWEP ES-0.1 Attachment B
Y
K
jk
ANSWER
7.05
(1.00)
l ll
a.
False
(0.5)
}, ,
b.
True
(0,5)
I
REFERENCE
,
c'
c.
. . _ . .
7.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 35
-
'
RADfE.EICAL CONTROL
)
AN'SWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIDI
'
'
.
1
ANSWER
7.06
(3.00)
a.
100 F/hr
'
b.
100 F/hr
c.
50 F/hr
d.
50 F/hr
e.
50 ppm
f.
320 F
(0.50 each)
REFERENCE
-
BWOPs
ANSWER
7.07
(2.00)
,
a.
1.
564 F
(0.50)
20% p(ower(0.25) and after placing main FW regulating valves in
2.
AUTO 0.25)
3.
1.3fdeltak/k
(0.5)
'
b.
1. " ROD AT BOTTOM" (0.5)
.I
REFERENCE
l
BWGP 100-2 pages 1,2,5,9
y
.
ANSWER
7.08
(1.50)
,
'
a.
1.
RCS subcooling - not acceptable from iconic display or attachment A
lj
step A.
(0.5)
- .
2.
Pressurizer level cannot be maintained > 4% (38% for adverse
1
containment - not required for answer)
(0.5)
y ,t
b.
500 gpm
(0.5)
,
[i
REFERENCE
1BWCA-2.1 Foldout and page 2
)
ANSWER
7.09
(1.00)
.. -..h.
b- (ES)
$5
d. t y,)
_ _
- _
.
.
-
.
-
-
-
7.
PROCEDURES - NORMAL, ABNORMAL, EMERGENCY AND
PAGE 36
-
,
'
RADIOLOGICAL CONTROL
'
,
'
ANSWERS -- BRAIDWOOD 142
-86/10/22-HAAGENSEN,B./REIDI
l
e
REFERENCE
BWEP 0
' $ * / 6I
ANSWER
7.10
(2.50)
,
, ,. -
/-
a.
Less than or equal to 1 microcurie per gram dose equivalent I-131 (0.5)
and less than or equal to g microcuries per gram of gross
radioactivity. (0.5)
"
'
'
b.
1.
High radiation alert of alarm from the gross failed fuel monitor.
2.
High radiation alert or alarm or increase in radioactivity from~
any containment area monitor.
3.
Daily beta-ganne sample greater than 20 microcuries per cubic
centimeter.
(0.5eachII5$$$7en)
REFERENCE
1BWOA PRI-4
BW Technical Specifications 3.4.8
,
ANSWER
7.11
(3.00)
1.
a.
75 Rem
(0.5)
b.
25 Rem
(0.5)
2.
a.
Station superintendent
(0.5)
b.
CECO Medical Director
(0.5)
c.
Radiation Chemistry Supervisor
(0.5)
3.
True
(0.5)
REFERENCE
Connonwealth Edison Radiation Protection Standards
Personnel Exposures Under Emergency Situations (page 27)
. -
-_.
_ . _ - _ _
_
__
_
__ _ _
,' 7.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 37
-
-
RADIOLOGICAL CONTROL
,
..
,
.
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIDI
s
a
y,g up.n j.es IAC.
ANSWER
7.12
(2.00)
,
f
They have backup nitrogen accumulators and
be positioned f
"='=-@8TE N m %5;6tt d ra%cwthr -> ~ 1--)
a.
b.
To minimize RCS inventory loss (via the RCP seals). (0.5)
c.
To prevent injection of accumulator nitrogen into the RCS. (0,5)
d.
Continue depressurizing. (0,5)
'
REFERENCE
1BWCA-0.0
Westinghouse MCD CH 5
BW STM VOL 3 Chapter 23 Appendix D (23-60/61)
ANSWER
7.13
(1.25)
[0.25] xd ;t=: '
c'- - t- : br 00 F0ri.; (0. 1 (0.50)
a.
I':: *
,
b.
Draining and charging
Refueling pool cooling / recirculation
SI pump injection
Inject accumulators
(0.25 for each correct method, 0.75 max)
(o I)
k.
I.USC b
and Me4m 10 Ws
PR -9, 18w0A REFUEL-4
sna ut condensey. lo.8d
2. Osc,
W *aJ sdeem b Tc, Poed
sea ts.
t..sg.,tt..w)
[hP.11and Aen A ec.s [skei
to 1 &On Rwusrt.-q.} (o.as)
(0.254acA,Sof3de
,
P~@
~ */ a..a p u, L w
- ,%
-
.
( X.A 4 2.
- . - _
- -
- -
-..
a
~
'
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 38
-
E.
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN,B./REIDI
i
.
ANSWER
8.01
(2.00)
a.
Interval requirement not exceeded (0.5). Eight days
does not exceed 1.25 times the specified interval (0.5).
(1.0)
b.
Interval requirement exceeded (0.5). The last 3 consecutive
intervals exceed 3.25 times the specified interval (0.5).
(1.0)
.
REFERENCE
BW TS 4.0.2
ANSWER
8.02
(1.50)
Prevents a release of activity in event of a SGTR [1.0]
because the saturation pressure for 500 degrees is less
than atmospheric steam relief valve setpoint (0.5).
(1.5)
{ koY ~ 0:3G*f(sedidha
"g Ak*
REFERENCE
m c.e., 44mA $%
s'
g
4. S pop
y y,,c
)
BW TS B 3/4 4-5/6
y
ANSWER
8.03
(2.00)
a.
5
(0.5)
b.
The fire brigade shall NOT include the minimum shift crew required
for safe shutdown of Unit 1
(0.5)
and any personnel required for
essential functions during the fire. (0.5)
f
c.
The Cognizant Shif t Foreman is designated as the leader.
(0.5)
REFERENCE
BWAP 1100-1
BW Technical Specifications, Section 6
l
_._
.
. _ _ _ - . . _ _ - _ _ _
-_
_ - _ _ _ _ . _ _
. . _ _ _ _ . _ _ .
- - - -
- . _ _ _ _ - _
-
-
..
__
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 39
.-
,
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIDI
,
,
i
.
ANSWER
8.04
(2.00)
i
a.
Position
Modes 1,2,3 or 4
Modes 5 or 6
1
1
SF (licensed)
1
0
NSO
2
1
7
5
1
0
RAD and CHEM
personnel
2
2 (0.1 for each)
(1.2)
b.
2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br />
(0.5)
c.
thermal hydraulics, reactor engineering and plant analysis (0.3)
REFERENCE
BWAP 320-1
ANSWER
8.05
(2.50)
a.
1. 18 minutes
sy
(0.5)
2. 36 minutes
(or M minutes cumulative for 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> period)
(0,5)
(or g minutes cumulative for 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> period)
(0.5)
3. 41 minutes
b.
Imediately (as long as Delta-I remains in the target band) but
,
operation would be limited to 30 minutes at > 50% power by action
'
statement b.
Also accept when penalty decreases to < 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> in
previous 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.(Equivalent to 1614 on 2-19-86.)
(1.0)
,
REFERENCE
BW TS 3.2.1
BW TS 3.10.2.7
'
ANSWER
8.06
(2.00)
i
a.
NO (0.5)
b.
YES (0.5)
c.
Within 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br />, (0.5) take action to place the plant in
Hot Standby (0.5)
REFERENCE
BW Technical Specifications 3.0.3, 3.1.2.4, 3.5.2
i
i
.
.
.
. .
. .
. .
_ _ _ , . _ _ _ . _ . _
._.
._
_
_.
_
._.
. .
. _ . . _ _ _ _ _ _
__. .
.
8.
ADMINISTRATIVE PROCEDURES. CONDITIONS. AND LIMITATIONS
PAGE 40
,
' , . -
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, 8./REIDI
-
,
..
ANSWER
8.07
(3.00)
1.
Declaration of any emergency classiffcation.
2.
The initiation of any plant shutdown required by Technical
Spectffcations.
3.
Any authorized deviatton (10CFR50)from Technical Spectffcations.
4.
Any event or condition during operation that results in the condition
of the plant or safety barriers being seriously degraded, or results in
the plant being:
In an unanalyzed condition that signf ffcantly compromises plant
a.
safety, or
b.
Inaconditionthatisoutsidethedesignbasisoftheplant,or
In a condition not covered by the plant s operating and emergency
c.
procedures.
5.
Any natural phenomenom or external condition that poses an actual
threat to safety of plant or significantly hampers site personnel while
i
l
performing duties required for safe operation of the plant.
6.
Any event that results or should have resulted in ECCS actuation en a
valid sfgnal.
!
7.
Any event that results in a major loss of emergency assessment
capability.
.
8.
Any event that poses an actual threat to the safety of the plant or
.
significantly hampers site personnel while performing duties necessary
i
for safe operation of the plant including fires, toxic gas releases, or
radioactive releases.
3
"
9.
Any violation of a safety ifmf t.
(any 6 at 0.5 each)
,
'
(No. 4 counts as 4 separate conditions)
ec
cal Specifications
bE
,
3
3
e so.aes muti.-
et n=6denia.
(a) immediate not(heation. Each II.
.-
aa
....lately report any
ANSWER
8.08
(1.00)
events involving byproduct source, or
4
special nuclear material possessed by
)
the licensee that may have caused or
a.
(1.0)
threatens to cause:
)
(1) Exposure of the whole body of
REFERENCE
any individual to 25 rems or more of
,
radiation; esposure of the skin of the
8W Technical Speciffcations Deffnftions
whole body of any individual of ISO
rems or more or radiation; or esposure
of the feet, ankles, hands or forearms
of any individual to 378 rems or amore
of radiation;or
(2)The release of radionettve materi.
.
al in concentrations whleh. If averaged
!
ever a period of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, woult
i
exceed 8,000 times the liarJts specifier
'
for such materials in Appendis f
Table II of this part; or
f
(3) A loss of one working week
i
more of the operation of any facill'
-
affected; or
!
(4) Damage to property in esew
]
$300,000,
l
!
- -
- - - -
.
. - -
. -
- -
. - - -
- - .
_,
- -
_
.
-.
- _ -
l
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 41
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, B./REIDI
..
.
t
.
ANSWER
8.09
(2.50)
a.
15 minutes, 60 minutes
(0.5 each)
b.
False
(0.5)
c.
every hour
(0.5)
d.
60 minutes
(0.5)
REFERENCE
BWZP
.
ANSWER
8.10
(1.00)
No, the message must be sent.
(1.0)
REFERENCE
BWZP 300-2
.
ANSWER
8.11
(1.00)
-
b.
(1.0)
BWZP 200-1
ANSWER
8.12
(1.00)
a.
Shelter the 2 mile radius and 5 mile downwind sectors
(0.5)
b.
Take shelter or evacuate
(0.5)
-ru.f 1 L I . L.t _
f
-
'-
'
-
p-
alp acced MARS 3C,0 Q p}
REFERENCE
/
BWZP 380-4
dr Sg
[0,2g
aA sk ud646-s)afu(o.aq
ANSWER
8.13
(1.00)
[g $
-
Core cooling
(1.0)
Q
Qg
4e.@ k M*cd
MO
REFERENCE
BWAP 340-1
3
s
,
1
,
.
-
-
-.
- _ .
.-
.- .
.
--.
.
- . . _ _ .
- *
8.
ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS
PAGE 42
.
.**
ANSWERS -- BRAIDWOOD 182
-86/10/22-HAAGENSEN, 8./REIDI
.
.
s
-
ANSWER
8.14
(2.50)
a.
check in the shut direction and restore to original position
(0.5)
b.
remove locking device, check in the shut direction, restore to original
position, lock
(0.5)
c.
check in the shut direction
'
(0.5)
d.
verify valve and controller are lined up for auto operation and valve
position is correct for existing conditions.
(0.5)
e. s.close valve counting the number of turns until the valve seats, restore
the valve to its proper position by opening it the same number of turns [.Q.5
that it was closed
. - ws gT., T e t 8 is 67)
bo
M {g
g,
, ,
. . .
,
-
"g!"!"g2
a.3 AAAA A
( re,nw ,,. ae r.4emn= t.u.)
- Ata oo-A % M
1
% $ ( TM e
4 M41 A--d4
8TA % -a.
cF**le A4l h%
a &-Q
akkd
" % p] $ 4 4 A%m'L A A
!
!
.A~ir~ik,.
@
c
!
%A
A A A */b # p dr
-A A.
M 4(*, p- )
i
.
.
'
~%I
Ws~
!
- O (A41.g
.
!
'
!
!
l
i
t
I
- - - - -
-
-.
-
-
~
MASTER COPY
- su -
...
.
U. S. NUCLEAR REGULATORY COPNISSION
REACTOR OPERATOR LICENSE EXAMINATION
i
FACILITY:
BRAIDWOOD 182
REACTOR TYPE:
PWR-WEC4
DATE ADMINISTERED: 86/10/22
EXAMINER:
WEALE, G./REIDINGER
CANDIDATE:
INSTRUCTIONS TO CANDIDATE:
Use separate paper for the answers. Write answers on one side only.
Staple question sheet on top of the answer sheets.
Points for each
question are indicated in parentheses af ter the question. The passing
grade requires at least 70% in each category and a final
grade of at
Icast 80%. Examination papers will be picked up six (6) hours after
the examination starts.
% OF
CATEGORY % OF
CANDIDATE'S CATEGORY
YALUE
TOTAL
SCORE
VALUE
CATEGORY
25.00
25.00
1.
PRINCIPLES OF NUCLEAR POWER
PLANT OPERATION, THERMODYNAMICS,
HEAT TRANSFER AND FLUID FLOW
25.00
25.00
2.
PLANT DESIGN INCLUDING SAFETY
AND EMERGENCY SYSTEMS
25.00
25.00
3.
INSTRUMENTS AND CONTROLS
25.00
25.00
4.
PROCEDURES - NORMAL, ABNORMAL,
EMERGENCY AND RADIOLOGICAL
CONTROL
100.00
Totals
Final Grade
All work done on this exami .ation is my own.
I have neither given
nor received aid.
Candidate's Signature
_ _ _ _ _ _ _ .
_ _ .
_
- .
-
.
-
-
_
.
'*
' '
'
NRC RULES AND GUIDELINES FOR LICENSE EXAMINATIONS
During the administration of this examination the following rules apply:
,*
1.
Cheating on the examination means an automatic denial of your application
and could result in more severe penalties.
'
,
2.
Restroom trips are to be limited and only one candidate at a time may
leave. You must avoid all contacts with anyone outside the examination
room to avoid even the appearance or possibility of cheating.
3.
Use black ink or dark pencil only to facilitate legible reproductions.
4.
Print your name in the blank provided on the cover sheet of the
'
examination.
5.
Fill in the date on the cover sheet of the examination (if necessary).
l
6.
Use only the paper provided for answers.
7.
Print your name in the upper right-hand corner of the first page of each
section of the answer sheet.
Consecutively number each answer sheet, write "End of Category 'ne" side
8.
'
as
appropriate, start each category on a new page, write only on o
,
of the paper, and write "Last Page" on the last answer sheet?
'
9.
Number each answer as to category and number, for example,1.4, 6.3.
10. Skip at least three lines between each answer.
11. Separate answer sheets from pad and place finished answer sheets face
down on your desk or table.
12. Use abbreviations only if they are commonly used in facility literature.
13. The point value for each question is indicated in parentheses after the
question and can be used as a guide for the depth of answer required.
14. Show all calculations, methods, or assumptions used to obtain an answer
!,
to mathematical problems whether indicated in the question or not.
I
15. Partial credit may be given. Therefore, ANSWER ALL PARTS OF THE
QUESTION AND DO NOT LEAVE ANY ANSWER BLANK.
16. If parts of the examination are not clear as to intent, ask questions of
the examiner enly.
17. You must sign the statement on the cover sheet that indicates that the
.
work is your own and you have not received or been given assistance in
completing the examination. This must be done after the examination has
been completed.
,
I
4
,
-n
--.--.-.-,-.-n-.._.,--_,,,---,,,_.,,-.-.__,,._,-..,,,..-.,.,..n,.,
- . , .
,,,,,,,-.----..,,--,_,p
n,, , - - - - ,. ,
. -
' -
.
18. When you complete your examination, you shall:
,
a.
Assemble your examination as follows:
(1) Exam questions on top.
(2) Exam aids - figures, tables, etc.
(3) Answer pages including figures which are part of the answer.
b.
Turn in your copy of the examination and all pages used to answer
the examination questions.
Turn in all scrap paper and the balance of the paper that you did
c.
not use for answering the questions.
d.
Leave the examination area, as defined by the examiner.
If after
leaving, you are found in this area while the examination is still
in progress, your license may be denied or revoked.
!
l
l
'
, . _ _ _ _ . . _ _ _ _ _ . . _ _ _ .
. . . - . -
- - - - - - - -
- - - - - - - - - - - - - - - - - - - - - - - - t
_ _ _
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE
2
THERMODYNAMICS, HEAT 1RANSFER AND FLUID FLOW
., .
.
.
,
QUESTION 1.01
(2.00)
With the plant at 70% power and all systems in automatic, how AND why is
operating Shutdcwn Margin affected(INCREASE, DECREASE, NO CHANGE)
by the following occurrer.ces? EXPLAIN YOUR ANSWER.
a. RCS Boron concentration is increased by 10 ppm.
(1.00
b. Power is increased by 10% without dilution.
(1.00)
QUESTIOR 1.02
(3.00)
An Estimated Critical Position (ECP) is calculated for a reactor startup
to be performed 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> after a trip from a month at 100% power near EOL.,
If the following events or conditions occur, but the same ECP is used,
state whether the Actual Critical Position (ACP) is HIGHER THAN, LOWER THAN,
or the SAME as the ECP and explain WHY.
Consider each event or condition separately.
a. The startup is delayed for 8 more hours after the trip.
(0.75)
b. The startup is delayed for 8 days after the trip.
(0.75)
c.
The steam dump pressure setpoint is increased by 75 psig.
(0.75)
d.
All steam generator it:yels are being raised by 5% as criticality is
being approached.
(0.75)
QUESTION 1.03
(2.00)
Considering their production and removal rates, explain why:
a. Equilibrium concentration of Xenon increases as reactor power increases
(1.0)
b. Equilibrium concentration of Samarium remains constant regardless of
reactor power level.
(1.0)
(***** CATEGORY 01 CONTINUED ON NEXT PAGE *****)
. _ - _
_ - _ _ - -
_ _
. . -
-_
._
-
-
.
-
.
1.
PRINCIPLES OF NUCLEAR. POWER PLANT OPERATION,
PAGE
3
THERMDDYNAMICS, HEAT TRANSFER AAD FLUID FLOW
-
.
.
,
.
QUESTION 1.04
(1.50)
A motor-drivin, variable-speed centrifugal pump is operating at 1/4 speed
in a " closed" cooling water system with the following parameters:
(a) Current = 20 amps
(b) Flow = 50 gpm
(c) Pump delta-P = 8 psid
What are the new values for these parameters when the pump is shifted to
full rated speed?
(1.50)
QUESTION 1.05
(2.75)
a. Select / match one equation from the right-hand column that applies to
each of the following heat transfer rates in a steam generator (SG) (0.75)
.
.
a)
Q = mCp At
1) Rate of heat gain by feedwater/ steam
b)
h = UA AH
2) Rate of heat loss by reactor coolant
.
.
c)
Q = mCp AH
3) Rate of heat transfer thru SG tubewalls
.
.
.
.
d)
Q = WfAH
mh Idf = lJp
e)
h = UA AT
b. Define the following symbols / terms used in the above equations AS THEY
APPLY TO A STEAM GENERATOR.
(2.0)
.
1) m
2) Cp
3) At
4) U
5) A
6) A H
7)hf
sek hf3 $)p
8) AT
(***** CATEGORY 01 CONTINUED ON NEXT PAGE *****)
!
1
l
_,
.-, .
,
. - - . -
. . -
- . -
- .
. - . - - - -..
- - - - - -
-
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE
4
THERMODYNAMICS, HEAT TRANSFER AND FLUID FLOW
,
,
,
.
QUESTION 1.06
( .75)
'
In a simple " closed" cooling water system (similar to the CCW system, but
with just one centrifugal pump, a surge tank, and a heat exchanger loop),
the isolation valve in the line to the surge tank is inadvertently shut and
the pump discharge flow-control valve is fully opened. Soon afterward the
pump starts operating noisily and vibrating excessively due to cavitation.
In this situation:
<
a. What are 2 reasons why shutting the pump discharge flow-control valve
halfway shut will stop the pump vibrations / noisy operations?
(0.5)
b. What is 1 reason why opening the surge tank isolation valve halfway
open will stop the pump vibrations / noisy operations?
(0.25)
QUESTION 1.07
(3.00)
With the reactor subcritical at a shutdown margin of 2.5% delta-k/k,
the stable count rate is 135 cps.
a. How much reactivity is required to be added to increase the stable
count rate to 405 cps? SHOW ALL WORK.
(2.25)
b. If the reactivity of part a is inserted in small, equal-reactivity
steps with the rods, will it take longer for the subcritical reactor
to reach a stable count rate near 150 cps or near 400 cps? WHY? (0.75)
QUESTION 1.08
(2.00)
With the plant operating at 100% power, a reactor trip and turbine trip
occur. Explain WHY steam generator levels change.
I
I
,
(***** CATEGORY 01 CONTINUED ON NEXT PAGE *****)
. ,_
_._ __ ____.
---_-_
. . _ _ _ _ _ _ _
. - -.
-
--
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE
5
THERMODYNAMICS, HEAT TRANSFER AND FLUID FLOW
.
.
.
,
,
-
.
.
QUESTION 1.09
(3.00)
Concerning tegerature coefficients important to reactor control;
)< l Pea /*tc)
a. When Braidwood commences power operations (Cycle fl,BOL), the moderator
temperature coefficient (MTC) will be very small at the hot, zero power
n
condition. In view of this, explain WHY a large RCS dilution will be re-
quired for a power increas
o 100% power, even though Tavg will
increase during the power increase.
(1.50)
b. Explain why at end-of-life (EOL), the amount of RCS dilution required
for a power increaseyto 100% will be much more than at BOL.
(1.50)
0%
QUESTION 1.10
(2.00)
With the plant steady-state near 100% power at BOL on Cycle 1, Boron con-
centration at 1200 ppm and Tavg 587 F, a boration of 60 ppm is required to
compensate for a 600 pcm power defect due to a power decrease to 50% power.
Would the required boration be GREATER THAN, LESS THAN, or EQUAL TO 60 ppm
for the same 600 pcm gained by a power decrease if the following initial
condition change is made?(Only the listed condition changes; other initial
conditions stay the same.) EXPLAIN WHY FOR EACH ANSWER; CONSIDER EACH
CHANGE SEPARATELY.
a. Boron concentration is 900 ppm
(1.00)
b. Tavg is 572 F
(1.00)
QUESTION 1.11
(3.00)
With the plant stable at 80% power near BOL, which way will the Axial Flux
Difference initially change (MORE NEGATIVE or LESS NEGATIVE) for the
following occurrences? EXPLAIN YOUR ANSWER.
CONSIDER EACH OCCURRENCE SEPARATELY
a.
Xenon starts building in to the bottom of the core (1.00)
b.
OTdelta-T runback occurs with rods in automatic (1.00)
c.
A momentary large feed flow increase occurs with rods in manual (1.00)
(***** END OF CATEGORY 01 *****)
...
.-
-.
-
.
-
-
.
.
2.
PLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS
PAGE
6
.
,
.
.
[
f
N8
'
6
\\
'
'
,
.
QUESTION 2.01
(1.00)
What are 2 purposes for the flow orifices in the Aux Feed Water supply
lines to the steam generators?
QUESTION 2.02
(2.00)
a. If the "0" Component Cooling Water (CCW) pump is initially in standby,
what CCW pump switch lineup condition /s are required for the "0" pump to
y
start automatically on an autostart signal? Q g gym) (0.5)
b. With the correct puI
eup, what 3 occurrences / signals will cause
the "0" Component Coofing Water pump to start automatically?
(1.5)
QUESTION 2.03
(2.00)
What VALVES in what PIPING LINES prevent main turbine overspeeds that may
occur when the generator has tripped and all main turbine throttle valves
and governor valves have shut?
QUESTION 2.04
(2.00)
Manual actuation of the Phase A Containment Isolation will close 4 sets of
valves associated with CVCS piping or components in the containment
building,
a. List the 4 sets of valves (noun name or function is sufficient)
(1.0)
b. Is long-term critical operation of the plant possible with Phase A Cont-
ainment Isolation manually actuated? EXPLAIN YOUR ANSWER.
(1.0)
QUESTION 2.05
(3.00)
List the 4 sources AND flow paths of boron solution used for Emergency
Boration. INCLUDE the approximate flow rate from each source.
1
1
(***** CATEGORY 02 CONTINUED ON NEXT PAGE *****)
__ ._.
.
.
.-
_
_.
-
_ _ -
. - . -
2.
PLANT DESIGN INCLUDING SAFETY AND EERGENCY SYSTEMS
PAGE
7
-
..
.
1
.
QUESTION 2.06
(1.50)
During a continuous RCS depressurization caused by a major LOCA at 1005
'
power, indicate the order (highest to lowest pressure) in which the
.
'
specific ECCS subsystems will inject into the RCS ANO show the approximate
pressure at which each subsystem will start to inject.
QUESTION 2.07
(2.00)
When a worker accidentally (cuts through the energized control power cable
to the 1A diesel generator DG) control panel, the resulting current surge
trips the 125vdc power supply breaker for Bus 111 and damages that breaker
such that it cannot be closed again. Neither the bus supply breaker nor
the 1A DG control power cable can be repaired or replaced for a week.
In the interim, until repairs can be completed, state the major steps
required to restore power to:
a. 125V Bus 111
(1.0)
(1.0)
QUESTION 2.08
(1.50)
a. Explain why operation ofthe main generator under reverse power cond-
itions is undesirable.
(0.75)
b. What are 3 reasons for the time delay on the main generator reverse
power trip?
(0.75)
QUESTION 2.09
(1.75)
a. What is the purpose of the #1 seal bypass ifnes on the RCPs?
(0.75)
b. What are the upper and lower pressures at which the bypass
valve (CV-8142) must be shut AND what is a reason for each pressure limit?
(1.0)
(***** CATEGORY 02 CONTINUED ON NEXT PAGE *****)
I
. - - - _
_
-
.
.
.
- .
.
. .
_ - . _ . _ _ _ _ _ , _ _ . _ . . _ _
. - . _ , _ _ _ . _
,
-
-
--
-
_
.
2.
PLANT DESIGN INCLUDING SAFETY AND EERGENCY SYSTEMS
PAGE
8
,
.
.
.
QUESTION 2.10
(1.00)
a. List 2 CCW system indications in the Control Recm of a 1 gpm leak in
the in-use CVCS letdown heat exchanger.
(0.5)
b. Why is it likely that the leak is NOT in the non-operating ("not-in-use")
heat exchanger?
(0.25)
c. How can you confirm that the leak IS in the in-use heat exchanger?(0.25)
QUESTION 2.11
(1.50)
State 6 conditions required for the autoclosure of the diesel generator
feeder breaker ACB 1413 without synchronizing during an emergency.
(1.5)
QUESTION 2.12
(2.50)
a.1.ist 4 design features of the Spent Fuel Pool Cooling and Cleanup System
that prevent inadvertent draining of the Spent Fuel Pool below the tops
of the stored cells?
(2.0)
b. If all the NEW fuel cells for Unit 1 are temporarily stored in the
Spent Fuel Pool and the pool is inadvertently filled from the primary
water storage tanks, explain WHY an inadvertent criticality can/cannot
-
occur?
(0.5)
QUESTION 2.13
(1.25)
List 5 trips or automatic functions that occur when Breaker 41 (Main Gen-
erator Voltage Regulator Supply Breaker) trips.
l
r
(***** CATEGORY 02 CONTINUED ON NEXT PAGE *****)
l
l
.
. . -
. .- - -
.
. .
- - . -
- - . . . -
- - .
- - - .
-
_.
2.
TLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS
PAGE
9
-
.
.
,
,
'
QUESTION 2.14
(2.00)
Indic'te the water source (suction location) and SPECIFIC discharge
a
location (s) for the following 4 functions of the RHR system as part of the
Emergency Core Cooling System (ECCS).
a. Low head injection
(0.5)
b. Supply to other pumps
(0.5)
c. Cold leg recirculation
(0.5)
d. Hot leg recirculation
(0.5)
.
I
.l
l
(***** END OF CATEGORY 02 *****)
i
-
,.
. . _ . - .
- . . _
. - , - - . - . _ . - . - - . - - _ . _ . . , , - .
_
, _ - , . . - _ .
- ---. . . ,,
3.
INSTRUMENTS AND CONTROLS
PAGE 10
-
.
.
,.
e-
..
,
,
'
QUESTION 3.01
( .50)
Which one of the following conditions will actuate the Rod Control Urgent
Failure annunciator light?
a. A data error in one data cabinet
b. A logic error in one power cabinet
c. A failed oscillator in one power cabinet
d. A failed 25vdc power supply in one power cabinet
e. A failed 16.5vde power supply in the logic cabinet
QUESTION 3.02
(1.00)
During initial fuel load, the Shift Supervisor announces that an I&C tech
will be swapping the N42 and N43 power range Channel B drawers for trouble-
shooting. State 2 reasons why the SR0 should NOT permit the ISC tech to
do the power range swap.
QUESTION 3.03
(2.50)
Briefly .N. .R the interlock functions actuated whep the Alert Alarm
A
nc
cccurs on the following radiation monitors. (Nhaf
/
2.5)
a. ORE-AR055(FUEL BUILDING HANDLING INCIDENT)
b. ORE-PR009(CCW HEAT EXCHANGER "0" WATER OUTLET MONITOR)
c. ORE-PR031(CONTROL ROOM OUTSIDE AIR INTAKE A MONITOR)
d. 1RE-PR008(STEAM GENERATOR BLOWDOWN MONITOR)
o. 1RE-PR027(SJAE/ GLAND STEAM EXHAUST MONITOR)
l
(***** CATEGORY 03 CONTINUED ON NEXT PAGE *****)
l
_ -
.
_.
-
-.
_
_ _ _ _ _ .
---
.
3.
INSTRUMENTS AND CONTROLS
PAGE 11
-
.
.
..
i
.
QUESTION 3.04
(1.50)
a. List the 4 input signals to the S'Jbcooled Margin Monitor.
(1.0)
b. Under normal conditions at 100% power, what are the values of the
following? (Steam tables excerpts provided)
1) pressure margin to saturation
2)tenperature margin to saturation
(0.5)
.
QUESTION 3.05
(1.50)
On the steam dump control system, describe the difference between the
Loss of Load (or Load Rejection) controller and the Turbine Trip (or Plant
Trip) controller with regard to the following:
a. Arming requirements or signals
(0.5)
b. Input parameters or signals
(0.5)
c. Time delays or deadbands
(0.5)
QUESTION 3.06
(2.25)
During a plant power increase from 15% to 100% the steam pressure detector
for the selected steam flow channel on SG 1A sticks at the 15% position.
Explain the effect of the stuck steam pressure detector on the following:
a. IA SG inoicated steam flow versus actual steam flow
(0.75)
b. lA SG 1evel versus normal level at 100% power
(0.75)
c.1B main feed pump speed versus normal speed at 100% power
(0.75)
(***** CATEGORY 03 CONTINUED ON NEXT PAGE *****)
_.
..
.. -
__ . - _ _ - - -
- _ _
- - _ _ - _ - - _ ,
_ .
.
_
_
_ _ _ _
. _ _ .
_
. _ . . _ .
3.
INSTRUMENTS AND CONTROLS
PAGE 12
-
.
.
.
.
.
QUESTION 3.07
(2.25)
For the following actions / occurrences, state the:
1) Steam dump control system response,
2) The plant response, and
3) The resulting method of RCS temperature control
Assume all systems operate normally except as stated and that no operator
'
action is taken. CONSIDER EACH CASE SEPARATELY.
a.
With the plant in Hot Standby, steam pressure mode of control, waiting
for a reactor startup, the steam pressure setpoint is reduced by
200 psi.
(0.75)
b.
While in the steam pressure mode of control at 5% power, the train A
Steam Dump Interlock Bypass Selector Switch is placed in the
(0.75)
"off" position
~
c.
The train B reactor trip breaker fails to open on a reactor trip signal
while at 78% power. NOTE: The train A breaker opens properly. (0.75)
QUESTION 3.08
( .75)
Indicate whether the following statements concerning operation of the
reactor trip (RT) and bypass (BY) breakers are TRUE or FALSE.
a.
If RPS train A is placed in test while bypass breaker BYB is closed,
both reactor trip breakers and both bypass breakers will trip.
(0.25)
b.
If an attempt is made to close both bypass breakers at the same time,
both bypass breakers will trip, but the reactor trip breakers will
remain closed.
(0.25)
c.
A solid state protection system (SSPS) train A reactor trip signal will
'
trip all RT and BY breakers.
(0.25)
1
,
)
(***** CATEGORY 03 CONTINUED ON NEXT PAGE *****)
-
. .
.
.
. . .
.
.
...
-
.
. .- .-
.
3.
INSTRUENTS AND CONTROLS
PAGE 13
.
.
..
.
.
QUESTION 3.09
(1.25)
Match the following reactor protection and control signals in Column A
~
to their associated logic coincidence in Column B.
(1.25)
COLUMN A
COLUMN B
a.
RCS loop loss of flow trip (per loop)
1.
1/2
2.
2/2
b.
P-6(Source range turn-on on power decrease)
3.
1/3
4.
2/3
c.
P-10 (Nuclear at power)
5.
1/4
-
6.
2/4
d.
Pzr high pressure trip (pressure increase)
7.
3/4
e.
Power range high power rod stop (power increase)
QUESTION 3.10
(1.00)
What are 2 conditions (including setpoints if applicable) under which the
pressurizer level control system actuates the pressurizer heater controls?
Include WHY.
QUESTION 3.11
(1.50)
With the plant at 80% power and all systems in automatic control, state
the initial direction of rod motion for the following conditions or
occurrences. EXPLAIN your answer. Consider each condition separately.
a.
Loop 4 Tcold fails high.
(0.5)
b.
ure transmitter PT-505 fails high
(0.5)
c.
A spurious main turbine runback occurs
(0.5)
QUESTION 3.12
(1.00)
Why is a variable-gain circuit included in the rod control system power
cismatch circuitry?
(***** CATEGORY 03 CONTINUED ON NEXT PAGE *****)
_
^
3.
INSTRUMENTS AND CONTROLS
PAGE 14
. .
.
.
.
'
QUESTION 3.13
(1.00)
List the conditions or signals that will cause automatic closure of the
Main Feedwater Isolation Valves (1FW-009A,B,C D).
QUESTION 3.14
(2.00)
a. List all parameters or concitions WITH setpoints (as applicable) that
will prevent automatic AND manual rod withdrawal.
(1.4)
b. List all parameters or conditions WITH setpoints (as applicable) that
will prevent rod withdrawal in automatic ONLY.
(0.6)
QUESTION 3.15
(1.00)
Identify the control, protective, and permissive functions which use
individual loop Tavg signals and NOT auctioneered Tavg.
QUESTION 3.16
(1.50)
List ALL automatic start signals for the motor-driven aux feed pump 1A.
INCLUDE coincidence logic if applicable.
'
QUESTION 3.17
(1.75)
a. With the plant at 100% power and the Pressure Channel Selector Switch
set on Channel 1(IPT-455), list 3 insnediate pressurizer system responses
if pressure transmitter 1PT-455 fails HIGH.
(0.75)
b. If N0 operator action is taken for the IPT-455 failure, list 4 resulting
system actions.
(1.00)
QUESTION 3.18
( .75)
List the 3 separate functions of overspeed protection provided by the
everspeed protection controller in the Main Turbine Control and Protection
System.
(***** END OF CATEGORY 03 *****)
_ _ _ - _ -
_
_.
-
- - - -
. _ . - _ _
_- . - _
.
.
.-
__.
. _
_ .
..
.
_ - _ - _ _-
4.
PROCEDURES - NORMAL,. ABNORMAL, EMERGENCY AND
PAGE 15
.- , RADIOLOGICAL CONTROL
,,
.
QUESTION 4.01
(1.50)
Per the Technical Specifications, if the plant is at 2% reactor power,
and Tavg drops to 547F due to excessive warmup of the steam lines;
1) What action must be acconplished?
(0.75)
2) If action 1 cannot be accomplished, what other action must be taken?
(0.75)
(INCLUDE time limits in 1 and 2 if applicable)
1
QUESTION 4.02
(2.50)
A 24 year old male had a lifetime exposure of 23 REM through last quarter.
In addition to his lifetime exposure, he has also received I rem in
-
the present quarter.
a. In accordance with 10CFR20, what 3 provisions must be met to allow
this individual, in a non-emergency situation, to exceed the quarterly
regulatory limit?
(1.50)
b. Whose approval is needed to allow this individual to exceed the
quarterly regulatory limit?
(0.5)
c. How long may this individual work in a 200 mrem /hr radiation field
before he reaches the maximum quarterly limit allowed at Braidwood?
(0.5)
QUESTION 4.03
(1.50)
Per the Braidwood Tech Specs, if the plant is being maintained in hot
standby (Mode 3):
a.
What is the shutdown margin Ifmit?
(0.25)
l
b.
How often must the shutdown margin be checked?
(0.25)
c.
If the shutdown margin limit is not met, what required actions must be
taken? INCLUDE numbers (if applicable).
(1.0)
(***** CATEGORY 04 CONTINUED GN NEXT PAGE *****)
4.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 16
,RADIDLOGICAL CONTROL
,
,,
.
QUESTION 4.04
(1.00)
List four (4) entry conditions from the Emergency Procedures which require
transitioning to IBwEP-3, Steam Generator Tube Rupture?
l
QUESTION 4.05
(1.50)
18wEP ES-1.3, Transfer to Cold Leg Recirculation, contains the following
Caution: SI PUMPS MUST BE STOPPED IF RCS PRESSURE IS GREATER THAN THEIR
SHUT 0FF HEAD PRESSURE. What is the reason for this caution and why is it
included only in the Transfer to Cold Leg Recirculation procedure?
QUESTION 4.06
(1.00)
List the four " Design Basis Accidents" which the ECCS systems are designed
to mitigate.
QUESTION 4.07
(1.50)
List all Critical Safety Functions from highest to lowest priority.
-
QUESTION 4.08
(1.50)
List the 3 methods provided to cool and depressurize a Steam Generator with
a tube rupture per 18wEP-3, Steam Generator Tube Rupture.
QUESTION 4.09
(1.75)
Bw0A PRI-9(Loss of Shutdown Cooling) instructs the operator to establish
alternate decay heat removal if BOTH RHR trains should fail and NOT be
capable of restoration to operability,
a.
List two (2) alternate decay heat removal methods provided in the
procedure for the following plant conditions: RCS temperature 300 F.
RCS pressure 300 psig, all systems other than RHR operable.
(1.00)
b.
List three (3) alternate decay heat removal methods provided for if the
vessel head is removed.
(0.75)
(***** CATEGORY 04 CONTINUED ON NEXT PAGE *****)
-
-
_ _ .
.
-
.
- .
.
.
- - .
- - - .
. -
. - . - . .
-
4.
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 17
, RADIOLOGICAL CONTkOL
,
,
,
QUESTION 4.10
(2.25)
With the plant at 85% power and all systems in automatic, and N0 operator
actions in progress, the following symptoms are suddenly observed in
relatively quick succession:
,
,
a. Flow indicated on 1FY-0111, PRIMARY WATER CONTROL PREDET COUNTER,
,
b. Control rods inserting,
'
c. Actuation of annunciator 1-10-B6 ROD BANK LOW INSERTION LIMIT, and
d. Decreasing Boron Concentration Meter reading.
Shif ting the Makeup Control Switch to STOP does NOT change these symptoms.
What three (3) Main Control Board switch actions or operations should be
taken for these symptoms and WHY?
QUESTION 4.11
( .50)
For a dropped control rod with no reactor trip, the initial method of
removing / responding to the Tave/ Tref mismatch is which of the following?
a.
Controlling main turbine load.
b.
Taking manual control of individual control rod banks,
c.
Shifting to low load operation on the main turbine
d.
Boration and/or dilution of the reactor coolant system.
QUESTION 4.12
( .50)
Which of the following radiation exposures will inflict the greatest
biological damage?
a.
1 Rem of ALPHA
b.
1 Rad of NEUTRON
c.
1 Roentgen of BETA
d.
1 Rad of GAMMA
(***** CATEGORY 04 CONTINUED ON NEXT PAGE *****)
- -
.
-
- -- . .
-
-.
.
-
-_.
.__.
_ _ . _
.-
. - -
- . .
.
.
.
-
-
. . -
. .
.
.
.
..
4.
PROCEDURES --NORMAL, ABNORMAL, EERGENCY AND
PAGE 18
,, , RADIOLOGICAL CONTROL
,,
.
QUESTION 4.13
(1.00)
Complete the following statements using info from the Precautions and
Limitations sections of the Plant Heatup procedure (BwGP 100-1).
a.
For normal heatup of the pressurizer, a rate of
F/ hour
i
will not be exceeded.
(0.25)
i
b.
Spray flow into the pressurizer will NOT be initiated if the
temperature difference between the Pzr and Spray fluid exceeds
i
F.
(0.25)
l
c.
Administratively, RCS oxygen must be in specification prior to
exceeding
F.
(0.25)
'
d.
Heatup must be terminated or spray initiated if pressurizer
boron concentration approaches
ppm less than RCS loop (0.25)
concentration.
QUESTION 4.14
(2.00)
According to function restoration procedure IBwFR-S.1 " Response to Nuclear
4
Power Generation /ATWS" Step 2, the operator is to verify turbine trip. If
the turbine has not tripped, he should manually trip it. List the sequence
cf actions he should take if the turbine does not respond to his actions.
QUESTION 4.15
(1.50)
l
According to the BW Precautions, Limitations, and Setpoints book, all
reactor trip and safeguard actuation channels, except 3, shall be placed
in the trip mode when the channel is out of service for any reason. List
the 3 excepted circuits / trips that may be bypassed for maintenance. (1.5)
l
i
l
QUESTION 4.16
(3.50)
a. List 2 criteria (WITH limits if applicable) that require emergency
boration during refueling operations.
(1.0)
!
b. List 5 criteria (WITH limits if applicable) that require emergency
boration during operations at 98% power.
(2.5)
,
l
4
(***** END OF CATEGORY 04 *****)
l
(************* END OF EXAMINATION ***************)
- -
.
.
.
- .
.
.
. .
. .
.
. .
--
.. .
--
.
___
.. .
.o
.
EQUATION SHEET
f = ma
v = s/t
Cycle efficiency = (:tet work
'
out)/(Energy in)
2
w = ag
s = V,t + 1/2 at
2
E = mc
2
-at
KE = 1/2 av
a = (Vf - V,)/t
A = AN
A = A,e
PE = agn
Vf = V, + at
w = e/t
i = an2/t1/2 = 0.693/t1/2
1/2*ff = C(tui)(t)3
2
d
w
, ,p.
,n
A=
[(t1/2)*III)
4
b
- E " 93 I "
m = V,yAo
-b
y,
.
.
Q = mCoat
Q = UA A T
I " I ',
o
/TVL
Pwr = W ah
I*I
10
f
o
TV1. = 1.3/u
sur(t)
HVI. = -0.693/u
P = P 10
P = P e*I
o
SUR = 26.06/T
SCR = S/(1 - K,ff)
CR, = S/(1 - K,ffx)
CR (1 - X,ffj) = G ( -Eeff2)
SUR = 26a/t= + (a - p)T
j
2
T = (t*/o) + ((s - oV Io]
M = 1/(1 - K,ff) = G /G,
'
j
T = 1/(o - s)
M = (1 - K ,ff,)/(1 - K,ffj)
T = (a - o)/(Io)
SDM = ( - K ,ff)/K,ff
a = (K,ff-1) A,ff = K,f/K,ff
t* = 10
seconds
I = 0.1 seconds-I
o = [(t*/(T K,ff)] + [i ff (1 + IT)]
/
Idjj=Id
2 =2 2
P = (I4V)/(3 x 1010)
Id
l
Id
jj
22
2
I = oN
R/hr = (0.5 CE)/d (meters)
R/hr = 6 CE/d2 (f,,g)
Water Parameters
Miscellaneous Conversions
I gal. = 8.345 lbm.
1 curie = 3.7 x 1010dps
1 ga]. = 3.78 liters
} kg = 2.21 lbm
I ftJ = 7.48 gal.
I hp = 2.54 x 10 Stu/hr
Oensity = 62.4 lbm/ft3
1 mw = 3.41 x 10 Stu/hr
,
3
lin = 2.54 cm
Density = 1 gm/cm
Heat of vaccrization = 370 Stu/lem
- F = 9/5'C + 32
. test of fusion = 144 Stu/ltm
'C = 5/9 (*c-32)
1 Atm = 14.7 psi = 29.9 in. Hg.
1 BTU = 778 ft-lbf
I ft. H O = 0.4335 lbf/in.
2
_ _
_ -
..
_-
.
. . - - -
. - - - .
- . - . -
- _
-
.-___ --
_ __, _
_
_
_ _
.._
_
_
.
.
<
.
-
,
i
i
-
l
Table 1.
Saturated Steam: Temperature Table
i
Abs Press.
Specific Volume
Enthalpy
Entropy
Temp
Lb per
Sat.
Sat.
Sat.
Sat.
Sat.
Sal.
Temp
j
fahr
SqIn.
Liquid
Evap
vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
Fahr
,
i
t
p
vi
veg
vg
he
h fe
h
se
sig
s
t
g
g
1
32 0
0 08859
0.016022
33043
33043
0.0179
1075 5
1075 5
0 0000 2.1873 2 1873
32 8
I
34 0
0 09600
0 016021
3061.9
3061.9
1.996
1074.4
1076.4
0 0041
2.1762 2.1802
34 8
l
36 8
0 10395
0 016020
2839.0
2839 0
4.008
1073.2
1077.2
0 0081
2.1651
2.1732
35 0
i
38 0
0.I1249
0.016019
26341
2634.2
6.018
1072.1
10781
0 0122
2.1541 2.1663
3e s
1
'
i
et t
4.12163
0 016019
2445.8
2445.8
8.027
1071.0
1079 0
0 0162
2.1432 2 1594
48.9
i
42 8
0.13143
0 016019
2272.4
2272.4
10 035
1069 8
1079.9
0 0202
2.1325 2.1527
42 0
44 8
0 14192
0 016019
2112 8
2112.8
12.041
1068 7
10803
0 0242 2 1217 2.1459
44 e
4
j
46 I
O15314
0 016020
1%57
1%5.7
14 047
1067.6
1081 6
0 0282
2.1111
2.1393
46 8
40 0
0.16514
0.016021
1830 0
1830 0
16 051
1066 4
1082.5
0 0321
2.1006 21327
48 0
>
.
1
!
50 8
0.17796
0.016023
1704 8
1704 8
18 054
1065 3
1083.4
0.0361
2.0901
2.1262
30.0
52 0
0.19165
0 016024
1589.2
1589 2
20 057
1064 2 .1084 2
0 0400 2 0798 2.1197
52 8
54 0
0 20625
0 016026
1482.4
1482.4
22 058
1063.1
1085 1
0 0439
2 0695 2.1134
54 8
56.8
022183
0 016028
1383 6
1383.6
24 059
1061.9
1086 0
0 0478
2 0593 2.1070
56.8
58.8
0 23843
0.016031
1292.2
1292.2
26.060
1060 8
1086 9
0 0516
2.0491
2.1008
58.0
,
j
50 0
0.25611
0.016033
1207.6
1207.6
28 060
10593
10871
0 0555
2.0391 2.0946
80.0
t
52 0
0.27494
0 016036
1129.2
1129.2
30 059
1058.5
1088.6
0 0593
2.0291
2.0885
52.0
1
64.0
0 29497
0 016039
1056 5
1056.5
32 058
10574
1089.5
0 0632
2.0192 2.0824
54.0
I
56.8
0.31626
0 016043
989.0
989.1
34 056
1056.3
1090.4
0 0670 2 0094 2 0164
66.0
68.0
0.33889
0.016046
926.5
926.5
36 054
1055.2
1091.2
0.0708
1.99 % 2 0704
58.0
l
l
70 0
0.36292
0 016050
868 3
868.4
38 052
10540
1092.1
0 0745
1.9900 2 0645
78 3
'
-
72 3
0.38844
0016054
814 3
814 3
40 049
1052.9
1093 0
0 0783
1.9804 2 0587
72 5
74 0
0 41550
0 016058
764.1
764.1
42.046
1051 8
1093 8
0 0821
1.9708 2 0529
74 3
75 0
0 44420
0 016063
717.4
717.4
44 043
10503
10943
0 0858
1.%I4 2 0412
75 8
78.5
0 47461
0 016067
673 8
673.9
46.040
1049.5
1095.6
0 0895
1.9520 2.0415
isI
!
30.0
0 50683
0.016072
633.3
633.3
48 037
1048 4
1096.4
0 0932
1.9426 2.0559
30 e
i
82 0
0 54093
0.016077
595 5
595.5
50 033
1047.3
1097.3
0 0969
1.9334 2 0303
82 I
34 3
0 57702
0 016082
560 3
560.3
52 029
10461
19982
0 1006
1:9242 2.0248
MI
'
86 0
0 61518
0 016087
227 5
527.5
54 026
1045 0
1099 0
0.1043
1 9151
2 0193
IS O
j
80 0
0 65551
0 016093
4%8
4%8
56 022
1043 9
1099 9
0 1079
1.9060 2.0139
88 8
,
!
te 3
0 69813
0 016099
4681
4681
58 018
10427
1100 8
01115
1.8970 2 0086
98 5
,
92 0
0 74313
0 016105
441.3
441.3
60 014
1041 6
1101 6
01152
1.8881
2 0033
92 e
!
94 0
0 79062
0016111
416.3
416 3
62 010
1040 5
1102 5
0 1188
I.8792 1.9980
34 3
i
!
96 g
084072
0 016117
39? 8
392 9
64 006
1039 3
1103 3
0 1224
1.8704 19928
SE 8
98 0
0 89356
0 016123
3/09
370.9
66 003
10382
11042
01260
1 8617 1 9876
98 8
!
!
l
I
!
'
.
.
,
.
.
.
(
Abs Press.
Specilic Volume
Enthalpy
Entropy
Temp
Lb per
Sal.
Sal.
Sat.
Sal.
Sal.
Sal.
Temp
Fahr
SqIn.
Liquid
Evap
Vapor
liquid
Evap
Vapor
Liquid
Evap
Vapor
Fahr
I
p
vi
vig
vs
he
h ig
h
se
sig
s
t
g
g
les e
0.94924
0 016130
350 4
350 4
67.999
1037.1
1105.1
0.1295
1.8530 1.9825
108.0
182.8
100789
0016137
331.1
331.1
69 995
1035.9
1105 9
0.1331
1.8444 1.9775
102.8
134 g
1 06 % 5
0 016144
313.1
313 1
71.992
1034.8
1106.8
0.1366
1.8358 1.9725
184.0
13s g
1.1347
0 016151
296 16
296 18
73 99
1033 6
1107.6
0.1402
1.8273 1.9675
lese
lese
1.2030
0 016158
280.28
28030
75.98
1032.5
1108.5
0.1437
1.8188
1.% 26
les.g
115.8
12750
0.016165
26537
26539
77.98
1031.4
1109 3
0.1472
1.8105 1.9577
110.0
112s
1.3505
0 016113
251.37
251.38
79.98
1030.2
1110.2
0 1507
1.8021
1.9528
112.0
114 8
1.4299
0 016180
238 21
238 22
81 97
1029I
till 0
0.1542
1.7938 1.9480
1145
113 3
1.5133
0 016188
225 84
225 85
83 97
1027.9
1111.9
0.1577
1.7856 1.9433
11E I
118.8
1.6009
0.016196
214.20
214.21
85 97
1026.8
1112.7
0.1611
1.7774 1.9386
118.8
128 3
1.6927
0 016204
20325
203.26
87.97
1025 6
1113 6
0.1646
13693 1.9339
120.0
1229
1.7891
0 016213
192.94
192.95
89.%
1024.5
1114.4
0.1680
13613 1.9293
122.8
1248
1.8901
0 016221
183 23
183.24
91.%
1023.3
1115.3
0.1715
13533 1.9247
124.I
126 8
1.9959
0 016229
174 08
174.09
93 %
1022 2
1116.1
0.1749
13453 1.9202
125.I
128.I
2.1068
0 016238
16545
165.47
95.96
1021.0
1117.0
0.1783
13374 1.9157
120.0
i
138.8
2 2230
0 016247
157.32
157.33
97.%
1019.8
1117.8
0.1817
1.7295 1.9112
130.0
l
1320
2.3445
0 016256
149.64
149 66
99 95
10187
1118 6
0.1851
13217 1.9068
132.0
134.0
2 4717
0.016265
142.40
142.41
101.95
1017.5
1119 5
0.1884
13140 1.9024
134.s
136.8
2.6047
0.016214
135 55
135.57
103.95
1016 4
1120 3
0.1918
13063 1.8980
138.0
130 0
2.7438
0 016284
129 09
129.11
105.95
1015.2
1121.1
0.1951
1.6986 1.8937
133.g
14e 8
2.8892
0 016293
122.98
123 00
107.95
1014.0
1122.0
0.1985
1.6910 1.8895
140 8
142 8
3 0411
0.016303
117.21
117.22
109.95
1012.9
1122.8
0 2018
1.6534 1.8852
142.I
1448
3.1997
0 016312
11134
111.76
111.95
10113
1123.6
0.2051
1.6759 1.8810
144 s
146.8
3.3653
0 016322
10658
106 59
113 95
10105
1124.5
0.2084
1.6684 1.8769
144.5
148.8
3 5381
0 016332
101 68
101.70
115 95
1009.3
1125.3
0.2117
1.6610 1.8727
140.0
158.3
33184
0 016343
97.05
97.07
117.95
1008 2
1123.1
0 2150
1.6536 1.8686
150.0
152.0
3.9065
0 016353
92.66
92.68
119.95
1007.0
1126.9
0.2183
1.6463 1.8646
152.0
154.3
4.1025
0.016363
88 50
8852
121 95
1005.8
11273
0.2216
1.6390 1.8606
1540
156 8
4.3068
0 016374
84.56
84.57
123 95
1004.6
1128.6
02248
1.6318 1.8566
158.5
1588
4.5197
0016384
80 82
80.83
125.%
1003.4
1129.4
0.2281
1.6245 1.8526
150.0
163 3
43414
0 016395
7727
77.29
12796
1002.2
1130.2
0.2313
1.6174 1.8487
les 8
152 8
4.9722
0 016406
73 90
7392
129.96
1001.0
1131.0
0 2345
1.6103 1.8448
162.0
154 3
5 2124
0.016417
7030
70 72
131.96
999.8
1131.8
02377
1.6032 1.8409
154.8
IEE O
54623
0 016428
6767
67 68
13397
998 6
1132.6
0 2409
1.5%I
1.8371
185.0
IEs e
57223
0.016440
64 78
64.80
13597
997.4
1133.4
0.2441
1.5892 1.8333
168.0
178 g
5 9926
0 016451
62 04
62.06
137.97
996 2
1134 2
0.2473
1.5822 1.8295
170.0
172 I
6 2736
0 016463
5943
59.45
139 98
9950
1135 0
0.2505
15753 1.8258
172.0
174 I
6.5656
0 016474
56 95
56 97
141.98
993.8
1135.8
02537
1.5684 I.8221
174 e
115 g
6 8690
0 016486
54 59
54 61
14399
992.6
II36 6
0 2568
1.5616 1.8184
118.8
118.0
7.1840
0 016498
5235
5236
1%5 99
991.4
1137.4
0 2600
1.5548 1.8147
08.0
-
-.
- -
-.
-
-
-
-
.
-
.
,
.
.
I
h
-
.
.
-
J
!
!
Abs Press
Specific Volume
Enthalpy
Entropy
~
!
Temp
Lb per
Sat.
Sat.
Sat.
Sat.
Sat.
Sat
Temp
!
Fahr
SqIn.
Liquid
Evap
Vapor
liquid
Evap
Vapor
Liquid
Evap
Vapor
Fah
!
t
p
vi
vig
vg
he
h is
hg
se
s gg_
sL
I
f
133.8
7.5110
0.016510
50.21
50 22
148 00
990 2
1138.2
0 2631
1.5480 1.8111
less
!
132.0
7.850
0.016522
48.172
18.189
150 01
9890
1139.0
0.2662
15413
1.8075
182 I
I
IM.0
8.203
0.016534
46 232
46.249
152 01
987.8
1139.8
0.2694
15346
I8040
184 I
l
les e
8.568
0.016547
44.383
44.400
154 02
986.5
1140.5
0.2725
1.5279
1.8004
186 e
,
'
j
Igg e
8.947
0 016559
42.621
42.638
156 03
985 3
1141.3
0 2756
1.5213
13 %9
leg e
I
198 8
9.340
0.016572
40 941
40.957
158 04
984.1
1142.1
02787
1.5148
13934
Its t
192.s
9347
0.016585
39 337
39.354
160.05
982 6
1142.9
02818
1.5082
13900
192.5
l
1940
10.168
0.016598
31.808
37.824
162 05
981.6
11433
02848 1.5017
1.7865
1948
l
196.0
10.605
0.016611
36348
36364
164 06
980.4
1144 4
02879
1.4952
13831
196.I
i
193.s
11.058
0.016624
34.954
34.970
166.08
979.1
1145 2
0.2910 1.4888 13798
19eI
20s.s
11.526
0.016637
33.622
33.639
168 09
977.9
1146 0
0 2940
1.4824 11764
200 8
!
2ee s
12.512
0016664
31.135
31.151
172 11
975.4
1147.5
0 3001
1.4697 1 7698
204.I
i
200.0
13.568
0.016691
28 862
28 878
176.14
972.8
1149 0
0 3061
1.4571
1 7632
208 I
212.0
14.696
0.016719
26 782
26399
180.17
970 3
1150.5
03121
1.4447 11568
212 0
)
218.0
15 901
0.016747
24.878
24.894
184.20
967.8
1152.0
03181
1.4323 13505
215 0
,
220.0
17.186
0.016775
23.131
23.148
188 23
965.2
1153.4
0 3241
1.4201
13442
nos
224.s
18.556
0.016805
21.529
21.545
192.27
962.6
1154.9
0 3300
1.4081
13380
2249
22s 3
20.015
0.016834
20.056
20.073
196 31
960 0
1156 3
0 3359
1.3%1
13320
220 0
232 0
21.567
0.016864
18301
18.718
200.35
957.4
1157.8
03417
13842
13260
2328
236.8
23.216
0.016895
17.454
17.471
204.40
954.8
1159 2
0 3476
1 3725 13201
236 5
248.8
24.968
0.016926
16 304
16321
208 45
952.1
1160.6
0 3533
13609 13I42
240 I
.
244.0
26.826
0.016958
15 243
15.260
212.50
949.5
1162.0
0 3591
13494
1 7085
2448
l
248.8
283 %
0.016990
14.264
14.281
216 56
946.8
1163.4
03649
13379 13028
248 8
!
252.0
30.883
0.017022
13 358
13375
220 62
944.1
11643
03706
13266 1 6912
252 0
256.8
33.091
0.017055
12.520
12.538
224.69
941.4
1166.1
03763
13154
16917
255 0
1
l
200.0
35.427
0.017089
11345
11.762
22836
938 6
1167.4
0.3819
13043
16862
260 t
l
264.s
37.894
0 017123
11.025
11.042
232 83
935.9
11683
0 3816
1.2933
1 6808
264 I
!
258.8
40.500
0.017157
10.358
10 375
236 91
933.1
1170 0
0 3932
1.2823 1 6755
fle s
272.8
43.249
0 017193
9 738
9 755
240 99
930 3
1171 3
0 3987
12715
16702
272.0
'
,
276.8
46.147
0.017228
9.162
9.180
24508
927.5
1172.5
04043
13601
1.6650
276 8
!
200 0
49.200
0 017264
8.627
8.644
249 17
924 6
1173 8
0.4098
12501
16599
200 I
'
284.0
52.414
0 01730
8.1280
8.1453
253 3
921 3
1175 0
0 4154
12395 14548
204 8
'
288 9
55395
0 01734
7 6634
7.6801
2574
918 8
1176 2
0 4208
1.2290 1.6498
218 8
i
292 8
59 350
0 01738
7 2301
7.2475
261 5
915 9
1177.4
0 4263
12186 1 6449
292.0
j
}
296 8
63 084
0 01741
6 8259
6.8433
265 6
913.0
1178.6
0 4317
12082
16400
296 8
!
i
.
.
.
.
.
l
.
Abs Press.
Specific Volume
Enthalpy
Entropy
Temp
Lb per
Sal.
Sal.
Sat.
Sal.
Sal.
Sal.
Temp
Fahr
SqIn.
Liquid
Evap
Vapor
liquid
Evap
Vapor
liquid
Evap
Vapor
Fahr
VI
vig
vg
hg
h ig
he
sg
sig
s
i
g
i
p
30s.g
67 005
001745
6 4483
64658
269 7
9100
1l797
0.4372
11979
I6351
338 I
384.s
71.119
0 01749
6 0955
6.1130
273 8
907.0
1180.9
0 4426
1.1877
1.6303
334 8
30s.I;
75.433
0 01753
5 1655
5 7830
278 0
904.0
1182.0
0 4479
1.1776
16256
388 I
312.3
79 953
0 01157
54566
54742
2821
9010
1183.1
04533
1.1676
16209
312 e
318.8
84 688
0 01761
5 1673
5 1849
286.3
897.9
1184.1
0 4586
11576
I6162
31E e
323.3
89 643
0 01766
48%I
4 9138
290 4
894 8
1185 2
04640
1.1477
1.6116
320 0
324.0
94 826
0 01770
4 6418
4 6595
294 6
891.6
1186 2
04692
1.1378 16071
324 0
328.0
100 245
001774
44030
4 4208
298 7
888 5
1187.2
0.4745
1.1280 16025
323 0
332.0
105 907
0.01779
4.1788
4.1 % 6
302 9
885.3
1188.2
0 4798
11183
1.5981
3328
338 I
111.820
0.01783
3 9681
3 9859
307.1
882.1
11891
04850
1.1086 1.5936
338 8
340.0
117.992
0.01787
3 7699
3 7878
311 3
878.8
11901
04902
10990 15892
348 I
344.s
124 430
0.01792
3 5834
3 6013
315 5
875.5
1191 0
0 4954
1.0894
1.5849
3448
348.0
131.142
0 01797
34078
3 4258
319 7
872 2
1191.1
05006
1.0799 I5806
348 I
352.s
138.138
0 01801
3 2423
32603
323 9
868 9
1192.7
05058
1.0705 1.5763
352.0
358.0
145.424
001806
3 0863
3.1044
3281
865 5
1193 6
0 5110
10611
1.5721
35E e
388.8
153 010
0 01811
2 9392
2 9573
332 3
8621
1194 4
0 5161
10517
1.5678
3se s
364.s
160.903
001816
2.8002
2 8184
336 5
858 6
1195 2
0 5212
10424
15637
3s48
388.3
169.113
0 01821
26691
2.6873
340 8
855I
1195 9
0 5263
I0332
15595
368 5
372.8
177.648
0 01826
2.5451
2 5633
345 0
8516
1196 7
0 5314
1 0240 1 5554
372 s
318 e
186.517
001831
2.4279
24462
349 3
848.1
1197.4
0 5355
10148
15513
376s
300.0
195 729
0 01836
2 3170
2 3353
353 6
844.5
1198.0
0.5416
1.0057
1.54 73
333 3
384 3
205 294
001842
2.2120
2 2304
3579
840 8
1198.7
05466 09%6
1.5432
334.I
338 g
215 220
0 01847
2.1126
2.1311
362 2
8372
1139.3
0 5516 0 9876
15392
333 g
392.s
225 516
0.01853
2.0184
2 0369
366 5
833.4
1199.9
0 5567 0 9786
1.5352
332.8
398.0
236 193
0 01858
1.9291
1.9477
370 8
829.7
1200.4
0.5617 0 9696
15313
3st a
488.8
247.259
0 01064
1.8444
1.8630
375.1
825.9
1201.0
0.5667 09607
1.5274
Ass s
484.3
258 725
0 01870
1.7640
1.7827
379 4
822 0
1201.5
0 5717 09518
1.5234
434 s
400.0
270 600
0 01875
16877
I.7064
383.8
818.2
1201.9
0 5766 0 9429
1.5195
488.8
412 8
282 894
0 01881
1.6152
1 6340
388 1
814.2
1202.4
0.5816 09341
1.5157
412 8
'
418.8
295 617
0 01887
1.5463
1.5651
392.5
810 2
1202.8
05866 0 9253
1.5118
415 e
423 3
308.780
0 01894
1.4808
1.4997
396 9
806 2
1203.1
0 5915 0 9165
1.5080
428 0
424.3
322 391
0 01900
1.4184
1.4374
4013
802 2
1203 5
0 5964
0 9077
I5042
424I
'
'
l
428.9
336 463
0 01906
1.3591
1.3782
405 7
7980
1203.7
0 6014
0 8990 15004
428 s
l
432 e
351 00
0 01913 1.30266
1.32179
410 1
793 9
1204 0
0 6063
0 8903
1.4966
432 9
435 8
366 03
001919 1.24887
1.26806
414 6
789 7
1204 2
0 6112
0 8816 1.4928
43E 8
440 e
381.54
0 01926 119761
1.21687
419 0
785 4
1204 4
0 6161
0 8729
I4890
443 e
444 0
397 56
0 01933 114874
116806
423 5
781 1
1204 6
0 6210 0 8643
14853
444s
44f.a
414 09
0 01940 110212
1.12152
4 29.0
776 7
12041
0 6259
0 8557
14215
4470
44#
43]I4
0 01947 1 05764
1 07711
pt5
772 3
1204 8
0 6308
0 8471
1 47/8
4g.O
456 s
44813
001954 10151R
103472
437 0
767 8
1204 8
06356
0 8385
14741
45 6
i
.
.
.
.
.
.
.
.
Abs Press
Specific Volume
Enthalpy
Entropy
Temp
tb per
Sal.
Sal.
Sal.
Sal.
Sal.
Sal
Temp
Fahr
SqIn.
Liquid
Evap
Vapor
liquid
Evap
Vapor
Liquid
Evap
Vapor
fahr
vr
hg
h ig
h
s,
59,
5,
t
t
p
vi
ver
g
4ES I
466.87
0.01 % I
0.97463
0 99424
441.5
763.2
1204 8
0 6405 0 8299
1.4704
468.0
464 8
485 56
001%9 0 93588
0 95557
446.1
758 6
12043
0 6454
0 8213
1.4667
464.0
468 e
504 83
0 01976 0.89885
0 91862
4503
754 0
1204 6
0 6502 0 8127 1.4629
468.0
472 8
524 67
0 01984 0 86345
0 88329
455 2
749.3
1204 5
0.6551
0 8042
1.4592
472.I
47E g
545.11
0.01992
0 82958
084950
459.9
744.5
1204.3
0.6599 03956 1.4555
475.8
48s O
566 15
0 02000 0 79716
0 81717
464.5
739.6
1204.1
0.6648 03871
14518
esee
484 8
587 81
0 02009
036613
0 78622
4691
7343
1203.8
0 66 % 01785 1.4481
4s4.s
4sg a
610.10
0.02017
033641
035658
473 8
729 7
1203.5
0.6745 0.7700 1.4444
488.0
437 3
633.03
0 02026 030794
032820
4785
724 6
1203.1
0 6793
03614
1.4407
492.8
496 I
656 61
0 02034 0 68065
0 70100
483 2
719 5
12023
0 6842 03528 1.4370
495 e
,
'
!
500 5
680 86
0 02043 0 65448
0 67492
487.9
714.3
1202.2
0 6890 0 7443
1.4333
500.0
504 8
705 78
0 02053 0.62938
064991
492.7
709 0
1201.7
06939
03357
1.42 %
504.8
508 0
731 40
0 02062 0 60530
0 62592
497.5
7033
1201.1
0 6987
03271
1.4258
500.8
I
512 8
757 72
0 02072 0 58218
060289
502 3
698 2
12005
0 7036
03185 1.4221
517 8
SIE e
78436
0 02081
0.55997
0.58079
507.1
6923
Il99L8
0 7085 03099 1.4183
516 8
570 8
812 53
0 02091
0 53864
0 55956
512 0
687.0
1199 0
0.7133
0 7013
1.4146
529.8
5745
84104
0 02102 0 51814
0 53916
516 9
681.3
1198.2
03182
0 6926 1.4108
524.8
578 0
870 31
0 02112 0 49843
051955
521 8
675 5
1197.3
0 7231
0.6839 1.4070
528 3
537 8
900 34
0 02123 0 47947
0 50070
526 8
669 6
11 % 4
03280
0.6752 1.4032
532.0
535 0
931.17
0 02134
0 46123
048257
531 7
663.6
1195 4
0 7329
0.6665 1.3993
536.8
548 8
962 79
0 02146 0 44367
0 46513
5368
657.5
1194.3
0 7378
0 6577 1.3954
See e
544 8
995 22
0 02157 0 42677
0 44834
541 8
651.3
1193 1
0 7427
0 6489 1.3915
5448
5480
1028 49
0 02169 0 41048
0 43217
546 9
645.0
1191.9
03476
0 6400 1.3876
548.0
5578
1062 59
0 02182 039479
0 41660
552 0
638.5
1190 6
0 7525
0 6311
1.3837
5520
555 8
1097.55
0 02194 0 37966
0 40160
5573
632.0
1189.2
03575
0 6222 1.3797
556.8
568 8
1133 38
0 02207 0.36507
0 38714
562.4
625 3
11873
0.7625
0 6132 1.3757
560.8
- 54 0
1170 10
0 02221
0.35099
0 37320
567.6
618.5
11861
0 7674
0 6041
1.3716
564e
568 0
1207 72
0 02235 0 33741
0 35975
572 9
611.5
1184 5
0 7725
05950 1.3675
568 e
577 6
1246 26
0 02249 0 32429
0 34678
578 3
604 5
1182 7
03775
0 5859 13634
5720
515 0
1285 74
0 02264 0 31162
033426
5837
597.2
1180.9
03825
0.5766 1.3592
575.s
a
See 8
1326 17
0 02279 0 29937
0 32216
589I
589.9
1179 0
0 7876
0 5673 1.3550
500.0
584 0
13677
0 02295 0 28753
0 31048
594 6
582 4
1176 9
0 7927
0.5580 1.3507
544.5
5st O
1410 0
0 02311 0 27608
0 29919
600 1
5743
1174 8
07978
0 5485 1.3464
588 3
5970
1453 3
0 02328 0 26499
0 28827
605 7
566 8
1172 6
0 8030
0.5390 1.3420
597I
596 0
1407 8
0 02345 0 25425
0 27770
611 4
558 8
1110 2
0 8082
0 5293 1.3375
59E 8
-
.
.
.
.
.
.
!
Abs Press.
Specific Volume
Enthalpy
Entropy
Temp
tb per
Sal.
Sat.
Sal.
Sal.
Sat.
Sal
ten
Fahr
SqIn.
Liquid
Evap
Vapor
Liquid
Evap
Vapor
liquid
Evap
Vapor
Fa
I
p
vg
vtg
vg
hg
h gg
h
s,
5 ,,
s
I
g
t
i
sees
1543 2
0 02364 0.24384
036747
617.1
550.6
1167.7
0.8134
0.5196 1.3330
000.0
see e
1589 7
0 02382 0.23374
0 25757
622.9
542.2
1165.1
0.8187
0.5097 1.3284
804.0
seg 3
16313
0 02402 0 22394
0 247 %
628 8
533 6
1162.4
0.8240
0.4997 13238
530.0
-
s12 8
16861
0 02422 0.21442
0 23865
634 8
5243
1159 5
0.8294
0.48 % 1.3190
512.0
l
316.5
1735 9
0.02444 0.20516
0.22960
640.8
515.6
1156.4
0.8348
0.4794 1.3141
615.8
t
$28 8
1786.9
0.02466 0.1%I5
022081
646.9
506.3
1153 2
0.8403
0.4689 1.3092
820.0
524 8
1839 0
0 02489 0.18737
021226
653.1
406.6
1149 8
OE'5!
0.4583 1.3041
524.0
$23 8
1892 4
0 02514 0.17880
0 20394
659 5
4863
1146.1
0.8514
0.4474 1.2988
820 0
l
332.s
19470
0 02539 0.17044
0 19583
665.9
476.4
1142.2
0.8571
0.4364 1.2934
532.0
l
636.3
2002 8
0 02566 0.16226
0.18792
672.4
4653
1138.1
0.8628
0.4251
1.2879
636.0
548 8
2059 9
0 02595 0.15427
0 18021
679I
454.6 11333
0.8686
04134 1.2821
sese
544 8
2118 3
0 02625 0.14644
0.17269
685 9
443.1
1129 0
0.8746
0.4015 1.2761
544.8
648 e
21781
0.02657 0.13876
0.16534
692.9
431.1
1124.0
0.880E
03893 1.2699
648.0
552 3
2239 2
0.02691
0.13124
0.15816
700 0
4183
11183
0.8868
03767 1.2634
652 e
$56 I
23013
0.02728 0.12387
0.15115
707.4
4053
1113.1
0.8931
03637 1.2567
456.0
568 I
23653
0.02768 0.11663
0 14431
714 9
392.1
1107.0
0.8995
03502 1.2498
808.8
,
'
564 8
2431.1
0 02811
0.10947
0.13757
722 9
377.7
1100.6
0.9064
03361 1.2425
554.s
568 I
24981
0.02858 0.10229
0.13087
731.5
362.1
1093.5
0.9137
03210 1.2347
ses.g
572 0
256E 6
0.02911 0.09514
0 12424
740 2
3453
1085.9
0.9212
03054 1.2266
572.8
376 8
26368
0.02970 0 08799
0.11769
749.2
328.5
1077.6-
0.9287
0.2892 1.2179
876.0
$80.0
2708 6
0.03037 0.00080
0.11117
758 5
310.1
1068.5
0 9365
02720 1.2086
8e0.0
See B
2782.1
0.03114 0.07349
0.10463
768 2
290.2
1058.4
0.9447
0.2537 1.1984
604.0
588.I
2857.4
0 03204 0.065 %
0.09799
778.8
268 2
1047.0
0.% 35
0.2337 1.1872
les.8
592 8
2934.5
0 03313 0 05797
0 09110
790 5
243.1
1033.6
0.9634
0.2110 1.1744
892.0
896.I
3013.4
0.03455 0.04916
0.08371
804.4
212.8
1017.2
0.9749
0.1841 1.1591
895.8
700 0
30943
0.03662 0.03857
0.07519
822.4
1723
995.2
0.9901
0.1490 1.1390
700.0
782 s
3135.5
0.03824 0 03173
0 06997
835 0
1443
9793
1.0006
0.1246 1.1252
782 0
.
TM s
31772
0 04108 0 02192
0 06300
854 2
102.0
956 2
1.0169
0 0376 1.1046
704.0
~
705 0
31983
0 04427 0.01304
0.05730
873 0
61.4
934.4
1.0329
0 0527 1.0856
785 8
785.47*
32082
0.05078 0 00000
0.05078
906 0
00
906.0
1.0612
0 0000 1.0612
7e5.47*
I
-
-
-
-
-
. - _ _ _ _ _ _ _ _ _ - _ .
--
_
- . . .
..
-_
. _ - - - -
-
.
.
-
..
O
!
.
l
.
Table 2: Saturated Steam: Pressure Table
.
,
}
Specific Volume
Enthalpy
Entropy
Abs Press.
Temp
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Abs Press.
i
Lb/Sq In.
Fahr
liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
LblSq In.
p
t
vg
v
v
hg
hgg
h
sg
s ig
s
p
eg
g
g
g
i
,
l
g.g3065
32.018
0.016022
3302 4
3302.4
0 0003
1075.5
1075 5
0 0000
2 1872
2 1872
e39355
i
0 25
59 323
0 016032
1235 5
1235 5
27.382
1060.1
1087.4
0 0542
2.0425
2.0967
5 25
i
e 5e
79 586
0 016071
64I 5
641.5
47.623
1048 6
1096.3
0 0925
1.9446
2.0370
e 53
l
1e
10134
0016136
333 59
333 60
6913
10361
1105 8
01326
1.8455
I9781
Ie
1
50
162.24
0.016407
73.515
13 532
130 20
1000 9
1131.1
0 2349
1.6094
I8443
5g
l
18 I
193 21
0 016592
38 404
38.420
161.26
9821
1143 3
0 2836
1.5043
17879
le O
'
14 898
212.00
0.016719
26382
26399
18017
970 3
1150.5
0 3121
1.4447
17568
14 596
15.0
213.03
0 016726
26274
26.290
181.21
%97
1150.9
0.3137
1.4415
13552
15 8
2ee
227.96
0016834
20 070
20 087
196.27
9601
1I56.3
0 3358
1.3%2
13320
23 0
30.0
250 34
0.017009
13 7266
133436
218 9
945 2
1164.1
0.3682
1.3313
16995
30 e
i
oga
267.25
0017151
10.4794
10.4965
236.1
933 6
1169 8
0 3921
1.2844
16765
4e e
i
50 g
281 02
0 017274
84%7
8.5140
250 2
923 9
1174.1
0 4112
12474
16586
See
!
Ise
29231
0.017383
7.1562
7.1736
262.2
915 4
1177.6
0 4273
1.2167
1.6440
Is e
I
is e
302.93
0 017482
6.1875
6.2050
2723
907 8
1180 6
0 4411
1.1905
16316
7e e
i
33.8
312 04
0 017573
5.4536
5.4711
282.1
900.9
1183.1
0 4534
1.1675
16208
30 g
33.0
320 28
0 017659
4.8779
4.8953
2903
894.6
1185.3
0.4643
1.1470
1.6113
Se e
lesg
327.82
0 017740
4 4133
4.4310
298.5
888 6
1187.2
04743
1.1284
1.6027
lese
!
!
lig 8
334.79
001782
4 0306
4.0484
305 8
883.1
1188.9
0 4834
1.1115
1.5950
110 e
'
12g a
341.27
0.01789
33097
33275
312.6
877.8
1190.4
0 4919
1.0960
1.5879
120 g
l
130.0
347.33
0.017 %
3.4364
3.4544
319 0
872.8
1191.7
0.4998
1.0815
1.5813
13eI
14g.g
353 04
0.01803
3 2010
3.2190
325 0
8680
1193.0
0 5071
10681
1.5752
les O
'
150.0
358 43
0.01809
2.9958
3.0139
330 6
863.4
1194.1
0 5141
10554
1.% 95
15ee
its e
363 55
0 01815
2.8155
2 8336
336.1
859.0
1l95 1
0 5206
10435
1.5641
Ils e
17e g
368.42
0 01821
2 6556
2.6738
341 2
854 8
II96.0
0 5269
I0322
1.5591
17e s
133.0
373 08
0 01827
2.5129
2.5312
346.2
8503
11 %.9
0 5328
1.0215
I.5543
les e
130.0
377.53
0.01833
2.3847
2.4030
350.9
8463
1197.6
0 5384
1.0113
1.5498
19eI
!
2gg g
381.80
0 01839
2.2689
2.2873
355 5
042.8
1198.3
0.5438
1.0016
I.5454
230 e
l
210.0
385.91
0.01844
2.16373
2.18217
359.9
839.1
1199 0
0 5490
0 9923
1.5413
21g g
i
220.0
389.88
001850
2 06779
2.08629
364 2
835 4
1I99.6
0 5540
0 9834
1.5374
225 0
'
233 0
39330
0 01855
I97991
1.99846
368 3
831 8
12001
0 5588
0 9748
15336
238 g
l
240 e
397.39
0 01860
1.89909
I91769
372 3
828 4
1200 6
05634
0 9665
I5299
248 8
a
250.0
400 97
001865
1.82452
1.84317
376.1
825 0
1201.1
0 5679
0 9585
1.5264
250 0
!
260 0
404.44
C01870
1 75548
137418
379.9
821 6
1201.5
0 5722
0 9508
1.5230
260 0
l
270.g
407.80
0 01875
I69137
131013
383 6
818.3
1201.9
05764
0 9433
15197
275 0
4
238 I
411.07
0 01880
163169
1.65049
387.1
815.1
1202.3
05805
0.9361
15166
280 e
'
298.9
414.25
0 01885
1 57597
1.59482
390 6
812.0
1202.6
0.5844
0 9291
1.5135
290 0
333 e
417.35
0 01889
I 52384
1.54274
394 0
808 9
1202.9
05882
0 9223
I5105
300 e
350 0
43173
0 01912
130642
1.32554
409 8
794 2
1204 0
0 6059
0 8909
I4%8
358 8
488 0
444 60
0 01934
1.14162
1.16095
424 2
780 4
1204 6
0 6217
0 8630
14847
400 0
,
i
t
.
- - .
.
-
_ - -
. - .
. -
_ . - - - - - - . -
!
-
i
!
%
!
Specific Volume
Enthalpy
Entropy
,
o
l
Abs Press.
Temp
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Abs Press.
i
Lb/Sg in.
Fahr
liquid
Evap
Vapor
Liquid
Evap
Vapor
Liquid
Evap
Vapor
tblSq In. .
i
g
p
l
p
t
vi
vig
v
h l
h
h
g
ig
g
sg
s ,g
s
.
'
458.8
456 28
0 01954
101224
1.03179
437 3
767.5
1204.8
06360
0.8378
14738
458 8
580.0
46701
001975
0 90787
0.92762
449 5
755.1
12043
06490
0 8148
1.4639
500 0
l
t
550 0
476 94
0 01994
0 82183
0 84177
460.9
743.3
1204.3
0 6611
03936
1.4547
550 0
l
ses8
486 20
0 02013
074%2
0 76975
4713
732 0
12033
0 6723
03738
14461
See 0
,
j
650 8
494 89
0 02032
0 68811
0.70843
481.9
720.9
1202.8
06828
07552
14381
658 I
i
700.0
503 08
0 02050
0 63505
0.65556
491.6
710.2
1201.8
0 6928
03377
1.4304
fee t
750 0
510 84
0 02069
0 58880
0 60949
500 9
699 8
1200 7
0 7022
0 7210
14232
758 8
j
BIO O
518 21
0 02087
054809
0.568 %
509 8
689 6
1199.4
03111
0 7051
I4163
000 0
850.0
525 24
0.02105
0 51197
0 53302
518 4
679.5
1198 0
03197
0 6899
1.4096
350 0
'
900 8
531.95
0 02123
0 47968
0 50091
5267
669 7
1196 4
0 7279
06753
14032
93g e
958 8
538.39
0 02141
0 45064
0.47205
534 7
660 0
1194 7
0 7358
0 6612
1.3970
95s g
1000 0
544.58
0 02159
0 42436
0.44596
542 6
650.4
1192 9
0 7434
0 6476
1.3910
lege s
1950 0
550.53
0.02177
0.40047
0 42224
550.1
640.9
1191.0
01507
06344
1.3851
lessI
'
l
110s 8
556 28
0 02195
0 37863
0 40058
557.5
631.5
1189.1
03578
06216
13794
Ilse e
i
1150.8
561.82
0 02214
0.35859
0.38073
564 8
622 2
1187.0
03647
06091
13738
115eI
1200.0
567.19
0 02232
0.34013
0.36245
571.9
613 0
1184.8
0.7714
05%9
1.3683
12000
'
j
1250 9
572.38
0 02250
0 32306
0.34556
578 8
603 8
1182.6
01780
0 5850
1.3630
1258 8
j
1388 I
577.42
0.02269
0 30722
0 32991
585 6
594 6
1180 2
0 7843
0 5133
1.3577
13ss e
13500
582.32
0 02288
0.29250
0 31537
592.3
585 4
1177.8
03906
0.5620
1.3525
135e e
i
lose e
587.07
0 02307
0 27871
0.30178
598 8
576 5
1175.3
03966
0 5507
1.3474
lega 5
1458 8
591.70
0.02327
0 26584
0 28911
605 3
567 4
1172.8
0 8026
0 5397
1 3423
1450 0
150s 0
596 20
0 02346
0 25372
0 27719
611 3
558 4
1170.1
0 8085
0 5288
1.3373
15eg g
15580
600 59
0 02366
0 24235
0 26601
618 0
549 4
1167.4
0.8142
0.5182
1.3324
155II
ISOS S
604.87
0 02387
0 23159
0 25545
624.2
540.3
1164.5
0.8199
05076
1.3274
163g g
l
1658 8
609 05
0 02407
0 22143
0.24551
630.4
531.3
1161 6
08254
0 4971
1.3225
1650 0
1
1700 0
613.13
0.02428
021178
0.23607
636.5
522.2
1158 6
0.8309
0.4867
I.3176
Ilse g
l
1750.8
617.12
0.02450
0 20263
0.22713
642.5
513.1
1155.6
0 8363
0.4765
1.3128
17500
4
Igge 3
621 02
0 02472
0 19390
011861
648 5
503 8
1152.3
0 8417
0.4662
1.3079
Iges e
i
185g e
624.83
0 02495
018555
0.21052
654 5
494 6
1149 0
0.8470
0 4561
1.3030
is5e e
i
1900e
628.56
0 02517
0.17761
0.20278
660 4
485 2
1145 6
0 8522
0 4459
1.2981
19ee e
'
19500
632.22
0 02541
0.16999
0.19540
666 3
475.8
1142.0
0.8574
0.4358
13931
19500
!
2000.0
635 80
0.02565
0 16266
0 18831
612.1
4663
1138.3
0.8625
0 4256
12881
2000 5
1
2100.3
64236
0.02615
0.14885
0 17501
683.8
4463
14 30.5
0 8727
04053
1.2780
21ee e
.
2200.3
649.45
0 02669
0.13603
0.16272
695 5
4263
1122.2
0.8828
0.3848
1.2676
2200.8
l
2300.0
655.89
0.02727
0.12406
015133
707.2
406 0
1113.2
0.8929
0.3640
12569
2388 5
!
2400.0
662.11
0.02790
0.11287
0.14076
719 0
384.8
1103.7
0.9031
0.3430
1.2460
2480 8
l
i
2500 e
668.11
0.02859
0 10209
0.13068
731 7
361 6
1093 3
0 9139
0 3206
1.2345
7500 e
l
260s e
673 91
0 02938
0.09172
0.12110
744 5
337 6
1082.0
0 9247
0 2917
12225
2500 0
2700 0
679 53
0 03029
0 08165
0.11194
757 3
312 3
1069 7
0 93 %
02741
12097
2100 0
2000 e
684 96
0 03134
0 07171
0.10305
770 7
2851
1055 8
0 9468
02431
1.1958
20050
2900 8
690 22
0.03262
0 06158
0 09420
7851
2543
1039 8
0 9588
02215
1.1803
2988 8
30000
695 33
0 03428
0 05073.
0 08500
801 8
218 4
1020 3
0 9728
01891
1.1619
3seg g
31st8
700 28
0 03681
0 03771
0 07452
824 0
169.3
993 3
0 9914
0 1460
1.1373
3100 I
i
370sI
705 08
0 04472
0 01191
0 05663
875 5
56 1
931.6
1.0351
0 0482
1.0832
320s e
3200.2*
70547
0 05078
0 00000
0 05078
9E4
00
906 0
1 0612
0 0000
1 0612
1788 7-
- Critical pressure
!
-
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE 19
fHERM0 DYNAMICS,HEATTRANSFERANDFLUIDFLOW
B.
ANSWERS -- BRAIOWOOD 132
-86/10/22-WEALE, G./REIDINGER
MASTEri COPY
'
ANSWER
1.01
(2.00)
a. Increase (0.25) - increase in shutdown margin due to higher rod position
while available power defect reactivity remains constant (0.75)
(1.00)
b. No change (0.25) - decrease in shutdown margin due to more available
power defect matched by increase in shutdown margin due higher rod pos-
ition.(0.75)
(1.00)
REFERENCE
REACTOR THEORY REVIEW I-5.31/38, BW TECH SPECS I-5
ANSWER
1.02
(3.00)
a. (ACP) HIGHER)THAN $CP)(0.25)- Because Xenon will have built up (to nea
-c
peak value adding negative reactivity (0.5)
b. lACP) LOWE,R THAN (ECP)(0.25)- Because Xenon will have decayed off(to a low -%ddaf
value) adding positive reactivity (0.5)
(0.75)
c. I6CP) HIGHER THAN (ECP)(0.25)- Because with steam dumps maintaining higher
steam generator pressure / temperature, RCS temperature increases (due
decay heat and input from RCS pumps-optional) to add negative
reactivity (0.5)
(0.75)
d. lACP) LOWER THAN @C4(0.25)- Decause RCS temperature decreases (due to heat
removal in SGs-optional) and adds positive reactivity (0.5)
(0.75)
REFERENCE
REACTOR THEORY REVIEW FIG I-5.13/52
_
__
- _ _
_ - . _ _ _ - _ _ _ _ _ _ _ . _ _ _ ,
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE 20
THERMODYNAMICS, HEAT TRANSFER AND FLUID FLOW
,
,
.>
s
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE, G./REIDINGER
,
ANSWER
1.03
f2.00)
a. For equilibrium, llenon removal by decay must increase as power
-
increases (0.5). Xe.aon removal by decay is proptfitional to Xenon
concentration (0,5). (Therefore, Xenon concentration increases as
power increases - oottonal.)
(1.0)
b. Samarium does not decay (0.5). Samarium production and burnup rates
are proportional to power (0.5). (Therefore, Samarium concentration
is constant at power - optional.)
(1.0)
REFERENCE
REACTOR THEORY REVIEW I-5.68/77/78
huk62 b (1.50)
of
1.04
ANSWER
(a)(Current (2) = j nfak
r
Current (1 X (N2/N1)**3_= 20 X (4)**3 = 1280 amps (0.50)
9
(b)
low (2) = Flow (1) X (N2/N1) = 50 X 4 = 200 gpm
(0.50)
-
,
(c) Delta-P(2) = Delta-P(1) X (N2/N1)**2)= 8 X (4)**2 = 128 psid
(0.50)
REFERENCE
THERMAL HYDRAULIC PRIN 10-36
,
, - . , , -
. - , . - , , , _ ,
.- - . . - - , .
. . , - . - -
- - - - . , . - , . _ . ,
, . - . - - . . ,
, . . - , - . - - . - , - .
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE 21
THERMDDYNAMICS, HEAT TRANSFER AND FLUID FLOW
,
,,
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE, G./RE!DINGER
.
ANSWER
1.05
(2.75)
'
a. 1) d)
2) a)
3) e)
(0.25 each)
k. wbhdeact)rcoolanh(mass)flowrate
(0.25)
.
b. 1) m
2) Cp
specific heat capacity of reactor coolant
(0.25)
3) At reactor coolant delta-T or (Thot-Tcold)
(0.25)
4) U
overall heat transfer coefficient for SG
(0.25)
5) A
total area of SG tubes
(0.25)
6) AH feedwater/ steam enthalpy change or (Hstm-Hfeed)
(0.25)
7)hf
feed flow rate or steam flow rate
(0.25)
8) AT delta-T across tubewalls or (Tavg-Tstm) or (Tavg-Tsat) (0.25)
REFERENCE
THERMAL-HYDRAULIC PRIN 12-12/13/14
-
QM A / ( .75)
ANSWER
1.06
..
a. (1){educi'1g pump flow reduces the minimum / required NPSH
(0.25)
(2)hedue
tem flow' increases the available NPSH
(0.25)
J
wd!4.
b. Restores the source of require NPSH
(0.25)
REFERENCE
THERMAL-HYDRAULIC PRIN FIG FND-FF-85, 10-60/61
I
i
)
_ . , - _ - -
-
_ - . . _ - . - , . - , _ _ . - - . _ _ . _ , .
-
_ . , . _ . . _ -
_ . _ . . _ , -
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE 22
THERMODYNAMICS, HEAT TRANSFER AND FLUID FLOW
.
,,
..
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE,G./REIDINGER
'
\\
ANSWER
-1.07
(3.00)
a. Rhol = -2.5% delta-k/k
Keffl = 1/(1-rho) = 1/(1-( .025)) = .9756 t,0o2.
(0.75)
CR1/CR2 = (1-Keff2)/(1-Keff1)
135/405 = 1/3 = (1-Keff2)/(1.9756)
Keff2 = .992 t .002-
(0.75)
Rho 2 = 1-1/Keff2 = -0.81% delta-k/k
Reactivity added = -0.81% - (2.5%) = 1.69% delta-k/k i.,1*/o
(0.75)
b. Near 400 cps (0.25), because as Keff approaches 1, more neutron
generations are required to stabilize the neutron level (0.25).
(0.75)
1(I I I Iti NCl.
RLACIOR THLORY REVIEW 1-4.27/28
ANSWER
1.08
(2.00)
~
1) When the steam flow out of each SG decreases
SG temperature increases
,
Qo match RCS temperature](0.5), causing SG pressure to increase (0.5),
compressing / collapsing the steam bubbles in the riser (0.5). As a
result the SG levels drop or " shrink".(0.5)
(2.0)
OR (accept either answer)
(2) The loss of steam flow and recirculation flow through the SG moisture
separators removes the recirculation flow delta-P(0.5), removing the
need for recirculation flow driving head (0.5), allowing the downcomer
level to drop (0.5),and equalize with the lower level in the
riser. (0.5)
(2.0)
REFERENCE
THERMAL-HYDRAULIC PRIN 12-53
i
-
-
. -
-._.
.
_.
.
__ _ __ -
--
1.
PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,
PAGE 23
,. ,'
- JHERMDDYNAMICS, HEAT TRANSFER AND FLUID FLOW
86/10/22-WEALE, G./REIDINGER
ANSWERS -- BRAIDWOOD 182
-
.
ANSWER
1.09
(3.00)
a. The fuel temperature coefficient (Doppler-only power coefficient)
overrides the small NTC(0.50), making the total power coefficient large
negative (0.50), requiring large positive reactivity (dilution) to
increase power.(0.50)
(1.50)
b. The large negative change in MTC over core life (0.50) makes the total
power coefficient much more negative at EOL than at BOL(0.5), requiring
a much larger positive reactivity addition (more dilution) to increase
power (0.50)
(1.50)
REFERENCE
REACTOR THEORY REVIEW FIG I-5.9/13/20/22/23
ANSWER
1.10
(2.00)
a. LESS THAN (0.25) - Differential Boron worth is greater because Boron
concentration is less, so less ppm required. (0.75)
(1.00)
,
b. LESS THAN (0.25) - Differential Boron worth is greater because Tavg is
less, so less ppm required. (0.75)
(1.00)
REFERENCE
REACTOR THEORY REVIEW FIG I-5.24/25/27
ANSWER
1.11
(3.00)
a.
Less negative (0.25) because Xe inserts negative reactivity in the
bottom of the core and flux moves to the top of the core (0.75).
b.
More negative (0.25) because .~ods are inserted and push the flux to the
bottom of the core (0.75)
c.
More negative (0.25) because more moderation will occur in the bottom
of the core due to sudden influx of colder Tcold (0.75)
'
REFERENCE
REACTOR THEORY REVIEW FIG I-5.34/35/36
%
-,,
- --+~,
a
- - - - - - , - . - ,
n-e,--n--.-
-
-- -
a
-
- , - - - - - - - - , - - , , - - - - - - - - . , , - - , - - , , - , - - - - - - - - - - - , , , , ,
2.
PLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS
PAGE 24
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE, G./RE!DINGER
.
ANSWER
2.01
(1.00)
1) To maintain adequate flow to the 3 remaining SGs if one SG/AFW line is
ruptured OR keeps all AFW flow from going to ruptured SG/AFW line break.
(0.5)
2) Used for AFW flow detectors [p2 $gsh
(0.5)
,
,
REFERENCE
BW SYST TRNG MAN 26-23
ANSWER
2.02
(2.00)
a. Start /stop switch for other CCW purp on same 4.16KV ESF electrical bus
must be in " pull-to-lock" position.
(0.5)
b. Low CCW discharge header pressure
(0,5)
Safety injection signal
(0.5)
Power return after station blackout
(0.5)
REFERENCE
BW SYST TRNG MAN 19-12
ANSWER
2.03
(2.00)
(1) Interceptor control valves / reheat stop valves (0.5 for either)
in hot reheat steam lines to LP turbines (0.5)
(1.0)
(2) Non-return check valves / extraction steam isolation valves (0.5 for
either) in extraction steam lines to feedwater heaters (0.5)
(1.0)
REFERENCE
PW SYST TRNG MAN 35-16,36-16
!
.
_ _ - - _ - .
_ - _ . _ .
_ _ . . __
-
. . .
- -
. - - . _ - _
- . .
- -
. - - - - - - -
-
2.
PLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS
PAGE 25
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE,G./REIDINGER
-
,
ANSWER
2.04
(2.00)
a.1) CVCS letdown entmt isol valves (CV-8160,8152)
(0.25)
2) CVCS letdown orifice isol valves (CV-8149A,B,C)
(0,25)
3) RCP seal water return entmt isol valves (CV-8100,8112)
(0.25)
4) Cntmt isol valves for CCW to excess letdown HX(CC-9437A,B)
(0.25)
b. No(0.25); without letdown, pressurizer level will increase (0.25) due to
RCP seal flow into RCS(0.25) until plant must be tripped due to high
przr level (0.25)
(1.0)
REFERENCE
BW SYST TRNG MAN 15A-15/16/38/41, TECH SPECS 3/4 6-18
ANSWER
2.05
(3.00)
1) BAST, boric acid xfer pump /CV-8 4
gn
50-60gpm
2) BAST, boric acid xfer pump and RMCS manual or borate (mod
0-40gpm
3) RWST, thru CV-1120/E to centrif chg pump suction; 105gpm
4) BAST, boric acid xfer pump thru CV-8439(throgalg) to charg pump
suction; less than 10gpm
(0.4 for each path, 0.2 per source, and 0.15 per rate)
(3.0)
(10gpm tolerance on flow rates)
REFERENCE
BW SYST TRNG MAN 158-27
ANSWER
2.06
(1.50)
.j u e
04.SEdnSalien
1) Centrif Charg Pump injection
2235 psig3((0.25)(10% tolerance on
2) Safety Inject Pump injection
1500 psig 0.25)
all pressures)
3) Accumulator injection
640 psig (0.25)
4) RHR Pump injection
200 psig (0.25)
(0.5 for order)
i
REFERENCE
'
BW SYST TRNG MAN Fig 61-16,58-63
.
.
.
_
___
_ _ _ _ _ . _ - _ . . -
- - . . _ - _ -
-
'
-
~2.
PLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS
PAGE 26
~
ANSWERS -- BRAIDWOOD 182
-'
86/10/22-WEALE,G./RE!DINGER
-
-
.
ANSWER
2.07
(2.00)
1) Power to Bus 111 can be supplied from Unit 2 Bus 211(0.5) by closing
the 111/211 bus tie breakers (0.5)
(Optional - Check both bus grounds < 70vdc
Check bus voltages within 20vde
Close bus tie breakers 111 and 112
)
Isolate affected battery and battery charger)
2) Power to the 1A DG cont panel can be restored by shifting the removable
fuse block /no-blow link (0.5 for either) and closing the reserve feeder
,
breaker (0.5)
'
(Optional - Verify control power from reserve feeder
Open main and reserve supply breakers
Shift removable fuse block /no-blow link from main supply
receptacle to reserve supply receptacle
Close reserve supply breaker )
REFERENCE
BW SYST TRNG MAN 8A-13,21
ANSWER
2.08
(1.50)
a. After the turbine has tripped (0.25), turbine windmilling without steam
cooling (0.25)could cause overheating of the turbine blading(0.25).
(0.75)
b.1) To keep RCPs energized longer to maintain RCS flod if the turbine
trip was caused by a reactor trip.
(0.25)
2) To prevent RCP overspeed/ damage during steamflash on major LOCA(0.25)
3) To prevent overspeeding the turbine if some steam still present after
(0.25)
REFERENCE
BW SYST TRNG MAN 5-29, 5-40
J
<
!
i
l
i
.-
- - - - , _ -
,,,,m_,_,._,_.-.,mm
~,.,__-..._,-._,,-.-_____,_.,__._._..__._.__,,__,.______=_-_,...-.,--_.,.__..m
. -
- - -
-
I
2.
PLANT DESIGN INCLUDING SAFETY AND EERGENCY SYSTEMS
PAGE 27
ANS14ERS -- BRAIDWOOD 182
-86/10/22-WEALE, G./REIDINGER
'
.
ANSWER
2.09
(1.75)
a. Provides sufficient leakoff flow to cool lower pump radial bearing (0.5)
at low RCS pressures (0.25).
(0.75)
b. Upper-1000psig(0.25);1eakoff flow should be sufficient above 1000psig;
if not, something wrong (0.25)
(0.5)
Lower-100psig(0.25);to prevent backflow of potentially dirty water
from VCT/CVCS system OR contaminants from the seal water return
filter,(0.25 for ett er)&gnUtadu </00&
(0.5)
DC MdA kn
REFERENCE
BW SYST TRNG MAN 13-37
ANSWER
2.10
(1.00)
a. Increasing CCW surge tank level
Increasing rad reading on CCW HX outlet Process Rad Monitor (PR009)
Surge tank vent closure on PR009 ALERT
(any 2, 0.25 each)
b. CVCS inlet valve to nonoperating HX is normally shut and check valve on
outlet should prevent pressure in tubes from exceeding shell side
pressure.
(0.25)
(Optional-the non-operating HX is normally isolated at power OR the CVCS
supply valve to the HX is shut and assume no leakage o
valve)
c. Shif t HXs (also acceptable-increase on local thermometer reading on CCW
outlet of operating HX)
(0.25)
REFERENCE
BW SIM MALF CCW-1; SYST DIAG M-64 SH 5
ANSWER
2.11
(1.50)
1) No locko(uts on/d)
ai. *o DG feeder brkr(1413) or SAT feeder brkr(1412)
(0.25)
3
2) DG at rated frequency and voltage
(0.25)
3) ESF cross-tie breaker from Unit 2 (ACB 1414) open
(0.25)
4) SAT feeder breaker (ACB 1412) open
(0.25)
5) ESF-to-non-ESF bas cross-tie breaker (ACB 1411) open
(0.25)
6) Control switch for DG feeder brkr ACB 1413 in After Trip
(0.25)
--.
. - -
, - ___
. - - - -
.
._.
__
.-
-
. , .
- . -
- _ - _ -
2.
PLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS
PAGE 28
'
dNSWERS--BRAIDWOOD182
-86/10/22-WEALE, G./REIDINGER
'
,
'
REFERENCC
BW SYST TRNG MAN 4-101
ANSWER
2.12
(2.50)
a.1) Cooling pump suction lines are located 4 feet below normal level (0.5)
2) The downward range of the skimers is limited to about 4 inches
below normal level (0.5)
3) Cooling pump discharge line's terminate about 6 feet above fuel
assemblies (0.5)
4) Cooling pump discharge lines have anti-siphon holes (0.5)
b. An inadverfnt criticality cannot occur (0.25) because the design of the
storage racks provides sufficient center-to-center spaging to prevent
inadvertent criticality @ven with no
gnthewatej(0.25)
REFERENCE
BW SYST TRNG MAN 51-13, 51-25
ANSWER
2.13
(1.25)
b
"#
~ b Mb
h#"kk
77;?p[uhr %@ d543 ry h
1) WTA voltage regulator trips
2) Base adjuster goes to no-load position
T41 unr
4 e -ESF 4/4o 6m
3) Main transformer cooling equipment trips
4) Auto 24-hour ground detector trips
n'
oca4 I-r,7-f
5) Bus duct cooling equipment trips
ggQgeg
g
%TO
RFFERENCE
BW SYST TRNG MAN 6-31/40
ANSWER
2.14
(2.00)
a. From RWST(0.25), to all RCS cold legs (0.25)
b. From containment sump (0.25), to suctions of SI and centrifugal charging
pumps (0.25)
c. From containment sump (0.25), to all RCS cold legs (0.25)
d. From containment sump (0.25), to RCS hot legs A and C(0.25)
-
.
2.
PLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS
PAGE 29
.
-
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE,G./REIDINGER
.
,
-
REFERENCE
8W SYST TRNG MAN 58-51,52,53
.
l
!
-
-
- -
-
.
- . -
- -
- . - -
. .
,
3.
INSTRUMENTS AND CONTROLS
PAGE 30
.* ANSWERS.-- BRAIDWOOD 182
-86/10/22-WEALE, G./REIDINGER
'
1
-
ANSWER
3.01
( .50)
--b--
REFERENCE
BW SYST TRNG MAN 28-64,65,66;29-19
ANSWER
3.02
(1.00)
1) With 2 prs deenergized simultaneously, the P-10 signal will be actuated
to deenergize both Source Ranges (0.5).
2) Per Tech Specs both SRs must be operating for fuel load operations.(0.5)
REFERENCE
BW SYST TRNG MAN FIG 33-11, TECH SPEC 3/4.9.2
ANSWER
3.03
(2.50)
a. One charcoal booster fan starts and the filter bypass damper shuts (0.5)
b. Unit 1 and 2 CCW surge tank vent valves shut (0,5)
'
c. Outside air intake A dampers close, fan starts, and air intake A dampers
from turbine building open(0.5)
d. Steam Gen blowdown sample valves (1PS-179A-D - optional) close(0.5)
o. Energizes off-gas vent filter system (0,5)
REFERENCE
BW SYST TRNG MAN 49-64-68
.
-.y
-
. , , - . .
. - - - - , - . . - ,,
-_
,s,,
,.r-
-
w,--- - , - _. , . - .. . , .,y-.-.
-
,,,m-
-.
._,,, ,-
-m_.
e
y
.
3.
INSTRUMENTS AND CONTROLS
PAGE 31
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE, G./REIDINGER
.
ANSWER
3.04
(1.50)
a.1) top 3 sensors of RVLIS channels A and B
2)10 hottest core exit thermocouples
3) average pressurizer pressure (NR)
4) average RCS loop pressure (WR)
(0.25 each)
(1.0)
b. 1)490 psig
2)35 F
(20f, tolerance, 0.25 each)
(0.5)
REFERENCE
BW SYST TRNG MAN 348-35
ANSWER
3.05
(1.50)
a. L of L is armed by C9 and C7(0.25); TT is armed by C9 and C8(0.25)
b. L of L conpares Tavg to Tref (0.25); TT compares Tavg to Tno-load (0.25)
c. L of L has 4F deadband(0.25); TT has no deadband(0.25)
REFERENCE
BW SYST TRNG MAN 24-31
ANSWER
3.06
(2.25)
a. Indicated steam flow will be higher than actual flow (0.25) because
steam pressure compensation is using too high pressure multiplier.(0.5)
b. Erroneous high steam flow will try to bring feed flow up(0.25), but
level-dominant SGWLC system will reduce feed flow as necessary to main-
tain constant programmed level (0,5)
c. Erroneous high steam flow will cause programmed feed pump delta-P to
go higb(0.25) causing feed pump to speed up to suply more delta-P than
normal at 1007, power (0.5)
(Give full credit on b and c if effect traced correctly even though
initial effect on steam flow reasoned incorrectly.)
REFERENCE
BW SYST TRNG MAN FIG 27-4,27-8
_ _ - _ _ _ - .-
.
._ _
_
3.
INSTRUMENTS AND CONTROLS
PAGE 32
.* A'NSWERS -- BRAIDWOOD 182
-86/10/22-WEALE,G./REIDINGER
'
-
1
ANSWER
3.07
(2.25)
l
a.
1) The steam dumps open(.25)
J
2) Cooling Tavg to about 550F(0.25)
3) The P-12 interlock will control RCS temperature by cycling the steam
dump valves around 550 F (0.25)
b.
1) All steam dump valves will shut (0.25)
2) Steam pressure will rise to the setpoint of the main steam
atmospheric relie* valves (0.25)
3) MS atmospheric reiief valves will cycle to maintain steam pressure
and RCS temperature.(0.25)
c.
1) Normal shift to t'
Turbine Trip controller will not occur (0.25)
'
2) Plant will cooldow because load Rejection controller will open
steam dumps (0.25)
3) The Load Rejection c troller will maintain RCS temperature near
'
"No Load" Tref (+4F d fation/deadband)[0.25]
O%d
contwlQ h TuQ(fLJ74)cos, ties (.es)
2M M
Mm M So-MW 62O
W SYS
RNG MAN FIG 24-7,9
3) %
& tLs V 4 m u n m e. food Tav' 6 rs)
ANSWER
3.08
( .75)
a.
TRUE
b.
FALSE
c.
FALSE
[0.25 each]
REFERENCE
BW SYST TRNG MAN FIG 608-10
ANSWER
3.09
(1.25)
'
a.
4
(0.25)
b.
2
(0.25)
c.
6
(0.25)
d.
5
(0.25)
o. ' S
(0.25),
,
'
REFERENCE
'
BW SYST TRNG MAN 658-35
.
$
. . -
- . _ _ _ . _
. . - -
. -
.
3.
INSTRUMENTS AND CONTROLS
PAGE 33
. . -.- ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE,G./REIDINGER
.
.
ANSWER
3.10
(1.00)
1) Turns all heaters off at 17% level (0.25) to prevent heater burnout (.25)
2.
Turns on backup heaters if actual level varies above program by 5%(.25)
in anticipation of an outsurge after an insurge of relatively cold
water [0.25].
REFERENCE
BW SYST TRNG MAN FIG 14-2
ANSWER
3.11
(1.50)
a.
IN(0.25), because Tavg is higher than Tref (0.25)
b.
OUT(0.25), because Tref becomes more than Tavg(0.25)
c.
IN(0.25), because the power mismatch circuit sees turbine power
decreasing below Rx power (also, Tref decreasing below Tavg)(0.25)
'
REFERENCE
j
BW SYST TRNG MAN FIG 28-14
!
ANSWER
3.12
(1.00)
Because the change in 1 power is greater at higher power levels for a given
change in reactivity (0,5), it reduces signal multiplier at high power (0.5)
(optional - prevents overshoot (0.5) which is more likely to occur at high
power levels (0,5))
REFERENCE
BW SYST TRNG MAN 28-27
,
ANSWER
3.13
(1.00)
,
1) Low feed flow ( < 1700gpm - optional)
(0.25)
f
2) Feed reg valve or bypass (1FW510,1FW510A) not closed, with(0.25):
Either SG low press or low level or low feed flow (0.25)
3) Any fee &ater isolation signal
(0.25)
i
M3 AM"
SC Hi-lh Lud % a 4 scs
Le M (%+) W P-4 sl4
'
,
..-.,,..,.m,.
- .. _--.-,- ,
., .,.-.- ,..,- ,, ,,.+,,- ,. ---,_.
_,._,v
_.....,-,.,,__,.,_.m.,-,n.n._.,,_...,,.n_
a..
,.. _ . ,,-,
-
3.
INSTRUMENTS AND CONTROLS
PAGE 34
'.
' ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE, G./REIDINGER
l
.
REFERENCE
BW SYST TRNG MAN 25-68
l
ANSWER
3.14
(2.00)
a.
Power range high flux - 103%
[0.3]
Intermediate range overpower - current equiv. to 20%
[0.3]
OP Delta-T - 3% below setpoint
[0.3]
,
OT Delta-T - 3% below setpoint
[0.3]
Urgent Failure Alarm (no setpoint required)
[0.2]
b.
Turbine power < 15%
[0.3]
Control bank D withdrawal stop - 223 steps
[0.3]
REFERENCE
BW SYST TRNG MAN 28-70,71
i
ANSWER
3.15
(1.00)
1.
OT Delta-T calculator
(0.25)
2.
OP Delta-T calculator
(0.25)
3.
P-12 circuitry (Hi Stm. Flow SI permissive,gStm. dump block)
(0.25)
4.
Feedwater isolation circuitry
(0.25)
REFERENCE
BW SYST TRNG MAN FIG 12-14
ANSWER
3.16
(1.50)
1) Safety Injection Signal (3.25)
2) Undervoltage on RCP busses (0.25)
(2/4)
(0.25)
3) One SG low-low level (0.25)
2/4 channels (0.25)
4) Undervoltage on bus 141 (0.25)
REFERENCE
BW SYST 1RNG MAN 26-42
- _ _ _ _ _ _ _ _ _ _
_
_
_
__
3.
INSTRUMENTS AND CONTROLS
PAGE 35
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE, G./REI0INGER
.
,
9
ANSWER
3.17
(1.75)
a. Spray valves open fully
(0.25)
PORV-455A is opened
(0.25)
All pressurizer heaters interlocked off
(0.25)
bo Resuau
KV-45cA od 41ay yk
F. Backup pr% du.4s eius h(IPT-458I'will shut'PORV-455A
essure transditter
Pressure will continue to drop due to open sprays
Reactor will trip on pressurizer low pressure
Safety injection will initiate on pressurizer low pressure
Injection flow will fill pressurizer and stop spray effect
Pressure will cycle about PORV-455A backup pressure setpoint
(any 4, 0.25 each)
REFERENCE
BW SYST TRNG MAN 14-54
MSWER
3.18
( .75)
1) Overspeed (e4 cetAul dg*Ay$b
2) Interceptor valve fast timin{(e M(/MM)tfby
dh
y
3) Load drop anticipatorfat Nd hh25 a h)
-
REFERENCE
BW SYST TRNG MAN 37A-74
i
, _ . _ _ _ _ , _ _ _ _ _ _ _ _ _ _ _ . . -
__ ____
. , . _ _ . _ _ _ . _ _
. . _
__
- _ _ _ _ _ _ , . . _ _ _ _ _ _ .
4.
PROCEDURES - NORMAL, A8 NORMAL, EMERGENCY AN0
PAGE 36
RADIOLOGICAL CONTROL
.. . , . .
ANSWERS -- BRAIOW000142
-86/10/22-WEALE, G./REIDINGER
.
ANSWER
4.01
(1.50)
1. Restore Tavg > 550F(0,5) within 15 minutes (0.25), or
(0.75)
2. Be in hot standby (0.5) within next 15 minutes (0.25)
(0.75)
REFERENCE
TS, pgs. 3/4 1-6 8 B3/4 1-2
ANSWER
4.02
(2.50)
a.
Dose to whole body must not exceed 3 rem per quarter
(0.5)
The 5(N - 18) limit must not be exceeded
(0.5)
Individual's exposure history must be documented on NRC Form 4
(0.5)
b.
Administrative and Support Services Assistant Superintendent
(0.5)
c.
3000 mrem /Q - 1000 mrem = 2000 mrem at 200 mrem /hr = 10 hours1.157407e-4 days <br />0.00278 hours <br />1.653439e-5 weeks <br />3.805e-6 months <br />
(0.5)
REFERENCE
CW RAD PROT STDS 24,25
ANSWER
4.03
(1.50)
a.
1.3% delta-k/k
(0.25)
b.
Once per 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> (0.25)
c.
Immediately initiate and continue boration(0.25) at > 30gpm(0.25) of
solution at > 7000 ppm (0.25) until shutdown margin ilmit is met.(0.25)
REFERENCE
TS 3/4 1-1
..
.
.
_ _ - . _ _ _ _ .
. _ . , .__ .__ - -__ - _
_-
_-
_ - _ _ _ _ . - _ . _ _ _ _ _
4.
PROCEDURES - NORMAL, ABNORMAL, EMERGENCY AND
PAGE 37
RADIOLOGICAL CONTROL
.
ANSWERS -- BRAIDWOOD 142
-86/10/22-WEALE,G./REIDINGER
,
ANSWER
4.04
(1.00)
1) Uncontrolled increase in steam generator level
2) SJAE radiation abnormal
3) SG blowdown radiation abnormal
4) SG radioactivity abnormal
5) Main steamline radiation
(any 4 at 0.25 each)
REFERENCE
ANSWER
4.05
(1.50)
The miniflow isolation valves for the SI pumps are shut during this
procedure (0.5). If the RCS pressure is greater than the SI pump discharge
pressure, there will be no flow thru the pumps (0.5) to remove pump heat
and resulting overheating could damage the pumps (0,5)
(1.5)
REFERENCE
18wEP ES-1.3; BW SYST TRNG MAN 58-37
,
ANSWER
4.06
(1.00)
1) Rod Ejection
(0.25)
2) Loss of Steam / Secondary Coolant Accident
(0.25)
3) Steam Generator Tube Rupture
(0.25)
4) Loss of Coolant Accident
(0.25)
REFERENCE
8W SYST TRNG MAN 58-6
,
. . . - - - . -
-
. - . _ _
.
-_.
.- . - - . __.---.._. . _ . _ -
. _ -
4. - PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 38
RADIOLOGICAL CONTROL
j
=<
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE,G./REIDINGER
t
-
ANSWER
4.07
(1.50)
.
1) Subcriticality
2) Core Cooling
3) Heat Sink
4) RCS Integrity
5) Containment Integrity
6) RCS Inventory
(0.2 for each LS7, 0.3 for order)
REFERENCE
SwST BOOK
ANSWER
4.08
(1.50)
a.
Blow it down to the blowdown system. [0.5]
b.
Blow it down (backfill) to the RCS.
[0.5]
c.
Cooldown with steam dumps.
[0.5]
REFERENCE
IBwEP-3
ANSWER
4.09
(1.75)
a.
Use AFW and steaa to steam dumps (0.50).
Use AFW and steam to steam generator PORVs(0.50).
(1.0)
b.
Draining and charging
Refueling pool cooling / recirculation
SI pump injection
Inject accumulators
(any 3, 0.25 for each)
REFERENCE
18w0A PRI-9,18w0A REFUEL-4
.
4.
PROCEDURES - NORMAL, ABNORMAL, EMERGENCY AND
PAGE 39
RADIOLOGICAL CONTROL
- ,y
s i
ANSWERS -- BRAIDWOOD 182
-86/10/22-WEALE,G./REIDINGER
,
ANSWER
4.10
(2.25)
1) Place a Centrifugal Charging pump in operation if not operating (0.25)
to have high flow rate for borated water (0.5)
(0.75)
2) Open IMOV-CV112D/E(RWST TO CHG PUMPS SUCT VLV)(0.25) to have source of
borated water (0.5)
(0.75)
3) Close IMOV-CV112 B/C (VCT TO CHG PUMPS SUCT YLV)(0.25) to try to stop
path of dilution. (0.50)
(0.75)
REFERENCE
IBw0A PRI-11
,
.
ANSWER
4.11
( .50)
--a.--
REFERENCE
IBw0A R00-3
ANSWER
4.12
( .50)
--b.--
REFERENCE
ANSWER
4.13
(1.00)
a.
50
b.
320
c.
180
,
d.
50
(0.25 each)
'
REFERENCE
BwGP 100-1
1
i
l
l
.
.
-
,
4
PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND
PAGE 40
RADIOLOGICAL CONTROL
,
,3
%
-
ANSWERS -- BRAIDWOOO 182
-86/10/22-WEALE,G./REIDINGER
- ,
,
ANSWER
4.14
(2.00)
1) Manually run back the turbine at max rate by:
a) Pressing TURB MAN (0.33)
b) Pressing FAST ACTION (0.33) and GOV LWR (0.33) simultaneously
(1.00)
2) If turbine cannot be run back, Pull-to-Lock EH pumps (0,5)
3) If turbine cannot be run back, initiate Steamline Isolation (0.5)
REFERENCE
18wFR-S.1
ANSWER
4.15
(1.50)
1) Source range hi flux trip
2) Intermediate range hi flux trip
3) Containment pressure (hi-hpray actuation
(0.5 each)
REFERENCE
BW PLS PG 7
ANSWER
4.16
(3.50)
a. (1) Inadequate shutdown margin (Keff)(0.25), limit 0.95 (0.25)
(2) Inadequate shutdown margin (Boron)(0.25), ifmit 2000 ppm (0.25)
b. (1) Inadequate shutdown margin (delta k/k) (0.25), limit 1.3% (0.25)
(2) Rods low (0.25)below bank insertion ilmit (0.25)
(3) Failure of rods to fully insert on trip (0.25), limit one (0.25)
(4) Reactivity increase (0.25), unexplained / uncontrolled (0.25)
(5) Uncontrolled cooldown (0.5)
(6) Inability to borate normally (0.5)
(any 5, 0.5 each)
REFERENCE
18w0A PRI-2
,
- , , , . - . - - - .
,
, , . _ - . . -
- - - - . .
,
-
..-
- - - - , - ,- -
, .