ML20207M359

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Exam Repts 50-456/86-03 & 50-457/86-03 on 861027,1111-14 & 18-22.Exam results:15 of 17 Senior Reactor Operators & 6 of 7 Reactor Operators Passed Exams
ML20207M359
Person / Time
Site: Braidwood  Constellation icon.png
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

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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

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K. L. Parkinson, Sonalysts

F. W. Victor, Sonalysts

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Chief Examiner

Da'te '

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Approved By:

T. M. Burdick, Chie

Operator Licensing Section

Date

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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.

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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.

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(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.

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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

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(d) Q = wf AH (wf = Wp)

(e) h=UAAT

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b.

Define the following symbols / terms used in the above equations as they

apply to a steam generator.

(0.25)

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(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.

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1.06

Resolution

Candidate answers that stated opening the surge tank isolation valve halfway

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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:

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(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

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BRAIDWOOD CONTENTION:

Answer key Part 3

3.

Containment pressure hi-3 spray actuation.

REFERENCE:

BW PLS PG-10

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BW SYST TRNG MAN. 59-Page 21

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4.15 Rasolution

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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."

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Full credit was awarded to candidate answers that stated

3)

Containment pressure Hi-3 spray actuation.

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NOTE:

The facility should designate the correction / resolution of

Section A.11.b.3) as an open item.

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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:

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ACP higher than ECP.

b.

ACP lower than ECP.

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c.

ACP is unchanged.

1.

Actual RCS temperature is 551*F at criticality.

(0,5)

NRC ANSWER 5.06

1.

b.

(ACP lower than ECP)

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BRAIDWOOD CONTENTION:

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The question does not state the temperature at which the ECP was calculated

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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

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with Tavg equal to 551*F and the reactivity effects would be corrected for the

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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,

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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)

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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:

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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),

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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,

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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

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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.

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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

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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

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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

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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)

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Undercompensating results in a higher than actual reading, (0.50) and if

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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)

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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:

BW STM VOL. 3 CH 26 (26-42)

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

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closer review, the " " mark instead of a "0"

shows that " manual"

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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.

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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."

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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

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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

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2. - charging pump flow > 200 gpm

or

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3.

positive SI flow

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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

reactor trip.

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

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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)

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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

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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)

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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:

10 CFR 20.403

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.

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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)

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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

!

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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

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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.

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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.

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B99 AN C. Hm6ENsaJ

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U. S. NUCLEAR REGULATOR

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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

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NRC RULES AND GUIDELINES FOR LICENSE EXAMINATIONS

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  • 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.

.

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NRC RULES AND GUIDELINES FOR LICENSE EXAMINATIONS

.

During the administration of this examination the following rules apply:

.-

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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

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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.

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18. When you tompIete ko*ur examination, you shall:

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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.

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5.

THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND

PAGE

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THERMODYNAMICS

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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,

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CWL :

1.

O.

m

3. M

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THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND

PAGE

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THERMODYNAMICS

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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

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4 6 - 4 - - m , ex g ?

.p

3. cm sov, A d

p

(***** CATEGORY 05 CONTINUED ON NEXT PAGE *****)

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THEORY OF NUCLEAR POWER PLANT OPERATION, FLUIDS, AND

PAGE

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THERMODYNAMICS

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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:

a. ACP higher than ECP.

b. ACP lower than ECP.

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 *****)

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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 *****)

.

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_ _ _ - . - . - - ,__,, , . , _ . - - - , . - , ,

, , _ , . - - - -

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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 *****)

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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 *****)

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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 *****)

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6.

PLANT SYSTEMS DESIGN, CONTROL, AND INSTRUMENTATION

PAGE

9

,,

-

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~

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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

  1. 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 *****)

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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.

Overspeed

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 *****)

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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 ***** )

-_

. _

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. -

.-

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-

-

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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.

RCS

SG

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 *****)

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7.

PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND

PAGE 14

,

RADIOLOGICAL CONTROL

.

,

,

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~

.

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 *****)

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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 *****)

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.

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7.

PROCEDURES - NORMAL, ABNORMAL, EMERGENCY AND

PAGE 16

.,

RADIOLOGICAL CONTROL

.

.

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.

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.

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 *****)

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8.

ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS

PAGE 17

.

.

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.

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 *****)

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8.

ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS

PAGE 18

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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

SE

<

SF (licensed)

NSO

EA

SCRE or STA

,

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 *****)

/

-

$

OM

% , k % ann.

h O k-

.

u.

- .-


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8.

ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS

PAGE 19

,

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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:

CSF

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

.,

.

.

.

.

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.

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. . . . . . . . . . .

. _ _ _ .

.,

..

..g.

.[

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8

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,

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.;

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..

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. .,. ..

_.9,_..

!

..

.

_ . . _ . .

.

. . . . _ . . _ . . . . . . .

.

.,

.

l.

.

..

g

-

-

1

t

-

.

100 PSI A -

s-

e

.

.

g

E

.

>

.

.....J.

. . . .

e.

..

1e

. . . . . .

t

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.

.-

n

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m *

=

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o

    • 8

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t

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wi

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.s

s

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8

.

.. .

l

1000 PSIA

  • *

.

..;

.

..

.,.

.. ......

-

,

,

.,

.

...

.

.

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.

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.

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.

.g.

.

.

.

.

. ..

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.

..

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

_ _ - -.

.- .

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.

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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

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294.0

12.512

0.016664

31.135

31.151

172.11

975 4

11475

03001

1.4697 13698

204 8

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13.568

0 016691

28.862

28.878

176.14

9 72.8

1149 0

03061

1.4571

17632

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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

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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

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18.556

0.016805

21.529

21.545

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20.073

196 31

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20035

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236.0

23.216

0.016895

17.454

17.471

204.40

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0.016926

16304

16321

208.45

952.1

1160.6

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26.826

0.016958

15.243

15.260

212.50

949.5

1162.0

0 3591

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13085

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248.9

28396

0.016990

14.264

14.281

216.56

946 8

1163.4

03649

13379

1.7028

240 0

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252.s

30.883

0.017022

13358

13 375

220.62

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03706 1.3266 16972

252.0

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255.0

33.091

0.017055

12.520

12.538

224.69

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200.0

35.427

0.017089

11345

11362

22836

938.6

1I67.4

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268 8

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37.894

0.017123

11.025

11.042

232.83

935.9

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0 3876

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258.8

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0.017157

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0 3932

1.2823 16755

258 8

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43.249

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240.99

930 3

1171.3

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272.0

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276.0

46.147

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927.5

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249.17

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0.4098

1.2501

1.6599

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284.0

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8.1280

8.1453

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12395

1.6548

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0 01734

76634

1.6807

257.4

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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

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2968

63.084

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Specific Volume

Enihalpy

Entropy

Temp

Lb per

Sal.

Sat.

Sat.

Sat.

Sat.

Sat.

Temp

Fahr

SqIn.

Liquid

Evap

Vapor

Liquid

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h

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sig

sg

t

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l

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67.005

001745

6.4483

6.4658

269 7

9100

1179.7

0 4372

11979

I6351

-

300 e

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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

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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

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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

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2.9392

2.9573

332.3

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0 01816

2.8002

2.8184

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1.0424

1.5637

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169.113

0 01821

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2.6873

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1195.9

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1 0332 1.5595

363 3

t

372.0

177.648

0 01826

2.5451

2.5633

345 0

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0 5314

1.0240 1.5554

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186.517

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2.4279

2.4462

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338.0

195.729

0.01836

2 3170

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0 5416

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205 294

0.01842

2.2120

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1.5432

394.0

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837.2

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0 5516 0 9876

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225.516

0.01853

2.0184

2.0369

366.5

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395.0

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0.5617 0 9696

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247.259

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1.8444

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1.5274

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258.725

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1.7640

1.7827

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308.780

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381.54

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0 01947 1 05764

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Abs Press.

Specific Volume

Enthalpy

Entropy

Temp

Lb per

Sat.

Sat.

Sat.

Sat.

Sat.

Sal.

Temp

Fahr

SqIn.

Liquid

Evap

Vapor

Liquid

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p

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vg

he

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h

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sl8

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t

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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

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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

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566 15

0 02000 039716

0 81717

464.5

739.6

1204.1

0.6648 0.7871

1.4518

480.0

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484 e

587 81

0.02009 036613

038622

469.1

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1203.8

0.6696

0 7785

1.4481

484.0

438 s

610.10

0.02017

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0.75658

473.8

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1203.5

0.6745 03700 1.4444

438.9

492 0

633.03

0 02026 030794

032820

478.5

724.6

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0.6793

0.7614

1.4407

492.5

496 8

656 61

0 02034 0.68065

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483.2

719.5

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0.6842

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496.0

,

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680.86

0 02043 0.65448

0 67492

487.9

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504.0

705 78

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0 64991

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0.6939

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504.0

508 8

731.40

0 02062 0 60530

0 62592

497.5

7033

1201.1

0 6987

03271

1.4258

500.8

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757.72

0 02072 0 58218

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5023

698.2

1200.5

0.7036

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516.8

784.76

0 02081

0 55997

0.58079

507.1

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1199.8

0.7085

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516.0

528.s

812 53

0 02091

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0 55956

512.0

687.0

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1.4146

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0 02102 0.51814

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516.9

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1198.2

03182

0 6926 1.4108

524.0

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870 31

0 02112 0 49843

0 51955

521.8

675.5

1197.3

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0.6839 1.4070

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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

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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

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1193.1

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544.0

548 e

1028 49

0 02169 0.41048

0.43217

546 9

645.0

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0.6400 1.3876

548.0

552 s

1062.59

0.02182 0 39479

0 41660

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638.5

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13837

552.8

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1097.55

0 02194 0 37966

0.40160

557.2

632.0

1189.2

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0.6222 13797

556.8

560.8

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0.02207 0 36507

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562.4

625.3

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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

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512 8

1246 26

0 02249 0 32429

0 34678

578 3

604.5

11823

0.7775

0.5859 13634

572.8

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515.0

128534

0.02264 0 31162

0 33426

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597.2

1180.9

0.7825

0.5766 1.3592

578.8

5000

1326.17

0 02279 0.29937

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589.I

589.9

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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

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1174.8

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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

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14978

0 02345 0 25425

0 27770

611.4

558.8

11703

0.8082

0.5293 13375

595.0

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.

.

,

Abs Press.

Specific Volume

Enthalpy

Entropy

Temp

Lb per

Sal.

Sal.

Sal.

Sal.

Sal.

Sal'

ten

Fahr

SqIn.

Liquid

Evap

Vapor

Liquid

Evap

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p

vg

vgg

vg

hg

h gg

he

sg

sig

se

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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

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16861

0.02422 0.21442

0.23865

634 8

524.7

1159.5

0.8294

0.4896 1.3190

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1735 9

0.02444 0.20516

0.22960

640.8

515.6

1156.4

0.8348

0.4794 1.3141

816.8

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1786.9

0.02466

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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

BW STM VOL 5, CH 59

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

BW STM V0L 2 CH 15a,II,A,1,1

(pu

BW STM VOL 2 CH 15a,II,0,1,a

T

BW STM VOL 2 CH 14,II,A,6

l

BW STM VOL 3 CH 23 appendix 0

BW STM V0L 3 CH 26,II,0,4

_ _ . .

.-

.-_

- , _ , - .

-

. . _ - , _ - - - - -

-

. -

- .

- _ - -

. - .

--

--

_ _ .

-

--

_

.

_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

BW STM VOL 2 CH 15a

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

,

loss of offsite power.

(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 STM V0L 3 CH 26 Appendix A

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

BW STM V0L 3 CH 19 Appendix A

>

.-.

_ . _ . , - . - - _

.__.--____,.-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

BW STM V0L 1 CH 9 (9 - 50/51)

ANSWER

6.11

(1.50)

b.

c.

e.

(0.5 each)

REFERENCE

BW STM VOL 1 CH 4 Appendix A

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.

Turbine trip

(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

1BWEP-0

,

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'

BW STM VOL 2 CH ISB

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

-

BW STM Y0L 2 CH 12 Appendix A

BW STM VOL 2 CH 14

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

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8.

ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS

PAGE 39

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ANSWERS -- BRAIDWOOD 182

-86/10/22-HAAGENSEN, B./REIDI

,

,

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.

ANSWER

8.04

(2.00)

i

a.

Position

Modes 1,2,3 or 4

Modes 5 or 6

SE

1

1

SF (licensed)

1

0

NSO

2

1

EA

7

5

SCRE or STA

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

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8.

ADMINISTRATIVE PROCEDURES. CONDITIONS. AND LIMITATIONS

PAGE 40

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ANSWERS -- BRAIDWOOD 182

-86/10/22-HAAGENSEN, 8./REIDI

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,

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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

,

10CFR50.72

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,

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8.

ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS

PAGE 41

ANSWERS -- BRAIDWOOD 182

-86/10/22-HAAGENSEN, B./REIDI

..

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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

NUREG 0654

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

NUREG 0654

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

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  • *

8.

ADMINISTRATIVE PROCEDURES, CONDITIONS, AND LIMITATIONS

PAGE 42

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ANSWERS -- BRAIDWOOD 182

-86/10/22-HAAGENSEN, 8./REIDI

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s

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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

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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

_ _ _ _ _ _ _ .

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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.

,

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- . , .

,,,,,,,-.----..,,--,_,p

n,, , - - - - ,. ,

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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.

!

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1.

PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,

PAGE

2

THERMODYNAMICS, HEAT 1RANSFER AND FLUID FLOW

., .

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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 *****)

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1.

PRINCIPLES OF NUCLEAR. POWER PLANT OPERATION,

PAGE

3

THERMDDYNAMICS, HEAT TRANSFER AAD FLUID FLOW

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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

.

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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 *****)

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1.

PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,

PAGE

4

THERMODYNAMICS, HEAT TRANSFER AND FLUID FLOW

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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.

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(***** CATEGORY 01 CONTINUED ON NEXT PAGE *****)

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1.

PRINCIPLES OF NUCLEAR POWER PLANT OPERATION,

PAGE

5

THERMODYNAMICS, HEAT TRANSFER AND FLUID FLOW

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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 *****)

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2.

PLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS

PAGE

6

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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

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(***** CATEGORY 02 CONTINUED ON NEXT PAGE *****)

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2.

PLANT DESIGN INCLUDING SAFETY AND EERGENCY SYSTEMS

PAGE

7

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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)

b. IA DG Control Panel

(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 *****)

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2.

PLANT DESIGN INCLUDING SAFETY AND EERGENCY SYSTEMS

PAGE

8

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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

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2.

TLANT DESIGN INCLUDING SAFETY AND EMERGENCY SYSTEMS

PAGE

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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 *****)

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3.

INSTRUMENTS AND CONTROLS

PAGE 10

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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 *****)

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INSTRUMENTS AND CONTROLS

PAGE 11

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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 *****)

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INSTRUMENTS AND CONTROLS

PAGE 12

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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

,

)

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3.

INSTRUENTS AND CONTROLS

PAGE 13

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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 *****)

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3.

INSTRUMENTS AND CONTROLS

PAGE 14

. .

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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 *****)

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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

,

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.

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 *****)

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PROCEDURES - NORMAL, ABNORMAL, EERGENCY AND

PAGE 17

, RADIOLOGICAL CONTkOL

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,

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 *****)

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PROCEDURES --NORMAL, ABNORMAL, EERGENCY AND

PAGE 18

,, , RADIOLOGICAL CONTROL

,,

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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

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(***** END OF CATEGORY 04 *****)

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(************* END OF EXAMINATION ***************)

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.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

  1. 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

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Enthalpy

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Temp

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Sal.

Sal.

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Temp

Fahr

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67.999

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108.0

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331.1

331.1

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1035.9

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0.1331

1.8444 1.9775

102.8

134 g

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0 016144

313.1

313 1

71.992

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296 18

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251.37

251.38

79.98

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1.4299

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1.7938 1.9480

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1.5133

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214.20

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135.57

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122.98

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0.2473

1.5822 1.8295

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1.5616 1.8184

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Sat.

Sat.

Sat.

Sat.

Sat

Temp

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Fahr

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Liquid

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0.016522

48.172

18.189

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46.249

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0.016547

44.383

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42.621

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9.340

0.016572

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Enthalpy

Entropy

Temp

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Sal.

Sal.

Sat.

Sal.

Sal.

Sal.

Temp

Fahr

SqIn.

Liquid

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Vapor

liquid

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liquid

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vig

vg

hg

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he

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sig

s

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g

i

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67 005

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6 4483

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269 7

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0.4372

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71.119

0 01749

6 0955

6.1130

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1.1877

1.6303

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5 7830

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1.1776

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312.3

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318.8

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328.0

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0.4745

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302 9

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1.5981

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111.820

0.01783

3 9681

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340.0

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3 7699

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344.s

124 430

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3 5834

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315 5

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0 4954

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1.0799 I5806

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352.s

138.138

0 01801

3 2423

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323 9

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0 5110

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1.5721

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388.8

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364.s

160.903

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2.8002

2 8184

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2.6873

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0 5263

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186.517

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2.4279

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2.2120

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1198.7

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1.5432

334.I

338 g

215 220

0 01847

2.1126

2.1311

362 2

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0 5516 0 9876

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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

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488.8

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1.8630

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1.5274

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484.3

258 725

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1.7640

1.7827

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1.5234

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1.5195

488.8

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Specific Volume

Enthalpy

Entropy

Temp

tb per

Sal.

Sal.

Sal.

Sal.

Sal.

Sal

Temp

Fahr

SqIn.

Liquid

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Vapor

liquid

Evap

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vr

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h

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t

t

p

vi

ver

g

4ES I

466.87

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0.97463

0 99424

441.5

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0 6405 0 8299

1.4704

468.0

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0 6454

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1.4667

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0 01976 0.89885

0 91862

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468.0

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524 67

0 01984 0 86345

0 88329

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0.6551

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1.4592

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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

turbine trip.

(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

18wEP-3

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

10CFR20

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

,

- , , , . - . - - - .

,

, , . _ - . . -

- - - - . .

,

-

..-

- - - - , - ,- -

, .