ML20238D196

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Exam Rept 50-259/OL-87-03 on 871117-18.Exam Results:One Reactor Operator & Senior Reactor Operator Passed Exam. Rept for All Three Units
ML20238D196
Person / Time
Site: Browns Ferry  
Issue date: 12/03/1987
From: Brockman K, Payne D
NRC OFFICE OF SPECIAL PROJECTS
To:
Shared Package
ML20238D178 List:
References
50-259-OL-87-03, 50-259-OL-87-3, NUDOCS 8801040145
Download: ML20238D196 (29)
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Text

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l ENCLOSURE 1 EXAMINATION REPORT 259/0L-87-03 Facility Iicensee:

Tennessee Valley Authority 1

6N 38A Lcokout Place

{

1101 Market Street Chattanooga, TN 37402-2801 Facility Name:

Browns Ferry Nuclear Plant Facility Docket Nos.:

50-259, 50-260 and 50-296 Written and operating make-up requalification examinations were administered l

at the Browns Ferry Nuclear Plant near Decatur, Alabama.

4 3cyg J Kd @

Chief Examiner:

/

. C/ PayneV /

Date Signed 1

Approved Byf MMuM#

J SEC @

p E. Bro 3 Man #5ection Chief Date Signed Summary:

Examinations were administered on November 17-18,-1987.

A written (Section 1 only) examination was administered to one R0 candidate i

and an operating examination (oral only) was administered to one SR0 candidate.

One R0 passed the written examination. One SR0 passed the operating examination.

Based on the results described above, one of one R0s and one of one SR0s passed the overall examination.

The one technical correction on the written examination was not due to inaccurate /

I incomplete materials provided to the Commission for examination preparation.

1 8801040145 871217 PDR ADOCK 05000259 V

DCD i

f REPORT DETAILS 1.

Facility employees Contacted:

R. G. Jones, Operations Training Section Supervisor

  • E. S. Howard, License Operator Training Supervisor
  • Attended Exit Meeting 2.

Examiners:

  • D. C. Payne, Region II
  • Chief Examiner 3.

Examination Review Meeting:

At the conclusion of the written examination, the chief examiner provided your training staff with a copy of the written examination and answer key for review.

The NRC resolutions to comments made by the facility reviewers are listed below.

P.0 Exam (1)

Question 1.02 1

Facility Comment:

Choice "h" was the only logical choice for the candidate to match to CHF for this question.

CHF more accurately is defined as the value of heat flux at the point where transition boiling occurs.

This term is old and no longer used as a thermal limit.

It is contained in Chap. 8 of the HT&FF book only as a " history lesson" for the students.

1 Recommend deleting the use of CHF or change the word " point" to " heat flux" in choice "h" for future use of this question.

i NRC Resolution:

Comment acknowledged.

While the technical content of the question remains unchallenged, future effort will be made to orient the examination to more plant specific terminology.

No change to the exam or answer key necessitated.

(2)

Question 1.04 Facility Comment:

The three effects, as discussed in the Reactor Theory Book, Chap. 4, that cause an increase in voids 'to i

add negative reactivity are reasonance escape, fast leakage, and thermal leakage.

The other K factor that changes is thermal eff utilization and it increases.

Part 2 of the NRC answer leads one to believe that this factor would decrease on an increased CR -

neutron absorption, and thus an increased worth.

Recommend deletion of Part 2 of NRC answer, and accept for Parts 2 and 3 an increase in thermal and fast neutron leakage.

-)

~

j NRC Resolution:

Comment accepted.

The question does solicit three.

" negative" contributions to the void reactivity coefficient, while part "b" of the answer key is in fact a " positive" contribution.

I Therefore, part "b" of the answer is changed to " Thermal neutron leakage increases" for 0.5 points while part "c" is modified to

" Fast neutron leakage increases"-for 0.5 points.

Total question value remains the same at 1.5 points, 1

4.

Exit Meeting l

At the conclusion of the site visit, the examiner met with-1 a representative of the plant staff. to discuss the examination.

{

There was one generic weakness noted during the operating examination.

The candidate exhibited significant unfamiliarity with identifying the-requirements for and locating selected Surveillance Instructions; however, with time all Surveillance Instructions were found.

While this short coming reduces efficiency, it is not a concern of safety significance.

The cooperation given to the examiner and the effort to ensure an atmosphere in the Control F.oom conducive to oral examinations was noted and appreciated.

The licensee did not identify as proprietary any of the material provided to or reviewed by the examiners.

~

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NL K'LE AR RE.GULATORY COMMISSJON REACTOR OPERATOR REQU6L]FICATIlmi EXnMINAT10N FALILITY:

.!][;:OtuhEf ER[! f _ L._TN., __ _

FW. '.C T O R T Y F'E :

EWR-GE4 t7 DATE ADHi.NISTERED: _BT/.1.lf $k._,__.,_._._,._.__

EXAMINER:

. P!)y!L._ C.

C A N D I D A T fi..

_,h kU k _. _ _., _ _ _ _ _.

Read the attached instruction page c a r e-f u l l y.

Th1E examination replaces the current cycle facility administered requalificatTon en e mi n ati on.

Re t r ai rri n g r e qu i r crwn t s for ailure of this eM am1 n a ti on are the samt as for failure of a.~equalif1 cation examinatlan prepared and administered by vour training s t a f -f,

Pointe for each questian are indicated in parenthews after the questaan.

The passing grade requires at least 70%

in aach category and a f i nal orade of at 1 east E)0 %.

Ex ami nati on papera will be picked up iour (4) houru M t er the m: a mi nst i on starts.

O?-

C AT EWEY

, 0" CANDIDATE'R CATEGOW

.. hU.4UE _.10I.G(

. _ 5 [ C LM._.,_,

_y @ LW __

_._ _ _,_,_ _C @IE Q 0Ry_._ _.._,

1.7. Q _.100 00

_ _ _ _,.._ 1 6 'R I o!C I PLEG GF NUCLEAR PCWER PL. AN T OPERATTUN, THERMOD(NAMIC5 3 HEAT T RA%FER AND Ft..UID F LOW 11.00

/

Totals Fi nal Grads A}l Wor l: d2 c

or th)n e. fe rie l n a t.1 D')

15 Cy OWh.

} haVD n tdi t h s ?P g.1 V ta n PDF FECe2

,e 41 a.

l CandIdake % blQn3turO l

1 i

k 1

b

4 es N RL' RULE 5 AND GLJ1DE LlNES F OR LICENSE EX AMlNW1 J ONS During the administration of this econ 1nat. ton the following rule 3pplv.

1.

Che ?2og on tf->'

at i oli m e a n ts an automatic denial of vuur appli cat i or, and could r>1 ult in more severe penaltaes.

k.

F:es t r oc:n tripr ar e to be limited and only one cendidate at a time may leave.

You must. av~nd all contacts with anyor,e out si de the er ami nati on room to avoid even the appear ance or possibility of cheating.

T.

Une black i n l: or dark pencal qQ l,t to tacilitate l eg i b l e r epr oduc t i ons.

4.

Pr i. n t your name in the blsnk provided on the cover shunt of the e;: ami n at i on,.

5.

f~i l l in the date on the cover sheet of the examination (if n ec e n tar y ).

6.

Use on1y the paper pr ovi ded +or answeru 7.

Prant your name in the upper r i g h t --h an d corner of the f1rst pace of each section of the an swn4 sheet.

B.

Consecutively number each answer c h n e t,, write "End oi Cat eg or y _,, " a :-

d ap p r o p f I a t e,, starl PaCh cateQory On a n fj ef p r< g Ed, Write gr11 y og al,} {

Qe of the paper. and write "Laat Pge" on the last an e: wor sheet.

9.

Number c> i c h insm r as ta < a t e ;) a r v and numoer, for example, 1. 4.,

6.7 1 LL Sk1p at 1 east Fhreo 12 nes betwuer: nach answer.

11.

Separat e in s vm 7 h enet ' from pad and place f1ntsned answer sheets face dawn on yc <ur desk or table.

12. Uct abbreviataans or l v if they are commonl y used in facility

.l i t;e r a,t.u r e.

13. The point value for each question ia indiceted in par en theses after the quest 3On and can be ut ed as a guide for the depth of answer requ1 r eci.
14. Show all c al cul o t t onn, m?thods, or assumptions used to obtain an answer to mathema t i c a] prob)eme whether ina3tated in the question or not.
15. Partial c red 2 t.

c,a y be given, lherefore, ANSWER ALL PARTS Dir fHE QUE9 TION AND DO l>0T LEAVE ANY ANEMEF B L N.iK.

1 6,. If parts of the e amination arn not clear o s, to intent. ask questions of the gge n:1_ r3 e r on1 y.

17. You must utan the r; t a t r m e n t on the cover rheet that J.ndicates that the Work IG your own and yOu llave MOL recO1YUd Or been gl vef) aGsistante in c o m[) } e.'t I n ci t h (? e; ami nat ] Ul t.

lhlb mus+ be done after the ex ura n at i on has been Corp}elnd.

f c.

s

18. When you comalete you-tuam1 nation, you shal]:

a.

Assemble your o aminatiott follows.

I1)

E ): 3 n.

cit i c <;, t i o r i s a top.

(2, Ex a,o aids f i gure ;, tablea, etc.

(7) l'in E W Ec t' paQPG I n t I ud i flQ f i g u r E' Inhich are part of the aritwer.

b.

Turn in your CDpV Of thO e, a fllI n a t i Un and dl1 pdOEb UGGd tC a n 53 W O r the i?. Cim l n a t 103 Qt iP ut 1 Cn b.

C.

~Iurn i ll all Otrap p ia p Pr and tl>e balance of the paper t h a t.

you did not use for e n 9:na e r i r q the queStians, d.

Leave the En' a rir i n ft t i on area, 24 G dPf1ned b 'j t h t" L n e n','A n e r.

If a< f t tir

)

leaving, you are found in thic area while the esam1 nation is s;t i l l in progress, your ]icanse may tse denied or r evokea.

I

_________________----_-__-__a

1.r__CBINGIELES_OE_NyGLE98_EgWEB_CLBNLDEgBGIIQL PAGE

?

',t IHEBdQDyd@dlCh _ HEAT IBBNSEEB,680_ELUlp_ELgW OtJESTION 1.01 (1.00)

.i WHICH GNE of the f ollowing is the QUALITY of a 540 deg F vapor-l i qui'd.

mixture whose specific enthalpy is 1175 BTU /lbm?

a.

O.559 b.

0.816 c.

0.964 d.

0.971 QUEST 10N 1.02 t2.00)

MATCH each.of the lettered i t emro with.one of the numbered items.

A.

letter-number sequence is sufficient.

)

1.

MAPRAT 5.

PC10MR 2.

APL.HG R 6.

CHF 3.

CPR.

7.

TOTAL PF 4.

FLPD 8.

LHGR

_,_ _ o.

Parameter by which plastic strain and def ormation are limi ted l

to less than 1%.

__b.

Ratio of bundle power required to produce onset. of t ransi t i on boiling somewhere in the bundle to actual. bundle' power.

_.__._c.

Parameter by which peak ' clad temperature is maintained less than 2200 deg F during postulated Design: Basis Accidents.

,__._ d.

Contains guidelines restricting, power ramp rates above the t.hreshold power.

1 l

l

___e.

MAPLHBR / LIMLHGR

~

_,_f.

Ratio of highest pin power in a node to'the core average pin.

power.

1

__,__g.

As long as this factor i s-l ess t han 1.' O, the LHGR thermal' limit-will not be exceeded.

__ _ h.

Point at which nucleation'becomes-so dense that-bubbles coalesce and form a vapor film.

i l

1

(*****

CATEGORY 01 CONTINUED ON NE X T P AC,E * * * * * )

]

l~

1x__EB]NCIELES,,gE_NMCLEGG_EgWEB_ELONLDEgBSIlON, PAGE 3

IBEBMODYUBMIGh tEBLIBBNSEEB_GND_,ELylp FLOW OUESTION 1.03 (1.50) l

' The THRESHDLD power -bel ow which PCI fai1ures do not occur is known ta DECREASE wtth fuel burn-up.

LIST THREE (3) reasons f or ' thi s., decrease

.in the PCI threshold.

QUESTION 1.04 (1.50)

An' increase in vold content in en operating' reactor causes a negative reactivity i n ser t.t on.

DESCRIBE THREE (3) effects which cause the void reactivity coefficient (al pha-v) to be negative.

QUESTION' 1.05 (1.50) j Answer EACH of the following regarding the XENON transient'after:a significant DECREASE in reactor power from high power oper a t i on.

a.

EXPLAIN Why Xenon production exceeds Xenon removal (i.e.,

ton-centration increases) following the power change.

(0.5) b.

STA1E how peripheral control rod worth is affected (INCREASE DECREASE 3

REMAIN THE SAME) during the xenon peak.

JUSTIFY your response. (0.70) c.

If the decrease in reactor power was from 100% to'50%, would the NEW J

(50% power) equilibrium xenon reactivity be MORE THAN, LESS THAN, or EQUAL TO one half the 100% equ111brium value?

(0,25)

(***** CATEGORY 01 CONTINUED ON NEXT PA{bE

          • )

Lb

1,_._f;'BINQlELES_QEJgGLEBB_EOWEB ELGNI_OBEB8110N3, PAGE 4

ISKBdRDXUGulG h _UEGI_IBON EjEE B_8N D_ EL U I D _ELOW 4,

-QUESTION 1.06 (3.00)

Attached Figures DCP 1424A & B represent a transient that could occur at a BWR.

GIVEN:

(1)

A Total Loss of Feedwater occurs at time t = 0.8 min.,

(2)

No operator actians occur, and (3)

Recorder speed = 1 division

1. minute.

=

BRIEFLY EXPLAIN the cause(s) of ti.e f ollowing recorder indications:

a.

Core flow DECREASE (Point 2) b.

Reactor pressure INCREASE (Point 8) c.

Reactor pressure VARIATION (Point 12) d.

Reactor level DECREASE (Point 14) e.

Reactor level REDUCED INCREASE (Point 16) f.

Reactor power DECREASE (Point 17)

(0,5 eath)

QUESTION 1.07 (1.50)

During a reactcr start-up, Vef+ is 0.95 when the SRM channel s read 100-cps.

CAL.CLILATE the nes Eeff which would cause the SRM channels to read 270 cps SHOW ALL WORK' QUEST 10N 1.08 (2.00)

Uni t 3 is operat1 rig at 3292 MWt. (1007. of rated) and the reactor scram

]

setpoint is set for 118% of rated.

The total scram delay ti,ne is 30.

SECONDS, measured from the time the scram setpoint is exceeded until sufficient negative reactivity has been added to turn power.

If a nuc l ear e>t t ur si on creates a 10 second period,-CALCULATE the PEAK POWER for the excursion.

NOTE: (1)

IGNORE temperature and void effects.

(2)

ASSUME a CONSTANT period until power turns.

1

(*****

CATEDDRY 01 CONTINUED ON NEXT PAGE

          • )

L

.1 A _ _ [ B I N G'1 E L E S _ D E _ N U G L E G B E C W E B _ E L 6 N I _ Q E E B O I I O Lh -

.PAGE, 5

.ISEEDDDn!001GL _SE61_.lBGU5EES_8ND_.ELUID_ELOW QUESTION 1.09 (2.00)

Saturated steam with 100% quality enters the main condenser at 4.5 psia and

a. f low r a te of 6x10E+6 lbm/hr.

Condensate exits as'a saturated liquid.

Circulating water enters the condenser at 62 deg F and exits at 77 deg F.

a.,

CALCULATE the circulating water flow rate

( 1. 7 5 )-

b.

STATE whether condenser vacuum would INCREASE, DECREASE or REMAIN' 3

THE SAME.if the circulating water flow rate were INCREASED.

(0,20)

QLESTION 1.10 (1.00)

During a reactor shutdown, the vessel pressure decreased from 800 psig to 350 psig in 4S minutes.

a.

CALCULATE the cooldewn rate for this; time period.

b.

At the end of the 45 minute period. EXPLAIN whether any Technical' Specification OPERATIONAL LIMITB have been exceeded.

STATE.in your discussion which specific operational limits being applied.

(***** END OF CATEGORY 01

          • )

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

                          • 4*)

FIGURE DCPl 1424 A 9A.

.i,...,

e.,n,T97 6 persa100E 4

i 1

3 6

I

(

s

,a d

dB

  • a b "

g

' A

' '==.

1 4

0 to 40 60 40 100 130 0

4 s

13 to CORE FLOW TOTAL STEAM FLOW (a 10'ste/w) e is to in fw) 4 10

,,a""

a-g a

I' g*s-

~

y

~.

' O. -

' %.3 8

eso 970 sto 1010 1030 1080 0

4 s-13 to REACTOR PRESSURE -

TURBINE STEAM FLOW iPSICS s

(a le abs /tvl

}

a.m.

-~

n'-.

O o

_o

4 FIGURE DCP 1424B '~

93 sja::T TOTAL Lost OF FEEDWATER FLOW

? '

d'

,,r,g, geog l

I l

I j

r

(

\\

k

  • ,***,,**,,a,.

lam.

it e**,*

\\

-d Q

e4 u..

il

(

/

/

/

14

/

...-,,..--*,,,,....----~~~

3, L,

-==.,

9g 0

800 600 800 1200 1800 0

10 2(*

30 40 50 00 REACTOR PRESSURE REACTOR VESSEL LEVEL (PSIG)

(INCHES) 30 18

-_.,.j.7

P

- 19 jy 0

to 60 76

,100 125 0

.4 8

13.

10-APRM TOTAL FW FLOW

(% POWER)

(a 10s Ibe/ht) i

  • ^ - -

w.

- ~.-..- ~

.x.

.n u m

(

'. F w 'tfd Y = s/t Cycle Efficiency = (Net Work out)/(Energy in) 2

' W o Mg/ge s = Y t + 1/2 (ct )

e e = (Y - V )/t 9cernot = TA g

-T 2

E = Mc f

o 2

KE = MY /2 Yr = Y + At T

o 4

PE = Mgh v = e/t 2

P = ggh/gc A = (71D )f4 9 urbine = hj-h2r = wk1-2r t

Wk = P AY M=VA ev AE = 931( AM) g = 1/v h; - h21 1 - 21 wk Q = AAh 2

d = AC AT gZ j + V j

+ P jvj + u j + q 1 - 2 " 922+Y2

+PY22+U2 + wk -2 p

1 Q = UA AT Q

2gcJ J

Q 2gcJ J

J I#

u j + q1-2 = u2 + vk -2 I"l'P 1

o C = Au/AT y

J

-x/TYL C = Ah/AT Uj + Q -2 = U2 + Wk -2 p

1 1

TYL = 1.3/F Wk = h -h J

g Wk = M(h -h )

h = hr + X hrg HYL = -0.693/ F j

2 Wk - 2 =

P dv h = u + Pv/J II 1

2 2

J

'd Id "Id jj 22 PYj=PY22 R/hr = (0.55CiE)/d (meters) j 2

R/hr = 6CiE/d (feet) sur(t)

A = AN P = Po 10 A = A e-At p. p,,t/T c

A o 0.693/t SUR = 26.06/T SUR = 26( Ak/k)/ A* +(5,ff-( Ak/k)) T 1/2 t

eff = ((t 1/2)-(t ))/((t1/2) + (t ))

1/2 b

b E 0N T = (A*/AK/K) + ((5,7 - ( AK/K))/((kff-( AK/K)+ (d( AK/K)/dt))

( AK/K) = (K,ff - 1)/ Keff A o e/ f

( AK/K) = ( A*/ T) + (5,7f (1 +X,ff T))

/

N o 6.02 x 1023 'O

+ = 10- 4 A

X 0.1 seconds-I R RD = E-l = N 0-l eff = 0.05 seconds-1(up power)

(dovn power)

=

= 0.0125 seconds-I screm)

^'

P o (E-l v)/(3 x 10; o)

= 0.08 seconds"1 (cr(itical)

N = S - ( 1 - K,77 ) / ( 1 - K,ff)

N o No-(K,ff)"

M = 1/(1-K,ff) = CR /CR 3

o CRx = S/(1-Keffx)

M = ( 1 - K,77,) /( I - K,ff; )

l CR (1-K,ff 3 ) = CR (I'Keff2)

SDM = ( 1 - K,77 )/Keff j

2

~~

.., ' l Water Peremeters Miscellaneous Conversions 10 I gel. = 8.345 lb I watt = 3.12 x 10 fissions /second m

10 I gel. = 3.78 liters 1 curie = 3.7 x 10 dps 1

3 1 ft = 7.48 gel.

I kg = 2.21 lb m Density = 62.4 lbm/ft I hp = 2.54 x 10 Btu /hr 3

6 Density = 1 grem/cm 1MW = 3.413 x 10 Blu/hr Heat of Vaporization = 970 Btu /1b I inch = 2.54 cm m

Heat of Fusion = 144 Blu/1b F = 9/5'C + 32 m

1 f t. H O = 0.4335 lb / inch

  • C = 5/9(*F - 32) 2 7

Cp _ 1 Blu/lb

-F

'R = *F + 460 m

Physics, Thermo, and Heat Transfer 1 Blu = 778 f t-1b 7

~0 d = 0.172 x 10 Btu /hr-ft

  • R e = 2.718 m = 1.67264 x 10~

~

gram 1 ev = 1.60219 x 10 Coulomb-Volt p

-24

~I9 n = 1.67495 x 10 gram 1 Coulomb-Volt = 1.60219 x 10

. Joule m

-28 e = 9.10956 x 10 gram m

c = 2.99 x 10 cm/sec

~I O = 1.6 x 10 Coulombs p

y h = 6.626 x 10~

Joules-sec

-19 Q

=(-) 1.6 x 10 Coulombs e

i

~'

2 G = 6.67 x 10 N-m /kg 2

K = 9.0 x 10 N-m /C 1

e a 's p

Thermo. Formula Shsst.

1 i

E

_V12 pg g

y,a p,

ge Z2

+ 2ge + p geZa+ 2ge

+ p

=

V12 Pivt gZ2 V22 Pava _

gcJ + 2gcJ + J + ui + qt_2 = scJ + 2gcJ + J + un + wkt_2 p=

1_

PE = MZg v

gc KP. = 1/2 MV2

%. Weg h a _. h y g g4 h i - h a c,,__

ge Pu h=u+

J J,L Tds P = phs qt_2

=

ge f,,Pdu wki_:

=

Qi_ = mCp (AT) pAV m =

Pu = RT NPSH = (Pdy,- P ) EC.

s PV = MRT psg

  • I~N 72c. __ 8)u - Boer _ WKaet.

Q = m(Ah) h/N h/M Q = UA(aT)

Mc, --

Tia/

Water Parameters Conversions Cp = 1 BTU lbm of 1 hp = 2.54 x 108 BTU he p = 62.4 lbm 1 MW = 3.41 x 105 BTU j

ft*

hr i

f 1 gal. = 8.3 lbm 1 inch = 2.54 cm.

1 gal. = 3.78 1 1 BTU = 778 ft -lbf l

1 ft* = 7.48 gal oF = 9/50C + 32 OR = F + 460 OK = oC + 273 i

l 0273o

_j

Volume. ft'/lb Enthelpy. Blu/lb Entropy,8tu/lb a F P

Water Evap Steam Water Evap Steam Water Eysp Steam V

h hp, h,

se s eg s,

' Vr Vsg s

t 32 0.08859 0.01602 3305 3305

-0.02 1075.5 1075.5 0.0000 2.1873 2.1873 32 35 0.09991 0.01602 2948 2948 3.00 1073.8 1076.8 0.006) 2.1706 2.1767 35 40 0.12163 0.01602 2446 2446 8 03 1071.0 1079.0 0.0162 2.1432 2.1594 40 45 0.14744 0.01602 2037.7 2037.8 13.04 1068.1 1081.2 0 0252 2.1164 2.1426 45 50 0.17795 0.01602 1704.8 1704.8 18.05 1065.3 1083.4 0.0361 2.0901 2.1262 50 60 0.2501 0.01603 1207.6 1207.6 28.06 1059.7 1087.7 0.0535 2.0391 2.0946 60 70 0.3629 0.01605 868.3 868.4 38.05 1054.0 1092.1 0.0745 1.9900 2.0645 70 to 0.5068 0.01607 633.3 633.3 48.04 1048.4 1006.4 0.0932 1.9426 2.0359 80 SO 0.6981 0.01610 468.1 468.1 58.02 1042.7 1100.8 0 1115 1.8970 2.0086 60 100 0.9492 0.01613 350.4 350.4 68 00 1037.1 1105.1 0.1295 1.8530 1.9825 100 110 1.2750 0.01617 265.4 265.4 77.98 1031.4 1109.3 0.1472 1.8105 1.9577 110 120 1.6927 0.01620 203.25 203.26 87.97 1025.6 1113.6 0.1646 1.7693 1.9339 120 130 2.2230 0.01625 157.32 157.33 97.96 1019.8 1117.8 0.1817 1.7295 1.9112 130 140 2.8892 0.01629 122.98 123.00 107.95 1014.0 1122.0 0.1985 1.6910 1.8895 140 150 3.718 0.01634 97.05 97.07 117.95 1008.2 1126.1 0.2150 1.6536 1.8686 150 160 4.741 0.01640 77.27 77.29 127.96 1002.2 1130.2 0.2313 1.6174 1.8487 160 170 5.993 0.01645 62.04 62.06 137.97 996.2 1134.2 0.2473 1.5822 1.8295 17tr 180 7.511 0.01651 50.21 50.22 148.00 990.2 1138.2 0.2631 1.5480 1.8111 180 190 9.340 0.01657 40.94 40.96 158.04 984.1 1142.1 0.2787 1.5143 1.7934 100 200 11.526 0.01664 33.62 33.64 168.09 977.9 1146.0 0.2940 1.4824 1.7764 200 210 14.123 0.01671 27.80 27.02 178.15 971.6 1149.7 0.3091 1.4509 1.7600 210 212 14.696 0.01672 26.78 26.80 180.17 970.3 1150.5 0.3121 1.4447 1.7568 212 220 17.186 0.01678 23.13 23 15 188.23 965.2 1153 4 0.3241 1.4201 1.7442 220 230 20.779 0.01685 19.364 19.381 198.33 958.7 1157.1 0.3388 1.3902 1.7290 230 240 24.968 0.0!693 16.304 16.321 208.45 952.1 1160.6 0.3533 1.3609 1.7142 240 250 29.825 0.01701 13.802 13.819 218.59 945.4 1164.0 0.3677 1.3323 1.7000 250 260 3 5.-

0.01709 11.745 11.762 228.76 938 6 1167.4 0.3819 1.3043 1.6862 260 270 41.6.,o 0.01718 10.042 10.060 238.95 931.7 1170.6 0.3960 1.2769 1.6729 270 280 49.200 0 01726 8.627 8.644 249.17 924.6 1173.8 0.4098 1.2501 1.6599 280 290 57.550 0.01736 7.443 7.460 259.4 917.4 1176.8 0.4236 1.2238 1.6473 290 300 67.005 0.01745 6.448 6.466 269.7 910.0 1179.7 0.4372 1.1979 1.6351 300 310 77.67 0.01755 5.609 5.62 6 280.0 902.5 1182.5 0.4506 1.1726 1.6232 310 220 89.64 0.01766 4.896 4.914 290.4 894.8 1185.2 0.4640 1.1477 1.6116 320 l

340 117.99 0.01787 3.770 3.788 311.3 878.8 1190.1 0.4902 1.0990 1.5892 340 l

360 153.01 0.01811 2.939 2.957 332.3 862.1 1194.4 0.5161 1.0517 1.5678 360 l

380 195.73 0.01836 2.317 2.335 353.6 844.5 1198.0 0.5416 1.0057 1.5473 380 l

400 247.26 0.01864 1.8444 1.8630 375.1 825.9 1201.0 0.5667 0.9607 1.5274 400 420 30S.78 0.01894 1.4808 1.4997 396.9 806.2 1203.1 0.5915 0.9165 1.5080 420 440 381.54 0.01926 1.1976 1.2169 419.0 785.4 1204.4 0.6161 0.8729 1.4890 440 460 466.9 0.0196 0.9746 0.9942 441.5 763.2 1204.8 0.6405 0.8299 1.4704 460 460 566.2 0.0200 0.7972 0.8172 464.5 739.5 1204.1 0.6648 0.7871 1.4516 480 l

500 680.9 0.0204 0.6545 0.6749 487.9 714.3 1202.2 0.6890 0.7443 1.4333 500 520 812.5 0.0209 0.5386 0.5596 512.0 687.0 1199.0 0.7133 0.7013 1.4146 520 540 962.8 0.0215 0.4437 04651 536 8 657.5 1194.3 0.7378 0.6577 1.3954 540 560 1133.4 0.0221 0.3651 0.3871 562.4 625.3 1187.7 0.7625 0.6132 1.3757 560 5B0 1326.2 0.0228 0.2994 0.3222 589.1 589.9 1179.0 0.7876 0.5673 1.3550 580 600 1543.2 0.0236 0.2438 0.2675 617.1 550.6 1167.7 08134 0.5196 1.3330 G00

$20 1786.9 0.0247 0.1962 0.2208 646.9 506.3 1153.2 0.8403 046S9 1.3092 620 640 2059 9 0.0260 0.1543 0.1802 679.1 454.6 1133.7 0.8656 0.4134 1.2821 640 660 2365.7 0 0277 0.1166 0 1443 714.9 392.1 1107.0 0.8995 0.3502 1.2498 660 660 2708.6 0 0304 0.0808 01112 758 5 310.1 1068.5 0.9365 0.2720 1.2086 680 700 3094.3 0 0366 0.0386 0 0752 822.4 172.7 995 2 0.9901 0.1490 1.1390 700 705.5 3208.2 0.0508 0

0.0508 906.0 0

506 0 1.0612 0

1.0612 705.5 TABLE A.2 PROPERTIES OF SATURATED STEAM AND SATURATED WATER (TEMPERATURE)

A.3

Volume, f t'/it>

Enthalpy, Stu/lb Entropy. Stubb a F Energy, StW/lb

,s Water Evap Steam Water Evep Ste:m Water (vap Steam Water Steam 3yP S.

h, h,

g q

s, o

g g

y, s

s h

t er

's g

V V

0.0486 32.018 0.01602 3302.4 3302.4 0.00 1075.5 1075 5 0

2 1872 2.1872 0

1021.3 0.0886 0.10 35.023 0.01602 2945.5 2945.5 3 03 1073.8 1076.8 0 0061 2.1705 2.1766 3 23 1022.3 0.10 0.15 45.453 0.01602 2004.7 2004.7 13.50 1067.9 1081 4 0 0271 2.1140 2.1411 13.50 1025.7 0.15 0.20 53.160 0.01603 1526.3 1526.3 21.22 10615 1084.7 0.0422 2.07?B 2.1160 21.22 1028 3 0.20 0.30 64.484 0 01604 1039.7 1039.7 32.54 1057.1 1089.7 0.0641 2 016S 2.0809 3 2.54 1032 0 0.30 1 0.40 72.869 0.01606 792.0 792.1 40.92 1052.4 1093 3 0.0799 1.9762 2.0562 40.92 1034.7 0.40 0.5 79.586 0 01607 641.5 641.5 47.62 1048 6 1096.3 0 0925 1.9446 2.0370 47.62 1036.9 0.5 0.6 85.218 0.01609 540.0 540.1 53.25 1045 5 1098.7 0.1028 1.9186 2.0215 53.24 1038.7 0.6 0.7 90 09 0.01610 466.93 466 94 58 10 1042 7 11008 0.3 1.8966 2.0083 58.10 1040.3 0.7 0.8 94.38 0.01611 411.67 411.69 62.39 1040.3 1102.6 0.1117 1.8775 1.9970 6239 1041.7 0.8 0.9 98.24 0.01612 368.41 368.43 66.24 1038.1 1104.3 0.1264 1.8606 1.9870 66.24 1042.9 0.9 1.0 101.74 0.01614 333.59 333 60 69.73 1036.1 1105 8 0.1326 13455 1.9781 69.73 1044.1 3.0 2.0 126.07 0.01623 173.74 173.76 94.03 1022.1 1116.2 0.1750 1.7450 1.9200 94A3 1051 A 2.0 3.0 141 47 0.01630 118.71 118.73 109.42 1013.2 1122.6 0.2009 1.6854 1.8864 109.41 1056.7 3.0 4.0 152.96 0.01636 90 63 90.64 120.92 1006.4 1127.3 0.2199 1.6428 1.8626 120.90 1060.2 4.0 5.0 162.24 0.01641 73.515 73.53 130 20 1000.9 1131.1 0.2349 1.6094 13443 130.18 1063.1 5.0 6.0 170.05 0.01645 61.967 61.98 138 03 996.2 1134.2 0 2474 1.5820 1A294 138.01 1065.4' 6.0 7.0 176 84 0.01649 53 634 53 65 144 83 992.1 1136 9 02581 1.5587 1.8168 144.81 1067.4 7.0 _

8.0 182.86 0.01653 47.328 47.35 150.87 988.5 1139 3 0 2676 1.5384 1.8060 15034 1069.2 8.0 9.0 188.27 0 01656 42.385 42.40 156.30 985.1 1141.4 0.2760 1.5204 1.7964 156.28 1070.8 94 to 193.21 0.01659 38.404 38 42 161.26 982.1 1143.3 0.2836 1.5043 1.7879 161.23 1072.3 10 14.696 212.00-0.01672 26.782 26 80 180.17 970.3 1150.5 0.3121 1.4447 1.7568 180.12 1077.6 34.696 15 213.03 0.01673 26.274 26.29 181.21 969.7 1150.9 0.3137 1.4415 1.7552 181.16 1077.9 15 20 227.96 0.01683 20.070 20 087 196.27 960.1 1156.3 0.3358 1.3962 1.7320 19621 1082.0 20 30 250.34 0.01701 13.7266 13 744 218.9 945.2 1164.1 0.3682 1.3313 1.6995 2183 1087.9 30 40 267.25 0 01715 10 4794 10.497 236.1 933 6 1169.8 0.3921 1.2844 1.6765 2360 1092.1 40 50 281.02 0.01727 8.4967 8.514 250.2 923.9 1174.1 0.4112 1.2474 1.6585 250.1 1095.3 50 60 292.71 0.01738 7.1562 7.174 262.2 915 4 1177.6 0.4273 1.2167 1.6440 262.0 1098.0 60 70 302.93 0.01748 6.1875 6.205 272.7 907.8 1180.6 0 4411 1.1905 1.6316 272.5 1100.2 70 80 312.04 0.01757 5 4536 5 471 232.1 900.9 1183.1 04534 1.1675 1.6208 281.9 1102.1 to 90 320.28 0.01766 4.8777 4.895 290.7 894.6 1185.3 0.4643 1.1470 1.6113 290.4 1103.7 90 100 327.82 0.01774 4.4133 4.431 298.5 888.6 1187.2 04743 1.1284 1.6027 298.2 1105.2 100 120 341.27 0.01789 3 7097 3 728 312.6 877.8 11904 0 4919 1.0960 1.5879 312.2 1107.6 120 140 353 04 0 01803 3.2010 3 219 325.0 868.0 1193 0 0.5071 1.0681 1.5752 324.5 1109.6 140 160 363 55 0 01815 2.E155 7834 336.1 859.0 1195.1 0.5205 1.0435 1.5641 335.5 1111.2 160 180 373 08 0 01827 2.5129 2.531 346.2 850.7 1196.9 05328 1 0215 1.5543 345.6 1112.5 180 200 351 80 0 01829 2.26S9 2.287 355.5 842.8 1198.3 0 5438 1.0016 1.5454 354A 1113.7 200 250 40097 0 01865 1.8245 1.8432 376.1 825 0 1201.1 0 5679 09585 1.5264 3753 1115.8 250 300 417 35 0 01859 1.523B 1.5427 394 0 808.9 1202.9 0.5S82 0.9223 1.5105 392.9 1117.2 300 350 411.73 001913 1.3064 1.3255 409.8 794 2 1204 0 0 60L! 0 89M 1.4968 4066 1118 1 350 400 444 60 0.0193 1.14162 1.1610 424.2 760 4 1204 6 06217 0 8630 1.4547 422.7 111E 7 400 450 4b6 28 0 0195 1.01224 1.0318 437.3 767.5 1204.8 0.6360 0.8378 1.4738 435.7 1118.9 450 500 467.01 0 0199 0 90787 0 9276 449.5 755.1 1204.7 0.6490 0 8148 1.4639 447.7 1118.8 500 550 476 94 0 0199 0 82183 0.8418 460.9 743.3 1204 3 0.6611 07936 1.4547 4 56.9 1118 6 550 400 486.20 0 0201 0.74962 0.7698 471.7 732.0 1203 7 0.6723 0.7738 1.4461 469.5 111E. 2 600 700

.503 08 0.0205 0 63505 0.6556 491.6 710.2 1201.8 0 6928 07377 1.4304 488.9 1116.9 700 800 518 21 0 0209 0.54809 0.5690 509.8 689 6 1199 4 0.7111 0.7051 1.4163 506 7 1115.2 500 900 13! 95 0 0212 0 4796S 0 5009 526 7 669 7 1196 4 0 7279 0 6753 1 4032 523 2 1113 0 900 1000 544.LB 0 0216 0 42435 0 4460 542.6 (50 4 1192.9 0.74 3t. 0 6476 1.3910 5306 1110.4 1000

!!00 556 2d 00220 0 378f-3 04005 557.5 631.5 11891 07578 06216 1.3794 553 1 110/.5 1100 1200

~,7.19 0 0223 0 34013 0.362b 571.9 613 0 1184 8 07714 05969 1.36S3 556 9 1104.3 1200 1300 57742 0 0227 030722 0.3299 585 6 544.6 1180 2 0.7843 05733 1.3577 5801 1100 9 1300 1400 537 07 0 0231 0 27871 0 3018 59B B 576 5 1175 3 0 7966 05507 1.3474 592.9 1097.1 1400 1500 5 % 20 0 0235 02b372 0.2772 611.7 550 4 1170 1 080E5 05253 1.3373 605 2 1093.1 1500 2000 625 80 0 0257 016260 0 1883 6721 465 2 1133 3 0 86M 04256 1.7b81 f,62 6 1003 6 2000 2500 66d 11 0 02c.f-0 10209 01307 731 7 3616 1093 3 0 9139 03206 1.2345 71B 5 1032.9 2500 3000 695 33 0 0343 0 050/3 0 0850 801 8 2184 1070 3 0 9728 0 1891 1.1619 182 2 973.1 3000 3298.2 10147 0 0508 0

0 050d 906 0 0

9060 1.0612 0

1.0612 875 9 875 9 3708.8 TABLE A.3 PROPERTIES OF SATURATED STEAM AND SATURATED WATER (PRESSURE)

A.4

TempM81m f O'

Aln prm.

(

g, p) 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 e 0.0161 3925 452.3 liI 9 571.5 631.1 690.7 3

6 68 00 1 ISO 2 1195.7 124 a.e 1288 6 13361 1384 5 (101.74) s 0.1295 2 0509 2.1152 2.1722 2.2237 2.2708 2.3144 e 0.0161 78 14 90 24 102 24 114.21 126 15 138 08 150 01 761 94 173 86 185 78 197.70 209 62 22 6

6 68 01 1143.6 11448 1241.3 1788 2 1335 9 1384 3 1433 6 1483 7 1534.7 1586 7 1639 6 1693 3 (162.24) s 0.1295 1.8716 1.9369 1 9943 2.0460 2.0932 2 1369 2.1776 2 2159 2 2521 2.2866 2.3194 2.3509 e

0 0161 38 84 44 95 51 03 57.04 63 03 69 00 74 98 80 94 86 91 92 87 98.84 104 80 110.76 116 72 10 6

68 02 1146 6 1193 7 1240 6 1787.8 13355 13840 1433 4 14835 1534 6 1586 6 1639 5 1693.3 (192.21) s 0.1295 1.7928 1.8593 1.9173 1.9692 2.0166 2.0603 2.1011 2 1394 2.1757 2.2101 2.2430 2.274 v

0.0161 0.0166 29 899 33 963 37.985 41.986 45.978 49964 53 946 57.926 61.905 65 882 69858 73.83 15 6

68 04 168 09 1192 5 1239 9 1287.3 1335 2 1383.8 1433 2 1483 4 15345 1586 5 1639 4 1693.2 17 (213.03) s 0 1295 0.2940 1.8134 1.8720 1.9242 1.9717 2.0155 2.0563 2.0946 2 1309 2.1653 2.1982 2 2297 2.2 e

0.0161 0.0166 22.356 25 428 28 457 31 466 34 465 37.458 40 447 43 435 46 420 49 405 52.388 to 6

68.05 168 11 1191.4 1239.2 1286 9 1334.9 13835 1432 9 1483.2 1534.3 1586.3 1639.3 1693.1 (227.96) s 0.1295 0.2940 1.7805 1A397 1.8921 1.9397 1.9836 2.0244 2 0628 2.0991 2.1336 2.1665 2.1979 2 v

0.0161 0 0166 11.035 12.624 14.165 15 685 17.195 18.699 20 199 21.697 23 194 24 689 26.183 40 6

68 10 168 15 1186 6 1236 4 1285.0 1333 6 1382.5 1432 1 1482.5 1533.7 1585.8 1638.8 1992 7 1 (267.25) s 0.1295 0 2940 1.6992 1.7608 1.8143 1.8624 1.9065 1.9476 1.9860 2.0224 2.0569 2.0899 2.1224 e

0.0161 0.0156 7.257 8 354 9 400 10.425 11 438 12.446 13.450 14 452 15.452 16.450 17.448 18.445 60 6

68.15 168 20 1181 6 1233.5 1283.2 1332.3 1381.5 1431.3 1481.8 1533 2 1585.3 1638 4 1692.4 174 (292.71) s 0.1295 0.2939 1.6492 1.7134 1.7681 1.8168 1E612 1.9024 1.9410 1.9774 2.0120 2.0450 2.0765 2.1 0.01'61 0.0166 0.0175 6 218 7.018 7.794 8.560 9 319 10.075 to 829 11.581 12.331 13.081 13.829 14.577 80 6

68 21 168.24 269.74 1230.5 1281.3 1330.9 1380 5 1430.5 1481.1 1532 6 1584.9 1638.0 1692.0 1746A 18) e (312.04) s 0.1295 0.2939 0.4371 1 6790 1.7349 1.7842 1.8289 1.8702 1.9089 1.9454 1.9800 2.0131 2.0446 2.0750 2

)

=

0.0161 0.0166 0 0175 4 935 5.588 6.216 6.833 7.443 8 050 8 655 9258 9360 10.460 11.060 11.659 100 6 68.26 168.29 269 77 1727.4 1279.3 1329 6 1379.5 1429.7 1480 4 1532.0 1584 4 1637.6 1691.6 1746.5 1802 (327.82) s 0.1295 0.2939 04371 1.6516 1.7068 1.7586 13036 12451 1.8839 1.9205 1.9552 1.9883 2JD199 2.0502 2.079 e

0 0161 0 0166 0 0175 4 0786 4.6341 5 1637 5 6831 6.1929 6.7006 7.2060 7.7096 8.2119 8.7130 9.2134 9.713 120 A 68.31 168 33 269 81 1224.1 1277.4 13281 1378 4 1428 8 1479.8 1531.4 1583.9 1637.1 1691.3 17462 1802D (341.27) s 0.1295 02939 04371 1.6286 1.6872 1.7376 1.7829 12246 1.8635 1.9001 1.9349 1.9680 1.9996 2.0300 2.059 v

00161 0 0166 0 0175 3 4651 3 9526 4 4119 4.8585 5.2995 5.7364 6 1709 6.6036 7.0349 7.4652 72946 8.323 140 6 68 37 168 38 269 85 1220 8 1275.3 1326 8 1377.4 14280 1479.1 1530 8 1583 4 1636.7 1690.9 1745.9 1801.

(353 041 s 0 1295 0 2939 0 4370 1.6085 1.6686 1.7196 1.7652 1.8071 13461 1.8828 1.9176 1.9508 1.9625 2.0129 2.042 e

0 0161 0 0166 0 0175 3 0060 3 4413 3 8480 4.2420 4 6295 5.0132 5 3945 5.7741 6 1522 6 5293 '6 9055 7.281 160 4 68 42 168 42 269.89, 1217 4 1273 3 1325 4 1376 4 1827.2 1478 4 1530.3 1582.9 1636.3 1690.5 1745.6 1801.4 (363 55) s 0 1294 0 2938 0 4370 l 1.5906 1 6522 1.7039 1.7499 1.7919 1 8310 1.8678 1.9027 1.9359 1.9676 1.9980 2.027 e

0 0161 0 0166 0 0174 2 6474 3 0433 3 4093 3.7621 4.1064 4.4505 4.7907 5.1289 5.4657 5A014 6.1363 6.470 180 6 68 47 16647 269 9/

1213 8 1271.2 1324 0 1375.3 1426 3 1477.7 1529 7 1582.4 1635.9 1640 2 1745.3 1801 (373.C81 :

C 1294 0.2938 04370 1 5743 1.6376 1.6900 1 7362 1.7784 1.8176 1.8345 13894 1.9227 1.9545 1.9849 2.014 0 01f1 0 0166 0 0174 2 3598 2.7247 3.0583 3 3783 3 6915 4 0008 4.3077 4.6128 4.9165 52191 5.5209 5.821 i

200 6 6812 168 51 269 96 1210 1 1269.0 1322f 1374.3 1425 5 1477.0 15291 1581.9 1635 4 1689.8 1745.0 1800 J (13140) s 0 1294 0 2938 0 4359 1.5593 1.6242 1.6776 1.7239 1.7663 1.8057 1 8426 1A776 1.9109 1.9427 1.9732 2.00 0 0161 0 0166 0 0174 0 0186 2.1504 2 4662 2.6872 2.9410 3 1909 3.4382 3.6837 3 9278 4 1709 4.4131 4.6546 250 h 68 66 168 63 270 05 3/5.10 1263.5 1319 0 1371 6 1423 4 1475 3 1527.6 1580.6 1634.4 1688.9 1744.2 1800.2 i

e (400 97) :

0 1294 0 2937 0 4368 0 % 67 1.5951 1.6502 1.6976 1.7405 1.7601 18173 1.8524 1.8658 1.9177 1.9482 1.9776 v

00161 0 01E 5 0 0174 0 0186 1.76 % 2 0044 2 2263 2.4407 2 6509 2 65S5 3 0643 3.2688 3 4721 3 6746 3 8764 300 e 68 79 1 % 74 ? ?u 14 375.15 1257 7 1315 2 1368 9 1421.3 1473 6 1526.2 1579 4 1633 3 16880 1743 4 1799.6 (417.35) s 0.1294 02937 04337 0 % 65 1.5703 1.6274 1.6758 1.7192 1 7591 1.7964 1.8317 1.8652 1 8972 1.9278 1.957 e

0 0161 0 0166 0 0174 0 0186 1.4913 1.7028 1.8970 2 0332 2 2652 2 4445 2 6219 2.7980 2.9730 3.1471 3.3205 350 6 68 92 16B85 270 24 375 21 1251 5 13114 1366 2 1419 2 14718 1524 7 1578 2 1632.3 127.1 1742.6 1798 9 (431.73)

  • 01293 029 % 04367 0 568,4 1.5483 1 6077 1.6571 1.7009 1.7411 1 7787 1 8141 1.8477 12795 1.9405 1.9400 e

0 0161 0 0166 0 0174 0 0162 12841 14763 1 6493 18151 19759 ? 1339 2.2901 2.4450 2 5957 2.7515 2.9037 400 a 69 05 16897 270 33 375 27 12451 1307 4 1363 4 1417 0 14701 1523 3 1576 9 1631.2 1636 2 1741 9 1793 2 (444 60) s 01293 0 2935 0 4366 0 5663 1.5282 1 5901. 16406 16850 1725$ 17632 1.7988 1.8325 IS647 1.8955 1.9250 e

0 0161 0 0166 0 0174 0 0186 0 9919 1.1584 1 3037 1.4397 1.5708 1 6992 1.8256 1.9507 2.0746 2 1977 2.3200 500 6 69 32 1 % 14 270 51 375 38 12312 1299 1 1357.7 1412 7 1466 6 1520 3 1574 4 1629 1 1684 4 1740 3 1796.9 (457.01) s 0 1292 0 2934 0 4364 Obt00 1 4971 1 % 95 1 6123 1 65/8 16990 1.7371 1.7730 1.8069 18393 1.8702 1.8908 I

TABLE A.4 PROPERTIES OF SUPERHEATED STEAM AND COMPRESSED WATER (TEMPERATURE AND PRESSURE)

A.5

.c 5 Abs press.

DmPostm,F

...t

, 16M U (ut.nemp) 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 v

00161 0 01 % 0 0174 0 0186 0 7944 0.94 % 10726 1.1892 1.3008 14093 1.5160 1 6711 13252 18284 1.9309 600 6 69.58 169 42 270 70 37h 49 1215 9 1290 3 1351.8 14083 1463 0 1517.4 1571 9 1677.0 1682 6 17388 1795 6 (48620) s 0.1292 02933 0 4362 0.%b7 14590 1.5329 1.5844 163bl 1 6769 133 % 17517 13859 8.8184 1 8494 1.8792 e

0 0161 0 0166 0 0174 0 0186 0 0204 0 7928 0.9072 1.0102 1.1078 12023 1 2948 1.3858 14757 1 % 47 3.6530 700 6 69 04 169.65 270 89 375 61 487 93 1281 0 1345 6 14033 14b9 4 1514 4 15694 1624 8 16b07 1737 2 1794 3 (503.08) s 0.1291 0.2932 0.4 %0 0 % 55 0 6889 1.5090 3. % 73 1 6154 1.6580 1.6970 1 7335 1.7679 1800b 1 8318 1 8617 e

0 0161 0 0166 0 0174 0 0186 0 0704 0.6774 0 7825 0.8759 0 % 31 I N70 1.1289 1.2093 12835 13669 1.4446 800 6 70.11 169 88 271.07 375 73 487.88 1271.1 13392 1399.1 1455 8 1511 4 1566 9 1622 7 1678 9 1735 0 1792.9 (5182.) s 0.1290 02930 0.43b8 0 5052 0 6885 1.4869 1.5484 1.%B0 1.6413 16807 1.7175 13522 1.7851 1 8164 1.8464 e

00161 0.0166 0 0174 0 0186 0 0204 0 5869 0 6858 0 7713 0 8504 0.9262 0 9998 1.0720 1.1430 1.2131 12825 000 6 70.37 170.10 271.26 375.84 487.83 1260 6 1332.7 1394 4 1452.2 1508 5 1564 4 1620 6 1677.1 17341 1793.6 (551.95) a 01290 0.2929 0 4357 0 % 49 0.6881 1A659 1.5311 1.5822 1.6263 L6662 1.7033 1.7382 1.7713 1.6028 1.8329 e

0.0161 0 0166 0.0174 0 0186 0 0204 0 5137 0 6080 0 6875 0.7603 0 8295 0.8966 0 % 22 1.0766 1.0901 1.1529 1000 6 70.63 170.33 271.44 375.96 487.79 1249.3 1325 9 1389.6 1448 5 1504.4 1561.9 1618 4 1675.3 1732 5 1790 3 (544.58) s 0.1269 0.2928 0.4355 0. % 47 0.6876 1.4457 1.5149 1.5677 1.6126 16530 1.6905 13256 13589 1.7905 1 8207 e

0.0161 0 01 % 0 0174 0.0185 0.0203 0 4531 0 5440 0 6188 0 6865 0 7505 0 8121 08723 0 9313 0 9894 1.0468 1100 6 70 90 170.56 271.63 376 08 487.75 1237.3 1318 8 1384 7 1444.7 1502 4 1559.4 1616 3 1673.5 1731.0 1789 0

($b628) s 0.1269 02927 0 4353 0 5644 0 6872 1.4259 1.4996 1.5542 1.6000 1.6410 1.6787 13141 1.7475 1.7793 1.809,7 s

0 0161 0 0166 0.0174 0.0185 0 0203 0 4016 0 4905 0.5615 0 6250 0 6885 0 7418 CJ974 0 85!9 0.9055 0 9584 1200 6 71.16 170.78 271.82 376 20 487.72 1224.2 1311.5 13793 1440 9 1449 4 1556 9 1614.2 1671.6 17294 1787.6 (567.19) s 0.1288 0.2926 0.4351 0.5642 0.6868 1.4061 1.4S51 1.5415 1.5883 1.6298 16679 1.7035 1.7371 1.7691 1.7996 e

0.0181 0 0166 0 0174 0 0185 0 0203 0.3176 0.4059 0 4712 0 5282 0 5809 0 6311 0 6798 0 7272 0.7737 0 8195 1400 6 71.68 171.24 272.19 376 44 487.65 1194.1 12961 1369.3 1433 2 1493 2 1551 8 1609 9 1668 0 1726.3 1785.0 (587.07) s 0.1287 02923 0.4348 0.5636 0.6859 1.3652 1.4575 1.5182 1.5670 1.6036 1.6484 1.6845 1.7185 1.7508 1.7815 e

0.0161 0.0166 0.0173 0.0185 0 0202 0.0236 0.3415 0 4032 0 4555 0.5031 0 5482 0 5915 0 6336 0.6748 0.7153 1600 6 72.21 171.69 272.57 376 69 487.60 61637 1279.4 1358 5 1425.2 1486 9 1546 6 1605 6 1664.3 1723.2 1782.3 (604.87) s 0 1266 0 2921 0.4344 0.5631 0.6851 0.8129 1.4312 1.4965 1.5478 1.5916 1.6312 1.6678 1.7022 1.7344 1.7657 e

0.0160 0.0165 0 0173 0.0185 0.0202 0.0235 02906 0 3500 0.3988 0 4426 0.4836 0.5229 0.5609 0.5980 0 6?43 1800 a 72.73 172.15 272.95 376 93 487.56 615.58 1261.1 1347.2 1417.1 1480 6 1541.1 1601.2 16603 1720.1 1779.7 (621.02) s 0.1284 02918 0.4341 0 5626 0.68t3 0 8109 1.4054 1 A768 1.5302 1.5753 1.6156 1.6528 1.6876 1.7204 1.7516 e

0 0160 0.0165 0 0173 0 0184 0.0201 0 0233 0.2488 0.3072 0.3534 0.3942 0 4320 0.4680 0.5027 0.5365 0.5695 2000 6 73.26 172.60 273.32 377.19 487.53 614.48 1240.9 1353 4 14083 1447.1 1536.2 1596.9 1657.0 1717.0 1777.1 (635 80) s 0.1263 0.2916 0 4337 0 % 21 0 6834 0.8091 1.3794 1.4578 1.5138 1.5603 1.6014 1.6391 1.6743 1.7075 1.7389 e

0.0160 0 0165 0.0173 0.0184 0.0200 0.0230 0.1681 0 2293 01712 0.3068 0.3390 0.3692 0.3980 0 4259 0 1529 2500 6 74 57 173.74 274.27 377.82 487.50 612 08 1176.7 1303 4 13863 1457.5 1522.9 1585.9 1647.8 1709.2 17704 (668.11) s 0.1280 0.2910 0.4329 0 5609 0.6815 0 8048 1.3076 1.4129 1.4766 1.5269 1.5703 1.6094 1.6456 1.6796 1.7116 e

0 0160 0.0165 0.0172 0 0183 0 0200 0.0228 0 0982 0175$ 0.2161 0.2484 0.2770 0.3033 0.3282 0.3522 0.3753 3000 6 75 83 17e68 27522 378 47 487.52 610.08 10605 1267.0 13632 14402 1503.4 1574.8 1635 5 1701.4 17(1.8 (f 95.33) s 0.1277 0.2904 0.4320 0.5597 0.6796 0 8009 1.1966 1.3692 1.4429 1.4976 1.5434 1.5841 1421d 1.0561 1.6688 e

0.0160 0 0165 0.0172 0.0183 0.0199 0.0227 0.0335 0.1588 0.1987 0.2301 0.2576 0.2827 0.3065 0.3291 0.3510 3200 6 76.4 175,3 2756 378 7 487.5 609 4 800.8 1250 9 1353 4 1433.1 1503.8 1570.3 1634a 1698.3 1761.2 905te) s 0.1276 0.2902 0.4317 0.5592 0.6768 03994 0.9708 1.3515 1.4300 14866 1.5335 1.5749 14126 1.6477 14806 e

0.0160 0 0164 0 4172 0.0183 0 0199 0 0225 0.0307 0.1364 0.1764 0.2066 0 2326 0.2563 0.2784 02995 0.319P.

3500 6 77.2 176.0 276.2 3 79.1 487.6 608 4' 7794 1724 6 1338.2 1422 2 1495 5 1%3.3 16292 1693 6 17b7.2 s

0.1274 02899 0 4312 0 5585 0 6777 03973 0 9508 1.3242 1.4112 1.4709 1.5194 1.5618 1.6002 1.6353 1.6691 e

00159 0.0164 0 0172 0.0182 0 0198 0 0223 0 0287 0 1052 0 1463 0.1752 0 1994 0 22 to 0 2411 0 2601 0 2783 4000 6 78.5 1772 277.1 379.8 487.7 6065 763 0 1174.3 1311.6 34030 1481.3 1552.2 1619.8 16S5 7 1750 6 s

0 1271 0.2993 0.4304 0 5573 0 6760 0 7940 0 9343 1.2754 1.3807 1.4461 1.4970 1.5437 1.5812 1.6177 1.6516 e

0 0159 0.0164 0 0171 0 0181 0.01 % 0 0219 0.0268 0.0591 0.1038 0.1312 0 1529 0 1718 01660 0 2050 02203 l 5000 t 81 1.179 5 2791 381.2 488.1 604 6 746 0 1042 9 1252.9 13C46 1852.1 1529.1 16009 1670 0 1737.4 s

0.1265 0.2861 0 4287 0.5550 0 6726 03880 0 9153 1.1593 1.3207 1.4001 1.4582 1.5061

1. 9 81 1.5663 14216,

1 e

0 0154 0 0163 0 0170 0 0160 0 0195 0 0216 0 0256 0.0397 0 0757 0.1020 0.1221 0.1391 0.1544 0.16B4 0 1817 6000 6 63J l81 3 281.0 382 7 #86 602 9 7361 9451 1168.8 1323 6 1422 3 1505 9 1%20 1654 2 17241 s

01258 0.2670 0 4271 0 5528 0 6693 0 7826 0 9026 1.0176 1.2615 1.35'4 1.4229 1.4745 1.5194 1.5593 1596.2 l l

e 0.0158 0.0163 0 0170 0 0180 0 0193 0 0213 0 0248 0 0334 0 0573 0 03M 0 1004 0.1160 0 1298 0 1424 0.1542 7000 6 86.2 184 4 283 0 384 2 489 3 601 7 729 3 901.8 1124.9 1281 7 1392 2 3482.6 15631 1639 6 1711.1 8

0 1252 0 2859 0 4256 0 5'i07 06563 0 7/77 08926 10350 12055 1.3 D 1 13904 1.44u6 14938 1.53' $ 1.5735 TABLE A.4 PROPERTIES OF SUPERHEATED STEAM AND COMPRESSED WATER (TEMPERATURE AND PRESSURE) (CONTINUED)

A.6

v.;

v.

g.,

r4..JL.,'.',"Uf,p

'f u

o

.m o

a.

'~

7 Ni h, fb<yW I N // M i

'~

xi

~

i n

j 1

gf;ygA / N///T i

n i

ai t

ni i n i.

i.,

/f7]/Q\\/ N ///W n

ii w

i a,

/}lQg

/ N ///%j

$gbDU7 jyhk?*

/Rany;byg f.

'~

.~

//) sg 1290 N

/

7%4fyy?/

V I 1200 1300 my'

/n&[

!!SO fBW MK73

/

.- MA6W,5g//

.- AfMNMn //

MXWAYx/

~

V,'Mk % W E$0

/

\\

3d 15 1.6 gy ED 2.L pg

,jb3

. Entropy, stu /lb, F FIGURE A.5 MOLLIER ENTHALPY-ENTROPY DIAGRAM A.7

i s.s a

PROPEH71ES OF WATER Denslly e (Ibsift8)

P8IA Temp Soluteted

(*F)

Liquid 1000 2000 2100 2200 2300 2400 2500 3000 32 62.414 62.637 62.846 62.867 62.888 62.909 62.93 62.951 63.056 50 62.38 62.55 62.75 62.774 62.798 62.622 62.846 62.87 62.99 100 61.989 62.185 62.371 62.390 62.409 62.427 62.446 62.465

' 62.559 200 60.118 60.314 60.511 60.53 60.549 60.568 60.587 60.606 60.702 300 57.310 57.537 57.767 67.79 57.813 57.836 57.859 57.882 57398 400 53.651 53.903 54.218 54.249' 54.28 54.311 54.342 54.373

' 54.529 410 53.248 63.475 63.79 53.825 53.86 53A9 53.925- ' 53.95.

64.11 420 52.798 53.025 53.36 53.40 63.425 53.46 63.50 53.53 53A9 430 52.356 52.575-52.925 52.95 52.99 53.02 53.065 53.09 53.265 440

$1.921 52.125 52.42 52.45 52.475 62.51 52.54 52.56 52.275 450 51.546 51.66 52.025 62.065 62.10 62.14 52.175 52.21 52.41 460 51.020

$1.175 51.56 51.61 61.64 51.68 51.725

~ 51.76.

51.96 50.505 60.70 51.1 51.14 51.175' 51.22 51.25

' 61.30 61.50 480 50.00 60.20 60.62 60.66 60.7 60.74 60.78

' 60.825 51.035 470 490 49.505 49.685 60.13 60.175 60.22 60.265 60.31 60.35 60 575 500 48.943 49.097 49.618 49.666 49.714 49.762 49.81 49.KA 60.098-510 48.31 48.51 49.05 49.101 49.152 49.203' 49.254 -

49.305 49.56 520 47.85 47.91 48.46 48.515 48.57 48.625 48.68 48.735 49.01 530 47.17 47.29 47.86 47.919 47.978 48.037' 48.096 48.155 48.45 540 46.51 47.23 47.296 47.362 47.428 47.494 47.56 47A9 550 45.87 46.59 46.658 46.726 46.794 46.862 46.93 47.27 560 45.25 45.92 45.994 46.068-46.142 46.216 46.29-46.66 570 44.64 45.22 45.30 45.38 45.46 45.54 45.62 46.02 580 43.66 44.50 44.586 44.672 44.758 44.844-44.93 45.36 590 43.10 43.73 43.825 43.92 44.015 44.11 44.205 44.68 600 42.321 42.913 43.017 43.122.

43.226 43.33 43.434 43.956 610 41.49 41.96 42.08 42.196 42.314 42.432 42.55 43.14 620 40.552 40.950 41.083 41.217 41.35 41.483 41.616 42.283 41.44 630 39.53 40.388 '

640 38 491 39.26 650 37.31 38.000 660 36.01

'36.52 670 34.48 34.638 683 32.744 32.144 690 30.516 TABLE A.6 PROPERTIES OF WATER, DENSITY A.8

_1_.,_.. P._ R_.. _I N d_.I. P._L_E. S_.

O_ F._ N U_C L E.. A._R_. _P O._ W_E__ R _ P_.L_ A.N_ T_ _.O.P_E R A_T._._I O N.. s FAGE 6-(f

.a 1.

J. _ z

. b.

'2

=.

' ANSWERS - BROWNS FERRY 1,

2 t<3

-87/11/16-PAYNE, C.

1 ANSWER 1.01 (1.00) d REFERENCE Steam Tables GE Heat Transfer, Chap.

3, LD 5 BFNP: Steam Tables LP, p.

8; i

RD B4/02/02 2.5/2.6 2.8/3.1 293003K112 293003K123

...(KA'S) i ANSWER 1.02 (2.00) a.

8 e.

1 b.

^5 4,

7 c.

2 g.

4 d.

5 h.

6 REFERENCE GE Heat Transfer. Chap.

9, LO 1.1.d, 3.1, 3.5, 4.1, 4.5, 5.2, 7.1 3.0/2T.2 2.9/3.0 2.2/2.6 3 4/3.8 3.1/ :5. 7

3. 3 / 3. '7 3.2/3.7 3.1/3.6 293008K109 29000BK110 293009K104

- 293009K.106 293009K109

...(KA'8) s k.

48,0

}

j)<

f.\\

n I

4 1

J 3

k I

s 4

i

]

i

.i I

s

'1.

FRINCIPLES OF* NUCLEAR POWER PLANT _DPERAI,I.gN PAGE 7

t

.:.,JujEB002XUB01ChE01_lBBUSEEB_.692_ELUID_ELOW ANSWERS -- BROWNS FEPRY 1,

28<3

-87/11/16-PAYNE, C.

I l

ANSWER 1.03 (1.50) i 1.

Neutron

-ttlement of the cladding.

I 1

2,.

Thermal 1y iiJuted pel1et growth.

j J

3.

Inward motion of the cl adding walls (creepdown).

4.

Fission Product.2hemical) embrittlement of the clLdding (from Cd/1).

D.

Fi s si on Product gas bu ldup ( p r ess'ur e ).

.,(Any 3 :11 0.5 each) 1 REFERENCE GE Heat Transfer, Chap. 9 LD 7,.1 9/7.1 293009K132

...(KA"5)

ANSWER j.04 (1.50)

(1)

More neutrons will be captured in the resonant peaks of ur ani um and plutonium (0.5) (as the slowing down length increases).

(2)

' - E t-1

,g t h 2,3

~'

'4 THCgLrvths. ACHTlle Ll L.E4LAL,e /AJC/ cggg 5 (0,5) fA' 5r*

l (3)

Neutron leakage increaGes (0.5).

1 A

l REFERENCE GE Reactor T h eo r y., Chap.

1, LO 1.1 l

Chap.

4, LO 3. 3 2.0/2.1 1.9/2.0 2.6/2.7

. 2/7.2 292002K103 292002K104

.2t?2004 K 103 292004K110

...(KA"S)

I 1

-3

_1.~

_P,_R I.._N C.. I.. P. L..E.. S 0. "... N. U.. C.. t.... E, A._ R__. _ P_ O_. W_ E_ R_._ _ P. L_. A_ N..T _ D._ P_E R M... I O,. N.. _.

PAGE fJ e s'!.. H._,C R._ M... O.. D. Y._ N... a ~_l T_ C. S..A.._H.E.._ A_T..T R_ A. N.. S.. F_E R..

A_ N D _ F._ L_ U I_ D.._ F L.. f_A_l ANSWERS - - - E@uuNS FERRY 1., J.: *

--87 /11/16-PiWNE,

E.

ANEWER

1. O 4.1.50?

a The decre we an t Fu. - b u r r i o s.i t t er m

( 0, 6) w1 t b thn p r ted u c t i on of the

enen from decay of iodano still at the h.taher power rate, u m i n a t e ':,

( 0, "..

c etm) no t he nion c onc.en t r at t en to J. n c. r e-w.,,,

b.

F'er a pneral rad a c.< r t h va l i I nt.r e arm (0.23) b E s tum the h1gheit nenan c on t s n t r a t.l on vu l l be in the conter at the cor e where the t?J ghe5#t t i U; e -: 1 n, t e d (0.25).

Thas w111 auppre 2

the f l m, 1o the center of the ccn and i n c r e c. e the flus an the,a r e a of the ptripheral rods, t h er eb y., increas:,ng their worth (0.25).

o c,

t10RE THAN tha]4 ttie,alue e-. t 100%).

( C. l.' S )

REFERENCE GE finac t or

'I h e r r y, (T h a p.

6, L0 2.1,

'.2,

"?. 4 (1 / S. e Q s..

m c? i. / r s,. ( 7) x.r. /+

.s 3.. c, 1/

+

s s."v d%5& 10!

"9 2 00 :A 10 4

.J'CD 06lc 1 kM3 32006K131

.. ( t :N E, )

AM;3 WER 1.00

('.05) a.

ROC)r d1at1On p u m O D.

t t"1 ppi fi t

( E-

-51.5")

b.

MEIU tloc 4re c.

Ef 4 e-ct e of H 'L J c r.d RC]C ci.

Br F;SM i s lau 1, s m 1 c

Hi"C1 e ru.i RC.! C p tmp 1ripr t

>M'e i.

I n c r o

-1 d v o l d i n :1 fcauned a v d e c r e m:,c d cubcooling)

(0.5 each)

PEF EREl lEE EcNP-Op rer a t i o n s ) T r a m i c-1 LP, "I r s o n i en t 49 FD 80/OJ/01 i

4.2/4.6 4.J/4..

4.'/4.*

S50094201 2 E009(: 011 2:C01,10M11

.,.(F.A"9)

(

1. __)F.'BIBglELES,_gE,,00 Ctg 68,,COMiiB_ELGUI..,0CEBOllOM1.

PAGE 9

... lfBO90100 MICE 3EGI_IEGH!iEfiE OND_ELul[LELOW v

ANSWERS -- BROWNS FERRY 1, 2&3

-07/11/16-PAYNE.

C.

i l

AN5WER 1.07

( 1. 50)

CR1(1 - Refil) = CR2(1 - Keff2)

(0.5) i Keif2 = 1 - L (CR1/CR2) (1 - IAff1)J 1 - f_ ( 100 / 2 7 0) ( 1 - 0.95)3 (0.75)

=

- 0.0185

= 0.9815

(+/-

0.002)

(0.2b)

. j 1

REFERENCE GE Reactor Theory, Chap.

1.

L.O 5."

Chap.

3.

L.O 14 2.1/ 2. J.

'.3/3.4 j

292003K102 292008K104

...(IA"5) 1

-1 l

ANSWER 1.08 (2.00) 1 J

Scr arn Set poi nt (118%) (3292 MW) x 388S MW (0,,5)

=

t/T l

Po i e

( 0, 5 )

1 Peak Power c=

1

-l 10 sec/10 sec - 3885 > e 3885 / e (0,5)

=

10 562 MW (or 10.6 GW)

(+/-

100 MW)

( 0., 5 )

=

3 i

REFERENCE GE Reactor Theory, Chap.

3, LO

!.. 2 I

2.7/2.8 l

292003K108

.(KA"S)

~

ql u

l

- 1. _P619 186E@, QE,UQgtEGB_.EOWEB_ELG! I_QEEB@llgN PAGE 10 y

...J15E00DYtJ8t11GS EBI_IBBueEEB_OUQ_ELylD_ELOW t

u ANSWERS -- BROWNS FERRY 1,

2&3

-87/11/16-PAYNE, C.

1 i

ANSWER 1.09

( 2. L/0 )

125.9 BTU /lbm (0.25) 1129.4 BTU /lbm h (in) a.

h(out)

=

=

4 I

1. 0 BTLl/1 tam-deg F c (p)

=

STEAM:

01

-m Ch(out - in

)]-

(0.4) l 6x10E+6 [1129.4 - 125.93 (0.25)

{

l 6.021x10E+9 BTU /hr

(+/- 3. 02: 10E+7)

(0.1)

=

WATER:

m = O2 / Ec(p) x T(out -- in)J (0.4) 1 6.021x10E+9 / E1.0 x (77 - 62)3 (0.25)

=

i

= 4.014x10E+8 lbm/hr

(+/- 2.0x10E+6)

(0.1)

b. Incrutses (O'

RErERENCE GL s%at Trahnfer, Chao. 7 LO 5.2 3

1st t_aw of Thermodynamics Bernoulli's Equa ti on GGNS: OD-FH-504 EIH:

L-RD--6 6 6 1.5/1.6 2.3/2.9 293002K10'7 293007K113

...(KA"B) l l

l i

l l

s

1 _._l'B1!$C 1.PLM OE_.[J99bliOB_,f 0 WEB.lt O[g_. OEEBOH ON PAGE 11

-e.esilgB!$09'GMWJCL_ HEAT TRANSFER AND FLUlO FLOW ANSWERS - CROWNS FERRY 1,

2L3

-87/11/16-PAYNE.

C.

ANSWER 1.10 (1.00)

D20,3 deg F (D.15) a.

800 psig - 814.7 ps1a

=

364.7 p sa a =: 435.5 deg F (0.15) 350 p r>i g

=

C/D = S20.3 - 4T5.S -- 84.8 deg F (0.0b) 60 min /hr (0.10) 84,8 deg F/45 min,

C/D Rate c

-- 113.1 dog F/nr (0,05) b.

App 11rable operat.ianal limit is C/D rate 100 dng F/hr.

(0.25) s If C/D continuen at the prencnt rate (or any rate 60.8 deg F/hr) for en a d d i t i on ea l 15 nu nutes, then limit will be exceeded.

However, ai C/D ir slowed such that at the end af 60 nunutes tne C/D rato i e, 100 deg F/hr, then no operations 1 limi t wilJ have been e:< ceed ed.

(O.2b)

REFERENC E.

Steam Tables L4E Heat Transfer. Chep. ~ ~., L.O 4 Technical Gpeci-f1 cat 1 ann

2. 2 /

29300JKiel (F y 5)

TEST. CROSS REFERENCE-

-PAGE 1

l

' d L.,,

QUEGT60N' VALUE REFERENCE 01.01 1.00 DCP0001419

)

201.02 2;00 DCP0001422" 01.03 1.50 DCP0001420 01.04 1.50 DCP0001414 T01.05 1.50 DCP0001415

.01.'06 3.00 DCP0001424 01.07 1.50 DCP0001416 01.08 2.00 DCP0001418 01.09 2.00-DCP0001421 01.10 1.00 DCP0001423' 17.00 H----nt 17.00 i

-l

'I l

u d

J i

+

{

)

ENCLOSURE 3 REQUALIFICATION PROGRAM EVALUATION REPORT j

Facility:

Browns Ferry Nuclear Plant Examiner:

D. C. Payne Dates of Evaluation:

November 17-18, 1987 Areas Evaluated:

X Written X

Oral Simulator Examination Results:

R0 SR0 Total Evaluation Pass / Fail Pass / Fail Pass / Fail (S. M, or U)

Written Examination 1/0 1/0 S*

Operating Test Oral 1/0 1/0

.S*

Simulator Evaluation of facility written examination grading Overall Program Evaluation Satisfactory X*

Marginal Unsatisfactory (List major deficiency.

areas with brief descriptive comments)

  • Interim evaluation - Final evaluation will be made after completion _of the i

March 1988 examinations.

Progress satisfactory.

I Submi Forwarded:

Approved; WS

./'

YM Whi Y l

Qff/.'

e

f. E. lWoc#ifan C.A.Ju}4an l

......

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