ML19331B916

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Instrument Error Analysis for Fort Calhoun Containment Leak Rate Test:Jan 1980
ML19331B916
Person / Time
Site: Fort Calhoun Omaha Public Power District icon.png
Issue date: 07/11/1980
From: Noland C, Novgrod R, Rowley C
NUCLEAR SERVICES CORP.
To:
Shared Package
ML19331B914 List:
References
NUDOCS 8008130525
Download: ML19331B916 (5)


Text

,

s O

w INSTRUMENT ERROR ANALYSIS FOR FORT CALHOUN CLRT a

January 1980 Prepared for 5

Omana Public Pow'er District 1

By i

Nuclear Services Corporation 2622 E. 21st.' St.

Tulsa, OK 74114 1

(918)749-2582 Prepared _by: R.L. Novgrod C.B.Noland(,,,d-c

. Reviewed by:

C.W. Rowley f

Approved by:

July 11, 1980 OMA-0110 T-8068130 -DD

l ".

v

.l" INSTRUMENT ERROR ANALYSIS I.

Instrumentation A.

Pressure Digital Readout Inst #

PI-1, PI-2 Mfg Mensor Corp.

Type Bourdon Tube Capsule & Precision Pressure Gage Range 0-100 psia Stability i.002 psi I

Repeatability 1 0005 psi Resolution i.001 psi Accuracy i.015 psi 1i B.

Teiaperature Elements Inst #

T-001 through T-030 Mfg 1 Hy-Cal Engrg

.1 Type 100 0 Platium RTD Range Calibrated for 60, 85, and 110 F

. Repeatability &

4 Hysteresis

+ 0.1 F Accuracy

[0.02F C.

Dew Point Measurement System Inst #

DPT-31 through DPT-40 Mfg Volumetrics t

Model Dewcell

~

Range Calibrated for 50, 80, 100 F Accuracy 1 00726 psi Repeatability.

1 002 psi Stability (for threedays) 1 00006 psi F,

H D.

Readout System i.-

Mfg Data logger Model 3000~

accuracy

+.19 F

+.0024 psi repeatability T.05 F T.0006. psi i

stability

[.05F 1 0006 psi

E.

Flow Measurement System Inst #

FI-l Mfg Fisher-Porter Model 087-615-588 Calibration

.4 to 4 scfm of air 0 60 psig & 80 F Accuracy

+ 1% of full scale c-II.

Formula EL = 100

?p{py+2)

+2t py a

~'

where:

E = error in leakage rate in % by weight per day L

E = pressure instrument error po. inst.

j...

p

= error in total absolute pressure in psia E =. temperature instrument error no inst.

T

= error in temperature in 'R Ey = vapor pressure instr 3 ment error no. inst.

= error in water vapor pre-ssure in psia Assuming:

~

~

A.

Initial and final temperatures are identical B.

Initial and final pressures are identical III.

Calculation of Ep (repeatability)2 + (resolution)2 + (stability)2 E

=

p

  1. of senors

(.0005)2 + (.001)2 + (.002)2

=

2 1 6 202 x 10-3 psi

=

1 L-

e f:

1 IV. Calculation of E T (repeatability)2 (repeatability of)2

[ stability of)2 data logger E

f RTD data logger

=

T

  1. sensors

(.1)2 + (.05)2 + (.05)2 30 Q

.02236 F

=

V.

Calculation of Ey

+ (of readoutrepeatability)2, (of readou stability

("E** *ofdetector) + (o*f detector)

Y E

=

V

  1. of sensors

(.002)2 + (.00006)2 + (.0006)2 + (.0006)2 9

J

.00072 psi

=

VI. Calculation of E L

/

py)2

+2(ppy)2 E = 100 2

=2 t

= 100^

2(.00

+2(*0

+2(.00 2)2 2

- 30 6

=.0068% by wt/ day I

i

?

P I

VII. Calculation of E p Standard conditions for the flowmeters are defined as 14.73 psia and 60 F.

FlowmeterAccuracy=I{004'

=.04 scfm Flowmeter Error = E

=P F

60 T

  • 60 x 24 x 100 x.04 T

9-Pv 1.05 x 106 80 l-

, 60 + 14.7 76 + 460 x

x.137 x.04 =.0054 80 + 460 75.107.143 4

VIII. Calculation of r /

1 E'=EL+Ep =.0068 +.0054 =.0122% by wt/ day o

N 2

em k

L m

W W

t

,