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| Arkansas Power & Light ,
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| 2Lrkansas Nuclear One 1 Unit 1 O
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| Primary Reactor Containment Integrated Leakage Rate Test Final Report November 1988 Bechtel Power Company O
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| prs 889 =882gz 1
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| ARKANSAS IWER AND LIGE CIEPANY ARKANSAS NUCIEAR CNE UNIT 1 DOCM E NUMBER 50-313 PRIMARY REACIOR (INIAINMDR INTERATED IEAKAGE RATE TEST NCVEMBER 1988 O
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| Suhnitted to
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| 'Ihe United States Nuclear Regulatory hinaion Pursuant To Facility Operating License Number DPR-51 O
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| 4 TABIE OF CCNTENIS INIRODUCTICN. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1 dC I.
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| II. TEST SYNOPSIS..................................... 2 III. TEST DATA SUPEARY. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3 )
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| IV. ANALYSIS AND INIERPREIATICN. . . . . . . . . . . . . . . . . . . . . . . . 8 V. REFERENCES........................................ 10 APPENDICES A. Bechtel IIRP Ccaputer Preg.c= Sumary B. IIRP Stabilization Summary Data Report C. 9==avy Data Sheets D. IIRT @lafations E. IIRP Plot hwature vs. Time Pressure vs. Time Vapor Pressure vs. Time Air Mass vs. Time Entire Test Period IIRT Period verification Test Period Mass Point Isakage Rate vs. Time Total Time Isakage Rate vs. Time F. Verification Flow Test Summary Data Report G. Verification Flow Test Calculations Mass Point Analysis Tbtal Time Analysis H. Summary Data Sheets I. Type B & C Test Results i
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| I. IlmODUCTICN A mima ==ful Type A Caritainment Integrated Imakage Rate Test
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| . (IIRT) was conducted on the Arkansas Nuclear One, Uhit i l containment between November 8 and November 9, 1988. 'Iha test was perfanned to deumstrate that the cantairunent leakage under prescribed post-acciderit candities does not awmar1 allowable leakage specified in the ANO Unit 1 PSAR and Techniml specifications. 'Ihe test was parfanned under IIRE Prrv=rtire 1092.030, Revision O.
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| 'Ihe test was conducted in nerywdance with the requirements of
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| '10CMt50 Appendix J, using the absolute method defined in ANSI N45.4-1972. Isakage rates were calculated using the Mass Point Method of ANSI /ANS 56.8-1981 and the Total Time Method of Bi 'IUP-1, 1972. '!he "as left" IIRF leakage rates and minimum pathway Type B and C leakage ratas were used to calculata "as found" IIRr leakage ratas.
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| 'Ihe "as left" and "as found" leakage rates calculated at the 95% t@per confidence limit (UCL) were less the 75% of the allowable leakage rata, i.e., less than 0.150%/ day. All requirunents of 10CPR50 Appendix J and the Arkansas Nuclear One, Unit 1 FSAR and Technical Specifications were satisfied.
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| A sumnary of events and test du.u.., logy are presented in Section II, Test Synopsis. Plant information, technical data, O test results, and. innamirement systen information are geaad in Section III, Test Data Sununary. Test results are ocupared to the acceptance criteria in Section IV, Analysis and Inte.u s wtation.
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| O ANO1
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| II. SYNOPSIS f3 I
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| 'Ibe containment was isolated by aligning systems in the specified post-accident modes, except as noted in Section IV.
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| Containment pressurization started at 0014 on 11/8/88.
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| Containment fans were run during pressurization. Between 10 and 14 psig, a leak search was conducted on all penetrations. No significant leakage was observed.
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| 'Ibe containment fans were shut off at 1900 on 11/8 and test pressure, 59.26 psig, was reached at 1940 on 11/8. 'Ihe pressurization line was isolated and vented, and the ,
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| stabilization period started at 1945 on 11/8. !
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| During the first three and one-half hours of stabilization containment pressure decreased to 59.11 psig. Acklitional pressurization frun 2310 to 2325 on 11/8 increased the pressure to 59.25 psig. 'Ihe pressurization line was re-isolated and vented. Temperature stabilization criteria were satisfied during the six hour period fr m 1945 on 11/8 to 0145 on 11/9.
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| A sumamaful ten hour IIRT was performed frcan 0145 to 1145 on 11/9. 'Ihe calculated leakage rate using the mass point method was 0.077%/ day with a UCL of 0.080%/ day. 'Ihe calculated leakage rate using the total time method was 0.086%/ day with a UCL of 0.114%/ day.
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| i The verification flow of 13.0 scfm (0.2%/ day) was initiated at 1217 on 11/9. Following a one hour stabilization period, a successful five hour verification test was performed fram 1330 to 1830 on 11/9. 'Ihe calculated leakage rates during the verification test were 0.283%/ day using the mass point method and 0.275%/ day using the total time method.
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| O ANO1
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| l III. TEST DMA SUMGRY A. Plant Informatica -
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| Owner Arkansas Power & Light Plant Arkansas Nuclear One, Unit 1 Iocaticm 6 miles NW of Ramam11ville, Arkansas Cantaiment Type Prestressed, post-tensioned concreto NSSS Supplier, Type B&W, PWR Docket No. 50-313 License No. DPR-51 B. Technical Data
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| : 1. Containment Net Free Air Volume 1,865,600 cu. ft.
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| (truncated to 1,865,000 cu. ft. for leakage rate mlatlations)
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| : 2. Design Pressure 59 psig
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| : 3. Design Temperature 150' F
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| : 4. Calculated Peak Accident Pressure, Pa 59 psig
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| : 5. Peak Accident hWatiltu 350' F C. Test Results - Type A Test
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| : 1. Test Method Absolute
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| : 2. Data Analysis Mass Point (per ANSI /ANS Techniques 56.8-1981)
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| 'Ibtal Thne (per BN 'IOP-1, 1972)
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| : 3. Test Pressure 59.2
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| : 4. Maximum Allowable Isakage Rate, la 0.2%/ day
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| : 5. 75% of Ia 0.150%/ day O
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| AN01
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| : 6. Integratcd Isakage l< ate Isakace Rate, %/ day
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| ,o .:st Results Frcan Rs.gassion At Upper
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| ( Line (Iam) 95% Confi-den Limit Mass Point Analysis 0.077 0.080
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| 'Ibtal Time Analysis 0.086 0.114
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| : 7. Verification Test T W _
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| Isakage Rate 13.0 SCEM (0.2%/ day)
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| : 8. Verification Test Isakage Rate (%/ day)
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| Results Mass Point Analysis 0.283 Total Time Analysis 0.275
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| : 9. Verification Test Limits Test Limits (%/ day)
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| Mass Point Analysis Upper Limit (Io+Iam+0.25Ia) 0.327 Iower Limit (Io+Iam+0.25La) 0.227 Total Time Analysis Upper Limit (Io+Iam+0.25La) 0.336 Iower Limit (Io+Iam+0.25Ia) 0.236
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| : 10. 'Ibe report printouts and data plots for the Type A and Verification Test are provided in Appendices D throtr3h G.
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| D. Test Results - Type B & C Tests Refer to Appendix I for summary of Iocal Isakage Rate
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| 'Dast results since the last IRLT was performed.
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| E. Integrated Isakage Rate Measurement System
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| : 1. Absolute Pressure (2 channels)
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| Range: 0-100,000 count z.
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| Measurement system error: 0.001 psia Sensor error: 0.005 psia Range: 0-100 psia Sensor Repeatability: 0.0005 psia l Display Repeatability: 0.001 psia l l 0
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| )
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| ANO1 l - - _ _ _ _ - _ _ _ _ _ _ _ _ _ _ _ .\
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| 4
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| Texas Instruments Model 145-02 Precision Pressure r Instruments, Serial No. 2861 (j '
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| Bourdon N ur_11e Serial No. 6806 Calibration Date: 9/29/88 Texas Instruments Model 145-02 Precision Pressure Instruments, Serial No. 2860 Bourdan Np=11e Serial No. 6806 Calibration Date: 9/29/88
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| : 2. Drybulb LW&h2re (17 channels)
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| Range: (-190) - (+200) *F Measuriunent system error: 0.1* F Sensor error: 0.2* F Sensor Repeatability: 0.05* F Display Repeatability: 0.01* F Resimimie hwature Detectors - raada & Nvilluw
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| 'Ihermohm lead,100-chm w Calibration Date: 10/21/88
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| : 2. Dewpoint Temperature (6 channels)
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| Range: 0-100*F r Measurement system
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| ! error: 0.5* F Sensor error: 0.54' F Sensor Repeatability: 0.10' F Display Repeatability: 0.01* F Dewpoint h W du2re Systems - EG & G 660 Calibration Date: 10/6/88
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| : 4. Verification Flow (1 channel)
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| Range: 1.3-24.8 scfm Acx:uracy: 1.0% F.S.
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| Flowmeter-Brooks Hi-accuracy full view rotameter, Model 1110-08K2-E1A Calibration date: 10/25/88
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| : 5. Overall Instrumentation Selection unidaline (ISG)
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| Value (from ANSI /ANS 56.8-1981) based on IIRT instrumentation and an ten hour test duration is 0.009%/ day.
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| 'Ihe ISG calculation uses the errors described above and a pressure of 73.79 psia, a dewpoint temperature
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| , of 58' F (0.00857 psia /*F frtan steam tables between 57 and 59' F) and an RID temperature of 528.3* R.
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| AN01
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| l
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| : 6. Drybulb and Dewpoint Temperature Sensor locations and Volume Fractions - See Table 1.
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| F. Information Retained at Plant
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| '!he following infacention is available for review at the I facility:
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| 1
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| : 1) A listing of all ocntainment p.r.' u oticais, including the total number of like g ^ motions, penetration i size and function.
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| : 2) A listing of normal operating instrumentatics used for the laakage rate test.
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| : 3) A system lineup (at time of test), showing required valve positions and status of piping systems.
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| : 4) A continuous, marrwitial log of events frtan initial survey of cantairanent to restoration of all tested systems. l
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| : 5) h=aritation of instrumentation ml4hratica and standards.
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| O 6) Data to verify tenparature stabilization critaria as established by test p - hu. (Appendix B) .
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| : 7) '1he working copy of test r -Mnit that includes signature sign-off of pu -Miral steps.
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| ^
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| : 8) 'Ihe gi Mire and all data that would verify ocapletion of pes =^u ations and valve testing (Type B and C tests), including as found leakage rates, uu.4dve action taken, and final leakage rate.
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| : 9) A listing of all test exceptions including changes'in ocntainment system boundaries instituted by licensee to conclude s - aful testing.
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| : 10) hiption of method of leak rate verification of instrument measurirg system (super 4W_ leakage),
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| with calibration information on flowmeters along'with mimlations that were used to measure the verification leakage rate.
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| : 11) 'Ihe P & ID's of pertinent systems are readily available.
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| O ANO1
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| l TMEE1 o - - - -
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| saem tocmms e muME FRacr1ms q 4
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| RADIAL VOIIEE SENSm EEE7. AZIMmi DISTANCE FRACTI N EID 1 348 340 30 0.027 2 348 160 30 0.027 3 342 270 40 0.064 4 380 225 50 0.052 5 410 270 40 0.038 6 380 330 55 0.052
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| *7 340 60 55 0.000 8 400 0 0 0.038 9 410 120 50 0.038 10 410 180 35 0.031 11 410 0 40 0.031 12 500 180 50 0.086 13 510 0 40 0.086 14 480 180 20 0.086 15 450 0 20 0.086 16 465 180 40 0.086 17 430 0 30 0.086 18 520 180 40 0.086 1.000
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| * RID 7 was not calibrated and was not used during the IIRP DEWCELL 1 348 190 33 0.116 2 381 270 44 0.168 3 410 330 50 0.179 4 435 300 50 0.179 '
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| 5 480 180 30 0.179 6 510 180 50 0.179 1.000 0
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| ANO1
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| IV. A1& LYSIS AND INTERPfEFATION O A. IIRT Test Corrections During the IIRT five permeations were not in post-IIXA alignment.
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| 'Ibe per=Lations and mininum pathway "as left" leakage rates are given below:
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| Per= Lation System Isakage Rate P-7A* RCS Sanple 9.972 acm P-42 Plant Heating 0.155 accm P-43 Breathing Air 23.095 acam P-46 Instrument Air 2.09 acam P-48 Plant Heating 0.225 accm P-49 IIRT Pressurization 11.12 aom Total 46.657 ac m 0.0001%/ day
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| * Maintenance was performed on this valve post-IIRP.
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| Water volume changes in the containment during the IIRT were negligible. During the period fr m 2336 on 11/8 to 0920 on 11/9 the pressurizer level remained constant at 20.12" and the sump level increased fran 9.2% to 9.25%.
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| O B. "As Isft" Isakage Rate
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| 'Ihe "as left" leakage rates are equal to the leakage rates calculated during the IIRT plus the total of the "as left" minimum pathway leakages frun penetrations not in post-IIXA alignment during the IIRP. 'Ihe "as left" leakage rates are given below.
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| Isakage Rate, %/ day MASS POINT 'IUPAL TIME Isakage Rate UCL Isakage Rate UCL IIRT 0.077 0.080 0.086 0.114 Corrections 0.000 0.000 0.000 0.000 "As Inft" IIRT 0.077 0.080 0.086 0.114 Since the "as left" Mass Point and 'Ibtal Time UCL's are less then .751a (0.150%/ day), the test results demonstrate that the leakage through the prinary containment and systems and components penetrating primary containment do not exceed the allowable leakage rates specified in the Ato Unit 1 FSAR and
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| 'Ibchnical Specifications.
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| O ANO1 l
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| l
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| _ _ _ _ _ _ - = _ _ _ - _ _-_ -~
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| )
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| C. "As Found" Isakage Rates O
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| 'Q- The "as found" leakage rates are equal to the "as left" leakage rates plus the total of the differences (but not negative) between the "as'found" and "as left" mininum pathway leakages for all type c and type B per Lations.
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| Penetrations with "as found" "as left" = den are:
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| Penetration "as found" "as left" 1P-31 832.14 acon IP-32 275.255 acca IP-33 6.05 acca IP-42 0.84 acon ip-48 0.235 aa m 1P-52 4.86 acm 1P-53B 240.915 acom 1P-59 5.405~ac e IIHiO 15.8 acan
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| -C1 1.115 acca 1,382.615 acam 0.004%/ day i The "as found" leakage rates are given below:
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| Isakage Rate, %/ day MASS POINT 7UIAL TIME Isakage Rate UCL' Isakage Rate UCL IIRT 0.077 0.080 0.086 0.114 Corrections 0.004 0.004 0.004 0.004 "As Inft" IIRT 0.081 0.084 0.090 0.118 Since the "as found" Mass Point and Total Time UCL's are less then .75Ia (0.150%/ day), the test results J-rs Late that the leakage through the primary containment and systems and cuwwAs per=Lating primary containment do not exneed the allowable leakage rates specified in the ANO Unit 1 iSAR and Technical Specifications.
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| O ANO1 i
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| l I
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| V. REFERENCES
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| : 1. Arkansas Nuclear One Unit 1 Procedure No. 1092.030,
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| " Integrated Leak Rate 'hst of Primary Containment (Type A Test)", Revision O.
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| : 2. Code of Federal Regulation, Title 10, Part 50, Apperrlix J,
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| " Primary Reactor Containment Isakage Testing for Water l
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| Cooled Power Reactors".
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| l 3. ANSI /ANS 56.8-1981, " Containment Systen Isakage Testing l Requiummm/Ji".
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| : 4. ANSI N45.4-1972, "Isakage Rate Testing of Containment Structures for Nuclear Reactors".
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| : 5. Bechtel topical Report BN 'IOP'-1, " Testing Criteria for Integrated T W Rate Testing for Primary Containment Structures for Nuclear Power Plants", Revision 1, November 1972.
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| O O
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| ANO1
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| e O
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| NA MM Im conputer rc% %
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| I i
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| O I I
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| O
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| l (7 APPENDIX A b msmImm w wrmw. nur Cenza Paxmm 1 A. Pt wtam and Be ort Description
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| : 1. S e Bechtel IIRP computer pr@ tam is used to deternine the integrated leakage rate of a nuclear primary containment struc ~ure. % e pr% tam is used to cmpute leakage rate based on input value::s of time, free air volume, containment atmosphere total pressure, drybulb temperature, and dewpoint temperature (water vapor pressure) .
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| Isakage rate is emputed using the Absolute Method as defined in ANSI /ANS 56.8-1981, "Corth System Isakage Testing Requirements" and BN-40P-1, Pav 1, " Testing Criteria for Integrated Isakage Rate Testing of Primary Containment Structures for Nuclear Power Plants".
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| B e pr@ tam is designed to allow the user to evaluate containment leakage rate test results at the jobsite during containment leakage testing. Current leakage rate values may be obtained at any time during the testing period using one of two computational methods, yielding three different report printouts.
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| : 2. In the first printout, the Total Time Report, leakage rate is camputed fram initial values of free air volume, containment (Q) at - sitiere drybulb temperature and partial pressure of dry air, the latest values of the same parameters, and elapsed time. Rese individually camputed leakage rates are statistically averaged using linear regression by the method of least squares. W e htal Time Method is the computational technique upon which the short duration test criteria of BN 'IOP-1, Rev 1, " Testing Criteria for Integrated Leakage Rate h sting of Primary Containment Structures for Nuclear Ptver Plant," are based.
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| : 3. S e second printout is the Mass Point Report and is based on the Mass Point Analysis Technique described in ANSI /ANS 56.8-1981, ,
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| " Containment System Isakage Testing Requirements". Se mass of dry I air in the containment is computed at each data point (time) using the Equation of State, from current values of containment atmosphere drybulb temperature and partial pressure of dry air. Contained mass is " plotted" versus time a M a regression line is fit to the data using the method of least squares. Ieakage rate is determined from the statistically derived slope and intercept of the regression line.
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| : 4. The third printout, the TreM Report, is a summary of leakage rate values based on Ibtal Time and Mass Point computations presented as a function of number of data points and elapsed time (test duration) .
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| The Trend Report provides all leakage rate values required for p)
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| (
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| camparison to the acceptance criteria of BN-IDP-1 for conduct of a short duration test.
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| A-1
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| O
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| ()
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| ~ 5. 'Ihe sws== Wr.cetes a predictor report Mmi on " Suggested Criteria for a Short Duration IIRr", Ted Brown and Iouis Estenssoro, Prrv'aari4rns of the First Wvrks ic on Containment Testirn, January 18, 1982. 'Ihe " predictor" is an estimate of the upper bound on the change in mass point mlonated leakage rate which will occur during the next four hours. 'Ibe estimate is M=i on the mass point calculated leakage rates and 95% UCIs during the previous four hours.
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| : 6. 'Ihe pr@tmu is written in a high level language and is designed for use on a miu v ,.w A with direct data input from the data l acquisition system. Brief descriptions of progrun use, formulae used for leakage rate ocuputations, and pi wimu logic are provided in the following paragraphs.
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| B. Explanation of Fww.m.
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| : 1. 'Ihe Bechtel IIRr computer pr@tmu is written, for use by experienced IIRr pasanu7.1, to determine contairrJent integrated leakage rates l based on the Absolute 14elisi described in ANSI /ANS 56.8-1981 and BN-TOP-1.
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| 3 Information Irwlari into the swtmu prior to or at the start of the test:
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| : a. Ihmiber of containment atmosphere drym , =nperature sensors, dewpoint temperature (water vapor pressure) sensors and pressure gages to be used in leakage rate computations for the specific test
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| : b. Volume fractions assigned to each of the above sensors
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| : c. Calibration data for above sensors
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| : d. Test title
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| : e. Maximum allowable leakage rate at test pressure
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| : 3. Data received from the data acquisition system during the test, and q used to campute leakage rates:
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| : a. Time and date
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| : b. Containment atmosphere drybulb temperatures ;
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| i
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| : c. Containment atmosphere pressure (s)
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| : d. Containment atnesphere dewpoint temperatures
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| : e. Containment free air volume.
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| /
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| : 4. After all data at a given time are received, a Summary of Measured j Data report (refer to "Ftwicuu Logic," Paragraph D, " Data" option I command) is printed.
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| A-2
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| [
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| : 5. If drybulb ard dawpoint
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| * seq =rature sensors should fail during the
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| ..O
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| ' test, the data fr a the sensor (s) are not used. '1he volume fractions for the remaining sensors are r--> :-_2ted and rel* into the g,cuu .
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| for use in ensuing leakage rate ocuputations. )
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| 1 C. T=1== Rate Phr-w
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| : 1. Ccaputations Using the Total Time Method:
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| : a. Measured leakage rate fr m data:
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| PY11" W 1 El (1)
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| PVi1=WEi i (2) 2400 (W1-W) i
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| _ (3) at.Wi 1 solving for W1 and Wi and substiW equations (1) and (2) into (3) yields:
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| , [1_ b (4).
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| .O Ati ( TPYi11/
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| where W,Wi 1 = Weight of contained mass of dry air at times t1 .
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| and t i, respectively, lbm.
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| T,Ti 1 = containment ata = pere drybulb temperature at times t i and t i, respectively, *R.
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| P,Pi 1 = Partial pressure of the dry air camponent of the containment atlimpere.at times ty and t i, respectively, psia.
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| V,Vi 1 = Containment free air volume at times ti aM t, respectively (constantorvariableduring ]
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| i e test) , ft st and i D data points respectively, hr.
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| t,ti i = Time at 1 Ati = Elapsed time from ty to t i, hr.
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| R = Specific gas constant for air = 53.35 ft.lbf/lbm. *R. l O Li = Measured leakage rate computed during time interval t 1 to t i, wt.%/ day.
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| A-3
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| ('A ~ 'To reduce truncation error, the computer ptwtam uses the )
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| following equivalent formulation: j
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| -2400 / AWi j Ati (W1) where AWi -
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| Wi-W1 Wi - W1 api AVi APi AVi ATi
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| + + -
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| P1 Y1 PV11 T1 ATi T1 api =P -P 1 AV i=Ti-V1 ATi= i-T1 O
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| ~
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| : b. almlated leakage rate fran regression analysis:
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| L=a+ bat N (5) where i, = calculated leakage rate, wt.%/ day, as determined from the r%tussion line.
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| (6) a = (ILi - b I At i)/N N(IL iAt i) - (Iq)(I At i) b= (7) 2 N(I Ati ) - (I At i)2 N = Number of data points.
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| N I= I i=1
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| : c. 95% upper confidence limit on the calculated leakage rate:
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| UCL = a + b a tN + S-L A-4
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| e
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| .UCL = 95% upper confidence limit wt.%/ day, at' elapsed time AtN*
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| For a tN < 24 S- =
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| tsE(ILi - AILi - b IL iat )/(N-2)]1/2 i
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| [1 + 1 + (AtN - At)2/ (EAti2 - (Zat i)2/N)] W (9a)'
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| N where t = 1.95996 + 2.37226 + 2.82250 ;
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| s N-2 (N-2)d For AtN 2 24 S- =t s E(ILi - AILi - bIL At i )/(N-2)]1/2 i
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| 1/2
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| [1 N
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| + ( A ti- At)2/ (Eati2 - (It )2/N)]
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| i (9b)
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| /~ 1.6449(N-2)2 + 3.5283(N-2)-+ 0.85602 Where ts" (N-2)2 + 1.2209(N-2) - 1.5162 Li = Calculated leakage rate camputed using equation (5) at total elapsed time at ,i%/ day.
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| At = IAti N
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| : 2. Computation using the Mass Point Method:
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| : a. Contained mass of dry air from data:
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| W1 = 144 P Vii RTi (10) where All symbols as previously defined.
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| \' l A-5 1
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| : b. almlated leakage rate frtat regression analysis, W = a + b At E = -2400 a (11).
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| 1 eere 5 = m1mlated leakage rate, wt.%/ day, as datamined.fran the r%s s ion line. ,
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| a =
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| (IWi - bIat i)/N (12)
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| N(IW iat i) - (IW i)(IAt i) b = ~ (13) d N(I Ati ) - (I At i)#
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| ati= Total elapsed time at time of ith data point, hr.
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| N = Number of data points.
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| Wi
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| = cantained mass of dry air at i th data point, lhn, as ocmputed fran equation (10) .
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| h I ! ~
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| i=1 To reduce truncation error, the ccanputer pr%sma uses the following equivalent formulation:
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| ~
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| AW i
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| b -
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| a = W1 1 + (I -
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| -Iat i)/N (14)
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| W1 W1 .
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| I AWi AWi N (I at)-I i Iati W1 W1 b =
| |
| Wi (15) 2
| |
| , N(Iati ) - (Iat i)2 -
| |
| where is as previously defined.
| |
| W1
| |
| : c. 95% upper confidence limit.
| |
| -2400 ps UCL = (b - Sb) (16)
| |
| V a A-6
| |
| _ ___. ._______-___________-_a
| |
| | |
| 4 UCL = 95% upper confidence limit, wt.%/ day.
| |
| SN1/2 Sb =
| |
| t,[NIati 2- (I At )2)1/2 i (17).
| |
| L 1.6449 (N-2)2 + 3.5283 (N-2) + 0.85602 l
| |
| where t,=
| |
| (N-2)2 + 1.2209 (N-2) - 1.5162 l
| |
| l
| |
| =
| |
| ' I [Wi - (a + b ati)]2 V2 l S
| |
| ! . N-2 .
| |
| 1
| |
| =-W1 I ( AWi/W 1 )2 _ ( 3 ( 3wijg1 ))2fg _
| |
| qN-2
| |
| [E(aW i /W 1 ) a ti- I( a W i /W 1 ) (Iat i )/N]I (18) 2 I(a ti ) _-(I a t )2/N i .
| |
| : d. Predictor:
| |
| 2[(UCL L) + 4 (l Al + 2 S A) 3 100 Ia where UCL = 95% upper confidence limit of mass point calculated leakage rate at end of test.
| |
| L = Mass point calculated leakage rate at end of test.
| |
| A = Value of linear regression analysis slope of mass point calculated leakage rate vs. time for last 4 hours of test data.
| |
| Sg = Linear repxssion analysis standard deviation of slope.
| |
| La = Allowable leakage rate.
| |
| In tenns of elapsed time, a t and mgs point calculated leakage time interval.
| |
| rate Imi calculated at the end of i
| |
| .O A-7
| |
| - --------__---__._________m_ _ _ _ _ _ _ m
| |
| | |
| l /~ g. , 1 I mi-BI4 hr ati (19),
| |
| l M ,
| |
| 4 hr ,
| |
| M I 4 hr miati-I4 hr mi I4 hr ati .
| |
| (20) -
| |
| B = !
| |
| ati 2 Mr4 hr -I at i 2 4 hr I
| |
| 4 hr mi-AI4hr mi - B I4hr mi a ti (21)
| |
| SA "
| |
| [M-2] [M I At I At )2) i 4 hr i - (4 hr Imi = mass point mimilatal leakage rate evaluated using data up to time a t i.
| |
| 4 hr = sumation over last 4 hours of test data.
| |
| N
| |
| = I O
| |
| I-N-M+1 M = number of data points for last 4 hours of test.
| |
| t O 1 4
| |
| A-8 l
| |
| | |
| D. Proaran Imic
| |
| : 1. h Bechtel IIRT couputer program logic flow is dadaclied by a set of user options. h user opticos and a brief description of their associated function are p. -aded below.
| |
| OFIION CCPHAND PUNCTION After starting the program execution, the user either enters the name of the file containing previously entered data or initialized a new data .
| |
| file.
| |
| DWIA Enables user to enter raw data.= When the system requests values of time, volume, temperature, pressure and vapor pressure, the user enters the w up. lata data. After ocupleting the data entry, a vn== nary is printed out. '1he user then verifies that the data were entered sudy. If errors are detected, . the user will then be given the uppu.t. unity to correct the errors. After the user verifies that the data were entered uvudy, a Corrected Data Sinenary "+ i. of time, data, average tercure, partial pressure of dry air, and water vapor pressure is printed.
| |
| TREND A Trend Report is printed.
| |
| 'IUIAL A 'Ibtal Time Report is printed.
| |
| MASS A Mass Point Report is printed.
| |
| TERM Enables user to sign-off temporarily or permanently. All data is saved on a file for restarting.
| |
| CORR Enables usa to correct previously entered data.
| |
| LIST A Summary Data Report is printed.
| |
| READ Enable the computer to receive the next set of data frun the data acquisition system directly.
| |
| PIDF Enables user to plot e - ry data, individual sensor data or air mass versus time.
| |
| DE TfE Enables user to delete a data point.
| |
| INSERT Enables user to reinstate a previously deleted data l point. !
| |
| '" - Enable user to change volume fractions.
| |
| VOIERA A-9
| |
| | |
| 1
| |
| ,f] OFIION V _QOt!AND FUNCTION PRED A predictor report is printed.
| |
| L TIME Enable the user to specify the time interval for a report or plot.
| |
| VERF Enable the user to input 4 W leakage rate and l calculated IIRT leakage rates at start of verification test.
| |
| E. Ommuter Report and Data Printout MASS POINT REPORP 2 e Mass Point Report presents leakage rate data (wt%/ day) as determined by the Mass Point Method. The " Calculated Isakage Rate" is the value determined fr m the r%1.assion analysis. 'Ihe " Containment Air Mass" values are the m'- of dry air in the containment (1bm). 'Ihese air masses, determined fra the Equation of State, are used in the rey 1.assion analysis.
| |
| IUIAL TIME REEORT The Total Time Report presents data leakage rate (wt%/ day) as determined by the Total Time Method. 'Ihe " Calculated Isakage Rate" is the value determined frm the reg 1.assion analysis. She " Measured Isakage Rates" are the leakage rate values determined using Ibtal Time calculations.
| |
| These values of leakage rate are used in the regression analysis.
| |
| TREND REPORT The Trend Report presents leakage rates as determined by the Mass Point and 7btal Time methods in percent of the initial contained mass of dry air per day (wt%/ day), versus elapsed time (hours) and number of data points.
| |
| PREDICIOR REIORT The predictor reports presents a predicted upper bound on the change in calculated mans point leakage rate over the next four hours.
| |
| | |
| ==SUMMARY==
| |
| DATA m2uRI The Summary Data report presents the actual data used to calculate leakage rates by the various methods described in the Camputer Program" section of this report. The seven columns are TIME, DATE, TEMP, PRESSURE, VPRS, VOLUME, and AIRMASS and contain data defined as follows:
| |
| O A-10
| |
| | |
| r3 1. TIME: Thne in 24-hour notation (hours and mirutes) .
| |
| s I
| |
| : 2. IRTE: Calendar date (nonth and day) .
| |
| : 3. TIMP: Containment weighted-average drybulb temperature in absolute units, degrees Rankine ('R).
| |
| : 4. PRESSURE: Partial pressure of the dry air u. w ent of the !
| |
| containment atku@ere in absolute units (psia) .
| |
| : 5. VPRS: Partial pressure of water vapor of the containment atmosphere in absolute units (psia).
| |
| : 6. VOIUME: Containment free air volume (cu. ft.) .
| |
| : 7. AIRMASS: Calculated dry air mass (lbm) .
| |
| F. Summary of Measured Data and Sinemy of Cumsfwd Ibta l
| |
| 'Ihe Summary of Measured Data presents the individual containment atanosphere drybulb temperatures, dewpoint temperatures, absolute total pressure and free air volume measured at the time and date.
| |
| : 1. TEMP 1 through TEMP N are the drybulb temperatures, where N = No. of 7s RID's. 'Ihe values in the right-hand column are temperatures (*F),
| |
| (" ) multiplied by 100, as read from the data acquisition system (DAS) .
| |
| 'Ihe values in the left-h&nd column are the corrected temperatures expressed in absolute units (*R).
| |
| : 2. PRES 1 through PRES N are the total pressures, absolute, were N = No.
| |
| of pressure sensors. The right-harxi value, in parentheses, is a number of counts as read from the DAS. This count value is converted to a value in psia by the computer via the instrument's calibration table, counts versus psia. The left-hand column is the absolute total pressure, psia.
| |
| : 3. VPRS 1 through VPRS N are the dewpoint temperatures (water vapor pressures), where N = No. of dewpoint sensors. The values in the right-hand column are temperatures (*F), multiplied by 100 as read from the DAS. 'Ihe values in the left-hand column are the water vapor pressures (psia) fra the steam tables for saturated steam couesporKling to the dewpoint (saturation) temperatures in the center column.
| |
| The Summary of Corrected Data presented corrected temperature and pressure values and calculated air mass determined as follows:
| |
| : 1. TEMPERATURE (*R) is the volume weighted average containment atmosphere drybulb temperature derived from TEMP 1 thrcugh TEMP N.
| |
| O
| |
| \v)
| |
| A-11
| |
| : 2. CCRRBCIED PRESSURE (psia) is the partial pressure of the r" - dry air W.:ad of the ocntainment atmosphere,
| |
| ( absolute. 'Ihe volume weighted average containment atmosphere water vapor pressure is subtracted from the volume wei@ted average total pressure, yielding the partial pressure of the dry air.
| |
| : 3. VAPCR PRESSURE (psia) is the volume weighted average containment ah- ,We water vapor pressure, absolute,
| |
| _ derived fran VPRS 1 throu@ VPRS N.
| |
| : 4. WIIME (cu. ft.) is the containment free air volume.
| |
| : 5. CINIAINMElff AIR MASS (lbn) is the calculated mass of dry air in the acrztainnent. 'Ihe mass of dry air is m1aMated using the containment free air. volume and the above Tf!MPERA2URE and CIERECIED PRESSURE of the dry air.
| |
| G. IEAKMT RATE CAICUIATICE VERIFICATION
| |
| 'Ihe IIRT Ctsputer program leakage rate calculation is verified as follows:
| |
| : 1. A hand verified IIRP data set is used to verify that the program mlanates the correct mass point and total time i leakage rates and UCL's for a given set of air mammaa. I
| |
| 'O N1anated leakage rates ralst agree within 0.001%/ day.
| |
| : 2. After reaching test pressure, hand calculated weighted average tau p ature, pressure and vapor pressure and air mass for an actual data point are used to verify that the IIRT pu: oui calculates correct values for the parameters.
| |
| Calculated temperatures must agree within 0.001 degree R, pressure and vapor pressures within 0.001 psia and air mass within 1 lbm.
| |
| A-12
| |
| | |
| O APPENDIX B IIRT Stabilization Simemry Data Report l
| |
| O O
| |
| l
| |
| | |
| n ) ARKANSAS NUCLEAR ONE UNIT 1
| |
| (
| |
| | |
| ==SUMMARY==
| |
| DATA ALMAX = .200 VOLUME = 1865000.
| |
| VRATET = .286 VRATEM = .277 TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 1945 1108 529.462 73.5781 .2396 1865000.0 699553.8 2000 1108 529.264 73.5530 .2386 1865000.0 699576.1 2015 1108 529.123 73.5347 .2393 1865000.0 699588.5 2030 1108 529.018 73.5218 .2397 1865000.0 699604.6 2045 1108 528.931 73.5124 .2390 1865000.0 699630.8 2100 1108 528.864 73.5036 .2388 1865000.0 699634.6 2115 1108 528.807 73.4968 .2386 1865000.0 699645.3 2130 1108 528.763 73.4902 .2387 1865000.0 699641.3 2145 1108 528.718 73.4861 .2378 1865000.0 699660.7 2200 1108 528.677 73.4805 .2384 1865000.0 699662.5 2215 1108 528.642 73.4753 .2385 1865000.0 699660.0 2230 1108 528.612 73.4714 .2379 1865000.0 699662.4 2245 1108 528.582 73.4669 .2384 1865000.0 699657.6 2300 1108 528.554 73.4626 .2386 1865000.0 699654.6 2315 1108 528.533 73.4826 .2387 1865000.0 699873.4 2330 1108 528.673 73.6050 .2382 1865000.0 700853.4 2345 1108 528.617 73.5935 .2377 1865000.0 700818.9
| |
| - 0 1109 528.556 73.5852 .2385 1865000.0 700819.1 I\
| |
| \-
| |
| 15 1109 528.512 73.5785 .2387 1865000.0 700813.7 30 1109 528.470 73.5735 .2387 1865000.0 700822.1 45 1109 528.438 73.5693 .2384 1865000.0 700824.4 100 1109 528.414 73.5655 .2381 1865000.0 700821.3 115 1109 528.387 73.5614 .2377 1865000.0 700817.0 130 1109 528.356 73.5572 .2379 1865000.0 700818.4 145 1109 528.338 73.5533 .2383 1865000.0 700804.5 l
| |
| l
| |
| | |
| ARKANSAS NUCLEAR ONE UNIT 1 TEMPERATURE STABILIZATION FROM A STARTING-TIME AND DATE OF: 1945 1108 1988' TIME TEMP ANSI BN-TOP-1 (HOURS) ( R) AVE A T . AVE AT DIFF AVE A T (4 HRS) (1HR) (2 HRS)
| |
| .00 529.462
| |
| .25 529.264
| |
| .50 529.123
| |
| .75. 529.018 1.00- 528.931' 1.25 528.864 1.50 528.807 1.75 528.763-2.00 528.718 .372*
| |
| 2.25 528.677 .294*
| |
| 2.50- 528.642 .241*
| |
| 2.75- 528.612 .203*
| |
| 3.00 528.582 .174*
| |
| 3.25 '528.554 .155*
| |
| 3 . 5 0.- 528.533 .137*
| |
| .045*
| |
| O- 3.75 528.673 4.00- 528.617 .211 .034 .245* .051*
| |
| 4.25 528.556 .177 .002 .179* .060*
| |
| 4.50- 528.512 .153 .021 .132*' .065*
| |
| 4.75 528.470 .137 .203- .066* .071*
| |
| 5.00 528.438 .123 .178 .055* .072*
| |
| 5.25 528.414 .113 .143 .030* .070*
| |
| 5.50 528.387 .105- .125 .020* .073*
| |
| 5.75 528.356 .102 .114 .012* .159*
| |
| 6.00 528.338 .095 .100 .005* .139*
| |
| * INDICATES' TEMPERATURE STABILIZATION HAS'BEEN SATISFIED
| |
| | |
| i O
| |
| APPE2EX C IIRE Summary Data Report O
| |
| O
| |
| | |
| (o)
| |
| ~
| |
| ARKANSAS NUCLEAR ONE UNIT 1
| |
| | |
| ==SUMMARY==
| |
| DATA ALMAX = .200 VOLUME = 1865000.
| |
| VRATET = .286 VRATEM = .277 TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 145 1109 528.338 73.5533 .2383 1865000.0 700804.5 200 1109 528.310 73.5495 .2381 1865000.0 700806.5 215 1109 528.287 73.5463 .2388 1865000.0 700805.3 230 1109 528.267 73.5435 .2385 1865000.0 700806.1 245 1109 528.245 73.5396 .2390 1865000.0 700797.0 300 1109 528.227 73.5374 .2387 1865000.0 700800.8 315 1109 528.209 73.5338 .2392 1865000.0 700791.0 330 1109 528.192 73.5314 .2391 1865000.0 700790.3 345 1109 528.173 73.5285 .2395 1865000.0 700788.2 400 1109 528.157 73.5260 .2395 1865000.0 700784.6 415 1109 528.142 73.5224 .2401 1865000.0 700769.9 430 1109 528.123 73.5211 .2394 1865000.0 700783.4 445 1109 528.109 73.5178 .2397 1865000.0 700770.6 j t
| |
| 500 1109 528.095 73.5154 .2401 1865000.0 700766.4 515 1109 528.081 73.5131 .2403 1865000.0 700763.4 530 1109 528.066 73.5103 .2407 1865000.0 700756.5 545 1109 528.055 73.5077 .2407 1865000.0 700746.1 f> 600 1109 528.041 73.5044 .2420 1865000.0 700733.6 f 615 1109 528.032 73.5027 .2417 1865000.0 700728.6
| |
| ~
| |
| 630 1109 528.022 73.5005 .2419 1865000.0 700720.4 645 1109 528.011 73.4978 .2421 1865000.0 700709.9 700 1109 528.003 73.4959 .2420 1865000.0 700702.5 715 1109 527.991 73.4937 .2422 1865000.0 700697.8 730 1109 527.981 73.4915 .2424 1865000.0 700690.3 745 1109 527.971 73.4896 .2423 1865000.0 700685.3 800 1109 527.964 73.4869 .2429 1865000.0 700669.4 815 1109 527.954 73.4856 .2423 1865000.0 700668.9 830 1109 527.943 73.4844 .2420 1865000.0 700671.9 845 1109 527.937 73.4821 .2423 1865000.0 700657.7 900 1109 527.924 73.4801 .2428 1865000.0 700656.3 915 1109 527.912 73.4786 .2422 1865000.0 700658.7 930 1109 527.908 73.4773 .2425 1865000.0 700652.2 945 1109 527.899 73.4744 .2429 1865000.0 700635.9 1000 1109 527.889 73.4734 .2424 1865000.0 700639.9 1015 1109 527.878 73.4720 .2418 1865000.0 700640.4 1030 1109 527.873 73.4703 .2420 1865000.0 700630.5 1045 1109 527.869 73.4673 .2425 1865000.0 700608.0 1100 1109 527.855 73.4662 .2421 1865000.0 700616.5 1115 1109 527.841 73.4652 .2416 1865000.0 700624.1 l 1130 1109 527.833 73.4633 .2420 1865000.0 700617.8 1145 1109 527.828 73.4622 .2416 1865000.0 700613.4 O
| |
| 1
| |
| | |
| 0 0 .
| |
| APPENDIX D IIRT n=1onations O
| |
| 1 O l l
| |
| | |
| ARKANSAS NUCLEAR ONE UNIT 1 LEAKAGE RATE (WEIGHT PERCENT / DAY)
| |
| MASS POINT ANALYSIS
| |
| [D''') TIME AND DATE AT START OF TEST: 145 1109 1988 TEST DURATION: 10.00 HOURS TIME TEMP PRESSURE CTMT. AIR MASS LOSS AVERAGE MASS (R) (PSIA) MASS (LBM) (LBM) LOSS (LBM/HR) 145 528.338 73.5533 700804.5 200 528.310 73.5495 700806.5 -2.0 -7.9 215 528.287 73.5463 700805.3 1.1 -1.7 230 528.267 73.5435 700806.1 .7 -2.1 245 528.245 73.5396 700797.0 9.1 7.5 300 528.227 73.5374 700800.8 -3.8 2.9 I
| |
| 315 528.209 73.5338 700791.0 9.9 9.0 330 528.192 73.5314 700790.3 .6 8.1 345 528.173 73.5285 700788.2 2.1 8.2 400 528.157 73.5260 700784.6 3.6 8.9 415 528.142 73.5224 700769.9 14.6 13.8 430 528.123 73.5211 700783.4 -13.5 7.7 445 528.109 73.5178 700770.6 12.8 11.3 500 528.095 73.5154 700766.4 4.3 11.7 515 528.081 73.5131 700763.4 3.0 11.7 530 528.066 73.5103 700756.5 6.9 12.8 545 528.055 73.5077 700746.1 10.4 14.6 600 528.041 73.5044 700733.6 12.5 16.7 615 528.032 73.5027 700728.6 5.0 16.9 73.5005 700720.4 8.3 17.7
| |
| ('
| |
| s 630 645 528.022 528.011 73.4978 700709.9 10.4 18.9 700 528.003 73.4959 700702.5 7.4 19.4 715 527.991 73.4937 700697.8 4.7 19.4 730 527.981 73.4915 700690.3 7.5 19.9 745 527.971 73.4896 700685.3 5.0 19.9 800 527.964 73.4869 700669.4 15.9 21.6 815 527.954 73.4856 700668.9 .5 20.9 830 527.943 73.4844 700671.9 -2.9 19.6 845 527.937 73.4821 700657.7 14.2 21.0 900 527.924 73.4801 700656.3 1.4 20.4 915 527.912 73.4786 700658.7 -2.4 19.4 930 527.908 73.4773 700652.2 6.5 19.7 945 527.899 73.4744 700635.9 16.2 21.1 1000 527.889 73.4734 700639.9 -4.0 19.9 1015 527.878 73.4720 700640.4 .4 19.3 1030 527.873 73.4703 700630.5 9.8 19.9 1045 527.869 73.4673 700608.0 22.5 21.8 1100 527.855 73.4662 700616.5 -8.5 20.3 1115 527.841 73.4652 700624.1 -7.5 19.0 1130 527.833 73.4633 700617.8 6.2 19.1 1145 527.828 73.4622 700613.4 4.5 19.1 FREE AIR VOLUME USED (CU. FT.) =1865000.0 REGRESSION LINE
| |
| (^ INTERCEPT (LBM) = 700825.6
| |
| (_T) SLOPE (LBM/HR) = -22.4 MAXIMUM ALLOWABLE LEAKAGE RATE = .200 75% OF MAXIMUM ALLOWABLE LEAKAGE RATE = .150 THE UPPER 95% CONFIDENCE LIMIT = .080 THE CALCULATED LEAKAGE RATE = .077
| |
| | |
| ARKANSAS NUCLEAR ONE UNIT 1 LEAKAGE RATE (WEIGHT PERCENT / DAY)
| |
| TOTAL TIME ANALYSIS.
| |
| TIME AND DATE AT START OF TEST: 145 1109 1988 TEST DURATION: 10.00 HOURS TIME TEMP PRESSURE MEASURED (R) (PSIA) LEAKAGE RATE 145 528.338 73.5533 200 528.310 73.5495 .027
| |
| . 215 528.287 73.5463 .006 230 528.267 73.5435 .007 245 528.245 73.5396 .026 300 528.227 73.5374 .010 315 528.209 73.5338 .031 330 528.192 73.5314 .028 345 528.173 73.5285 .028 400 528.157 73.5260 .030 415 528.142 73.5224 .047 430 528.123 73.5211 .026 445 528.109 73.5178 .039 500 528.095 73.5154 .040 515 528.081 73.5131 .040 530 528.066 73.5103 .044 545 528.055 73.5077 .050 600 528.041 73.5044 .057
| |
| (' 615 528.032 73.5027 .058 630 528.022 73.5005 .061 645 528.011 73.4978 .065 700 528.003 73.4959 .067 715 527.991 73.4937 .066 730 527.981 73.4915 .068 745 527.971 73.4896 .068 800 527.964 73.4869 .074 815 527.954 73.4856 .071 830 527.943 73.4844 .067 845 527.937 73.4821 .072 900 527.924 73.4801 .070 915 527.912 73.4786 .067 930 527.908 73.4773 .067 945 527.899 73.4744 .072 1000 527.889 73.4734 .068 1015 527.878 73.4720 .066 1030 527.873 73.4703 .068 1045 527.869 73.4673 .075 1100 527.855 73.4662 .070 1115 527.841 73.4652 .065 1130 527.833 73.4633 .066 1145 527.828 73.4622 .065 MEAN OF THE MEASURED LEAKAGE RATES = .050 O MAXIMUM ALLOWABLE LEAKAGE RATE 75% OF MAXIMUM ALLOWABLE LEAKAGE RATE THE UPPER 95% CONFIDENCE LIMIT
| |
| =
| |
| =
| |
| =
| |
| .200
| |
| .150
| |
| .114 THE CALCULATED LEAKAGE RATE = .086
| |
| | |
| k' . -
| |
| ARKANSAS NUCLEAR ONE UNIT 1 TREND REPORT TIME AND DATE AT START OF TEST: 145 1109 1988 NO. END TOTAL TIME ANALYSIS MASS POINT ANALYSIS PTS TIME MEAS. CALCULATED UCL CALCULATED UCL 2 200 .027 .027 99.000 .027 99.000 3 215 .006 .006 99.000 .006 .100 4 230 .007 .003 .087 .005 .011 5 245 .026 .020 .070 .021 .057 6 300 .010 .020 .068 .018 .040 7 315 .031 .,031 .067 .029 .049 8 330 .028 .035 .068 .033 .047 9 345 .028 .037 .069 .034 .045 10 400 .030 .040 .070 .035 .044 i 11 415 .047 .047 .074 .044 .055 1 12 430 .026 .045 .077 .040 .050 13 445 .039 .047 .078 .042 .050 14 500 .040 .049 .078 .043 .051 15 515 .040 .050 .079 .044 .051 16 530 .044 .052 .080 .046 .052 17 545 .050 .055 .082 .049 .056 18 600 .057 .058 .084 .054 .061 O 19 20 615 630
| |
| .058
| |
| . 06'-
| |
| .061
| |
| .064
| |
| .086
| |
| .088
| |
| .057
| |
| .060
| |
| .064
| |
| .068 21 645 .065 .067 .091 .064 .071 22 700 .067 .070 .093 .067 .074 23 715 .066 .073 .095 .069 .076 24 730 .068 .075 .097 .071 .078 25 745 .068 .077 .098 .073 .079 96 800 .074 .079 .100 .075 .082 27 815 .071 .081 .102 .077 .083 28 830 .0C7 .082 .104 .077 .083 29 845 .072 .083 .105 .078 .083 30 900 .070 .084 .106 .079 .084 31 915 .067 .084 .108 .078 .083 32 930 .067 .085 .109 .078 .083 33 945 .072 .086 .110 .079 .083 34 1000 .068 .086 .111 .079 .083 35 1015 .066 .086 .111 .078 .082 36 1030 .068 .086 .112 .078 .081 37 1045 .075 .087 .113 .079 .082 38 1100 .070 .087 .113 .079 .082 39 1115 .065 .087 .114 .078 .081 40 1130 .066 .086 .114 .077 .080 41 1145 .065 .086 .114 .077 .080 0
| |
| 4
| |
| - - _.___.__m_____
| |
| | |
| . . . .w O
| |
| APPENDIX E l IIRT Plot h W 6ture vs. Time Pressure vs. Time Vapor Pressure vs. Time Air Mass vs. Time Mass Point Isakage Rate vs. Time Total Time Isakage Rate vs. Time O
| |
| O
| |
| | |
| O '
| |
| 9 0
| |
| 1 1
| |
| E T
| |
| A D
| |
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| O 4 APPENDIX F Verification Flow Test Summary Data Report l
| |
| 1 l
| |
| I t
| |
| O l
| |
| l
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| \
| |
| 4 l
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| O
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| I 1
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| , - ARKANSAS NUCLEAR ONE UNIT 1
| |
| | |
| ==SUMMARY==
| |
| DATA ALMAX = .200 VOLUME = 1865000.
| |
| VRATET = .286 VRATEM = .277 TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 1200 1109 527.820 73.4604 .2419 1865000.0 700606.4 1215 1109 527.812 73.4599 .2409 1865000.0 700612.7 1230'1109 527.810 73.4559 .2414 1865000.0 700576.8 1245 1109 527.796 73.4519 .2413 1865000.0 700557.9 1300 1109 527.793 73.4488 .2414 1865000.0 700532.9 1315 1109 527.784 73.4457 .2410 1865000.0 700514.3-1330 1109 527.782 73.4436 .2406 1865000.0 700497.4 1345 1109 527.775 73.4399 .2408 1865000.0 700470.8 1400 1109 527.770 73.4366 .2406 1865000.0 700445.8
| |
| -1415 1109 527.771 73.4337 .2405 1865000.0 700417.7 1430 1109 527.764 73.4301 .2411 1865000.0 700392.2 1445 1109 527.760 73.4282 .2405 1865000.0 700379.2 1500 1109 527.754 73.4249 .2407 1865000.0- 700355.8 1515 1109 527.752 73.4231 .2406 1865000.0 700340.4 1530 1109 527.749 73.4197 .2409 1865000.0 700313.3 1545 1109 527.742 73.4172 .2404 1865000.0 700298.8 1600 1109 527.741 73.4149 .2397 1865000.0 700277.1 1615 1109 521.731 73.4119 .2402 1865000.0 700262.1 1630 1109 527.734 73.4091 .2400 1865000.0 700230.8
| |
| - ('
| |
| 1645 1109 527.731 73.4069 .2391 1865000.0 700215.2 1700 1109 527.723 73.4042 .2399 1865000.0 700199.5 1715 1109 527.719 73.4012 .2399 1865000.0 700175.9 1730 1109 527.722 73.3998 .2392 1865000.0 700159.5 1745 1109 527.717 73.3960 .2400 1865000.0 700130.0 1800 1109 527.713 73.3943 .2392 1865000.0 700118.1 >
| |
| 1815 1109 527.721 73.3921 .2394 1865000.0 700086.8 1830 1109 527.707 73.3891 .2399 1865000.0 700077.3 O
| |
| | |
| O APPENDIX G Verification Flow Test Calculaticos Mass Point Analysis Total Time Analysis i
| |
| O l
| |
| O
| |
| | |
| ARKANSAS NUCLEAR ONE UNIT 1 LEAKAGE RATE -(WEIGHT PERCENT / DAY)
| |
| MASS POINT ANALYSIS TIME AND DATE AT START OF TEST: 1330 1109 1988 TEST DURATION: 5.00 HOURS TIME TEMP PRESSURE CTMT. AIR MASS LOSS AVERAGE MASS (R) (PSIA) MASS (LBM) (LBM) LOSS (LBM/HR)
| |
| --------n-----------------------------------------------------
| |
| 1330 527.782 73.4436 700497.4 1345 527.775 73.4399 700470.8 26.6 '106.4 1400 527.770 73.4366 700445.8 25.0 103.3 1415 527.771 73.4337 700417.7 28.1 106.3 1430 527.764 73.4301 700392.2 25.5 105.2 1445. 527.760 73.4282 700379.2 13.0 94.6 1500 527.754 73.4249 700355.8 23.3 94.4 1515 527.752 73.4231 700340.4 -15.5 89.7 1530 527.749 73.4197 700313.3 27.1 92.1 1545 527.742 73.4172 700298.8 14.6 88.3 1600 527.741 73.4149 700277.1 21.6 88.1 1615 527.731 73.4119 700262.1 15.0 85.6 1630 527.734 -73.4091 700230.8 31.3 88.9 1645 527.731 73.4069 700215.2 15.6 86.8 1700 527.723 73.4042 700199.5 15.7 85.1 0 1715 527.719 1730 527.722 1745 527.717 73.4012 73.3998 73.3960 700175.9 700159.5 700130.0
| |
| ;23.5 16.5 29.5 85.7 84.5 86.5 1800 527.713 73.3943 700118.1 11.9 84.3 1815 527.721 73.3921 700086.8 31.3 86.4 1830 527.707 73.3891 700077.3 9.6 84.0 FREE AIR VOLUME USED (CU. FT.) =1865000.0 REGRESSION LINE INTERCEPT (LBM) = 700485.0 SLOPE (LBM/HR) = -82.6 VERIFICATION TEST LEAKAGE RATE UPPER LIMIT = .327 VERIFICATION TEST LEAKAGE RATE LOWER LIMIT = .227 THE CALCULATED LEAKAGE RATE = .283 l
| |
| - - ____ _ a
| |
| | |
| I ARKANSAS NUCLEAR ONE UNIT 1 LEAKAGE RATE (WEIGHT PERCENT / DAY)
| |
| TOTAL TIME ANALYSIS TIME AND DATE AT START OF TEST: 1330 1109 1988 TEST DURATION: 5.00 HOURS TIME TEMP PRESSURE MEASURED (R) (PSIA) LEAKAGE RATE 1330 527.782 73.4436 1345 527.775 73.4399 .364 1400 527.770 73.4366 .354 1415 527.771 73.4337 .364 1430 527.764 73.4301 .361 1445 527.760 73.4282 .324 1500 527.754 73.4249 .323 1515 527.752 73.4231 .307 1530 527.749 73.4197 .315 1545 527.742 73.4172 .303 1600 527.741 73.4149 .302 1615 -527.731 73.4119 .293 1630 527.734 73.4091 .305 1645 527.731 73.4069 .298 1700 527.723 73.4042 .292 t' T 1715 527.719 73.4012 .294 kl 1730 527.722 73.3998 .289 1745 527.717 73.3960 .296 1800 527.713 73.3943 .289 1815 527.721 73.3921 .296 1830 527.707 73.3891 .288 MEAN OF THE MEASURED LEAKAGE RATES = .313 VERIFICATION TEST LEAKAGE RATE UPPER LIMIT = .336 VERIFICATION TEST LEAKAGE RATE LOWER LIMIT = .236 THE CALCULATED LEAKAGE RATE = .275 l
| |
| O t
| |
| L. - - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _
| |
| | |
| O APPENDIX H Summary Data Sheets l
| |
| l O
| |
| O
| |
| | |
| l i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1945 1108 TEMP 1 = 526.2000 ( 66.530 )
| |
| TEMP 2 = 526.1300 ( 66.460 ) i TEMP 3 = 526.1100 ( 66.440 )
| |
| TEMP 4 = 527.0800 ( 67.410 )'
| |
| TEMP 5 = 527.7600 ( 68.090 )
| |
| TEMP 6 = 527.1800 ( 67.510 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.6700 ( 68.000 )
| |
| TEMP' 9 = 527.7000 ( 68.030 )
| |
| TEMP 10 = 527.7300 ( 68.060 )
| |
| TEMP 11 = 527.7700 ( 68.100 )
| |
| TEMP 12 = 533.3000 ( 73.630 )
| |
| TEMP 13 = 534.0300 ( 74.360 )
| |
| TEMP 14 = 531.3800 ( 71.710 )
| |
| TEMP 15 = 528.2500 ( 68.580 )
| |
| TEMP 16 = 528.4100 ( 68.740 j TEMP 17 = 527.8700 ( 68.200 )
| |
| TEMP 18 = 533.9300 ( 74.260 )
| |
| PRES 1= 73.8120 ( 74347.0 )
| |
| PRES 2= 73.8233 ( 72639.0 )-
| |
| , VPRS 1= .2205 ( 55.840 )
| |
| \ VPRS 2= .2252 ( 56.420 )
| |
| VPRS 3= .2255 ( 56.450 )
| |
| VPRS 4= .2192 ( 55.670 )
| |
| VPRS 5= .2174 ( 55.450 )
| |
| VPRS 6= .3220 ( 66.520 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1945 DATE = 1108 TEMPERATURE (DEGREES R.) = 529.4615 CORRECTED PRESSURE (PSIA) = 73.5781 VAPOR PRESSURE (PSIA) = .2396 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699553.8 1
| |
| l O
| |
| 1 l
| |
| _ - _ _ - - _ _ _ _ - _ _ _ _ _ _ _ - _ _ _ _ _ _ _ O
| |
| | |
| 4 i
| |
| i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2000 1108 i
| |
| 1 TEMP 1 = 526.1900 ( 66.520 )
| |
| TEMP 2 = 526.0900 ( 66.420 )
| |
| TEMP 3 = 526.1100 ( 66.440 )
| |
| TEMP 4 = 527.1400 ( 67.470 )
| |
| TEMP 5 = 527.7600 ( 68.090 )
| |
| TEMP 6 = 527.2000 ( 67.530 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.6900 ( 68.020 )
| |
| TEMP 9 = 527.7000 ( 68.030 )
| |
| TEMP 10 = 527.7300 ( 68.060 )
| |
| TEMP 11 = 527.8000 ( 68.130 )
| |
| TEMP 12 = 532.7700 ( 73.100 )
| |
| TEMP 13 = 533.3500 ( 73.680 )
| |
| TEMP 14 = 531.0900 ( 71.420 )
| |
| TEMP 15 = 528.2000 ( 68.530 )
| |
| TEMP 16 = 528.3800 ( 68.710 )
| |
| TEMP 17 = 527.8300 ( 68.160 )
| |
| TEMP 18 = 533.2000 ( 73.530 )
| |
| PRES 1= 73.7852 ( 74320.0 )
| |
| PRES 2= 73.7980 ( 72614.0 )
| |
| VPRS 1= .2241 ( 56.280 )
| |
| VPRS 2= .2238 ( 56.240 )
| |
| VPRS 3= .2243 ( 56.300 )
| |
| VPRS 4= .2168 ( 55.370 )
| |
| VPRS 5= .2160 ( 55.270 )
| |
| VPRS 6= .3207 ( 66.400 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2000 DATE = 1108 TEMPERATURE (DEGREES R.) = 529.2639 CORRECTED PRESSURE (PSIA) = 73.5530 VAPOR PRESSURE (PSIA) = .2386 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 6C9576.1
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2015 1108 TEMP 1 = 526.2200 ( 66.550 )
| |
| TEMP 2 = 526.1100 ( 66.440 )
| |
| TEMP 3 = 526.1400 ( 66.470 )
| |
| TEMP 4 = 527.2500 ( 67.580 )
| |
| TEMP 5 = 527.7800 ( 68.110 )
| |
| TEMP 6 = 527.2600 ( 67.590 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| 68.050 )
| |
| TEMP 8 = 527.7200 (
| |
| TEMP 9 = 527.7300 ( 68.060 )
| |
| TEMP 10 = 527.7600 ( 68.090 )
| |
| TEMP 11 = 527.8400 ( 68.170 )
| |
| TEMP 12 = 532.3500 ( 72.680 )
| |
| TEMP 13 = 532.8300 ( 73.160 )
| |
| TEMP 14 = 530.8200 ( 71.150 )
| |
| TEMP 15 = 528.1500 ( 68.480 )
| |
| TEMP 16 = 528.3600 ( 68.690 )
| |
| TEMP 17 = 527.8200 ( 68.150 )
| |
| TEMP 18 = 532.6500 ( 72.980 )
| |
| PRES 1= 73.7684 ( 74303.0 )
| |
| PRES 2= 73.7797 ( 72596.0 )
| |
| ( VPRS 1= .2243 ( 56.310 )
| |
| VPRS 2= .2238 ( 56.250 )
| |
| VPRS 3= .2237 ( 56.230 )
| |
| VPRS 4= .2172 ( 55.420 )
| |
| VPRS 5= .2174 ( 55.450 )
| |
| VPRS 6= .3231 ( 66.620 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2015 DATE = 1108 TEMPERATURE (CEGREES R.) = 529.1230 CORRECTED PRESSURE (PSIA) = 73.5347 VAPOR PRESSURE (PSIA) = .2393 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699588.5 O
| |
| | |
| I I
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2030 1108 TEMP 1 = 526.2700 ( 6G.600 )
| |
| TEMP 2 = 526.1700 ( 66.500 )
| |
| TEMP 3 = 526.1700 ( 66.500 )
| |
| TEMP 4 = 527.3100 ( 67.640 )
| |
| TEMP 5 = 527.8300 ( 68.160 )
| |
| TEMP 6 = 527.3500 ( 67.680 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.7600 ( 68.090 )
| |
| TEMP 9 = 527.7500 ( 68.080 )
| |
| TEMP 10 = 527.8100 ( 68.140 )
| |
| TEMP 11 = 527.9000 ( 68.230 )
| |
| TEMP 12 = 531.9900 ( 72.320 )
| |
| TEMP 13 = 532.4100 ( 72.740 )
| |
| TEMP 14 = 530.6400 ( 70.970 )
| |
| TEMP 15 = 528.1100 ( 68.440 )
| |
| TEMP 16 = 528.3100 ( 68.640 )
| |
| TEMP 17 = 527.8200 ( 68.150 )
| |
| TEMP 18 = 532.2400 ( 72.570 )
| |
| PRES 1= 73.7555 ( 74290.0 )
| |
| PRES 2= 73.7675 ( 72584.0 )
| |
| VPRS 1= .2241 ( 56.280 )
| |
| VPRS 2= .7233 ( 56.180 )
| |
| VPRS 3= .2253 ( 56.430 )
| |
| VPRS 4= .2279 ( 55.510 )
| |
| VPRS 5= .2180 ( 55.520 )
| |
| VPRS 6= .3231 ( 66.620 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2030 DATE = 1108 TEMPERATURE (DEGREES R.) = 529.0178 CORRECTED PRESSURE (PSIA) = 73.5218 VAPOR PRESSURE (PSIA) = .2397 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699604.6 O
| |
| | |
| STIMMARY OF MEASURED DATA AT 2045 1108 TEMP 1 = 526.3100 ( 66.640 )
| |
| TEMP 2 = 526.2100 ( 66.540 )
| |
| TEMP 3 = 526.1900 ( 66.520 )
| |
| TEMP 4 = 527.3600 ( 67.690 )
| |
| TEMP 5 = 527.8600 ( 68.190 )
| |
| TEMP 6 = 527.4100 ( 67.740 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.8000 ( 68.130 )
| |
| TEMP 9 = 527.8100 ( 68.140 )
| |
| TEMP 10 = 527.8600 ( 68.190 )
| |
| TEMP 11 = 527.9400 ( 68.270 )
| |
| TEMP 12 = 531.7100 ( 72.040 )
| |
| TEMP 13 = 532.1000 ( 72.430 )
| |
| TEMP 14 = 530.4500 ( 70.780 )
| |
| TEMP 15 = 528.0700 ( 68.400 )
| |
| TEMP 16 = 528.2600 ( 68.590 )
| |
| TEMP 17 = 527.8400 ( 68.170 )
| |
| TEMP 18 = 531.8800 ( 72.210 )
| |
| PRES 1= 73.7455 ( 74280.0 )
| |
| PRES 2= 73.7574 ( 72574.0 )
| |
| ( VPRS VPRS 1=
| |
| 2=
| |
| .2238
| |
| .2235
| |
| (
| |
| (
| |
| 56.240 )
| |
| 56.210 )
| |
| VPRS 3= .2255 ( 56.450 )
| |
| VPRS 4= .2178 ( 55.500 )
| |
| VPRS 5= .2157 ( 55.230 )
| |
| VPRS 6= .3216 ( 66.480 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2045 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.9306 CORRECTED PRESSURE (PSIA) = 73.5124 VAPOR PRESSURE (PSIA) = .2390 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699630.8 O
| |
| | |
| i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2100 1108 TEMP 1 = 526.3300 ( 66.660 )
| |
| TEMP 2 = 526.2600 ( 66.590 )
| |
| TEMP 3 = 526.2200 ( 66.550 )
| |
| TEMP 4 = 527.4300 ( 67.760 )
| |
| TEMP 5 = 527.8800 ( 68.210 )
| |
| TEMP 6 = 527.4600 ( 67.790 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.8400 ( 68.170 )
| |
| TEMP 9 = 527.8300 ( 68.160 )
| |
| TEMP 10 = 527.8900 ( 68.220 )
| |
| TEMP 11 = 527.9800 ( 68.310 )
| |
| TEMP 12 = 531.4700 ( 71.800 )
| |
| TEMP 13 = 531.8300 ( 72.160 )
| |
| TEMP 14 = 530.3000 ( 70.630 )
| |
| TEMP 15 = 528.0400 ( 68.370 )
| |
| TEMP 16 = 528.2400 ( 68.570 )
| |
| TEMP 17 = 527.8700 ( 68.200 )
| |
| TEMP 18 = 531.6100 ( 71.940 ) h PRES 1= 73.7366 ( 74271.0 )
| |
| PRES 2= 73.7482 ( 72565.0 )
| |
| VPRS 1= .2237 ( 56.230 )
| |
| VPRS 2= .2237 ( 56.230 )
| |
| VPRS 3= .2251 ( 56.400 )
| |
| VPRS 4= .2183 ( 55.560 )
| |
| VPRS 5= .2167 ( 55.350 )
| |
| VPRS 6= .3193 ( 66.280 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2100 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.8641 CORRECTED PRESSURE (PSIA) = 73.5036 VAPOR PRESSURE (PSIA) = .2388 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699634.6 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2115 1108 TEMP 1 = 526.3600 ( 66.690 )
| |
| TEMP 2 = 526.3000' (- 66.630 )
| |
| TEMP 3.= 526.2500 ( 66.580~)
| |
| TEMP 4 =~527.4700 ( 67.800 )
| |
| TEMP. 5-= 527.9100 ( 68.240 )
| |
| TEMP 6 = 527.4900 ( 67.820 )
| |
| TEMP 7 ='536.4400 ( 76.770 )
| |
| TEMP 8 = 527.8600 ( 68.190 )
| |
| TEMP. 9 = 527.8600 ( 68.190-) >
| |
| TEMP 10 = 527.9200 ( 68.250 )
| |
| TEMP 11 = 528.0200 ( 68.350-)
| |
| TEMP 12 = 531.2800 ( 71.610 }
| |
| TEMP 13 = 531.6000 ( 71.930 )
| |
| TEMP 14 = 530.1600 ( 70.490 )
| |
| TEMP 15 = 528.0200 ( 68.350 )
| |
| TEMP 16 = 528.2100 ( 68.540 )
| |
| TEMP 17 = 527.8900 ( 68.220 )
| |
| TEMP'18 = 531.3900 (. 71.720 )
| |
| PRES 1= 73.7297 ( 74264.0 )
| |
| PRES 2= 73.7411 ( 72558.0 )
| |
| ) VPRS VPRS 1=
| |
| 2=
| |
| .2239
| |
| .2219
| |
| (
| |
| (
| |
| 56.260 )
| |
| 56.010 )
| |
| VPRS- 3= .2254 ( 56.440 )
| |
| VPRS 4= .2184 ( 55.570 )
| |
| VPRS 5= .2162 ( 55.290 )
| |
| VPRS 6= .3197 ( 66.310 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2115 DATE = 1108 l TEMPERATURE-(DEGREES R.) = 528.8071 CORRECTED PRESSURE (PSIA) = 73.4968 VAPOR PRESSURE (PSIA) = .2386 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699645.3 0
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2130 1108 TEMP 1 = 526.4000 ( 66.730 )
| |
| TEMP 2 = 526.3400 ( 66.670 )
| |
| TEMP 3 = 526.2700 ( 66.600 )
| |
| TEMP 4 = 527.5100 ( 67.840 )
| |
| TEMP 5 = 527.9200 ( 68.250 )
| |
| TEMP 6 = 527.5500 ( 67.880 ) l TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.9000 ( 68.230 )
| |
| TEMP 9 = 527.9000 ( 68.230 ) ,
| |
| TEMP 10 = 527.9700 ( 68.300 ) l 68.390 )
| |
| TEMP 11 = 528.0600 (
| |
| TEMP 12 = 531.1100 ( 71.440 )
| |
| TEMP 13 = 531.4100 ( 71.740 )
| |
| 70.350 )
| |
| TEMP 14 = 530.0200 (
| |
| TEMP 15 = 528.0100 ( 68.340 )
| |
| TEMP 16 = 528.2000 ( 68.530 )
| |
| TEMP 17 = 527.9000 ( 68.230 )
| |
| TEMP 18 = 531.2100 ( 71.540 ) ;
| |
| PRES 1= 73.7227 ( 74257.0 )
| |
| PRES 2= 73.7350 ( 72552.0 )
| |
| VPRS 1= .2235 ( 56.210 )
| |
| VPRS 2= .2248 ( 56.370 )
| |
| VPRS 3= .2257 ( 56.480 )
| |
| VPRS 4 = .2179 ( 55.510 )
| |
| VPRS 5= .2139 ( S5.000 )
| |
| VPRS 6= .3200 ( 66.340 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2130 DATE = 1108 i TEMPERATURE (DEGREES R.) = 528.7627 l CORRECTED PRESSURE (PSIA) = 73.4902 VAPOR PRESSURE (PSIA) = .2387
| |
| , VOLUME (CU.FT.) = 1865000.0 l AIR MASS (LBM) = 699641.3 l
| |
| O 1
| |
| l __ ________-_-__L
| |
| | |
| . (~T
| |
| ''t) -
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2145 1108 TEMP 1 = 526.4200 ( 66.750 )
| |
| TEMP 2 = 526.3800 ( 66.710 )
| |
| TEMP 3 = 526.2900 ( 66.620 )
| |
| TEMP 4 = 527.5600 ( 67.890 )
| |
| TEMP 5 = 527.9600 ( 68.290 )
| |
| TEMP 6 = 527.5700 ( 67.900 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.9000 ( 68.230 )
| |
| TEMP 9 = 527.9000 ( 68.230 )
| |
| TEMP 10 = 527.9800 ( 68.310 )
| |
| TEMP 11 = 528.0800 ( 68.410 )
| |
| TEMP 12 = 530.9600 ( 71.290 )
| |
| TEMP 13 = 531.2300 ( 71.560 )
| |
| TEMP 14 = 529.9000 ( 70.230 )
| |
| TEMP 15 = 528.0100 ( 68.340 )
| |
| TEMP 16 = 528.1900 ( 68.520 )
| |
| TEMP 17 = 527.9400 ( 68.270 )
| |
| TEMP 18 = 531.0100 ( 71.340 )'
| |
| PRES 1= 73.7177 ( 74252.0 )
| |
| PRES 2= 73.7299 ( 72547.0 )
| |
| VPRS 1= .2241 ( 56.280 )
| |
| VPRS 2= .2238 ( 56.240 )
| |
| VPRS 3= .2252 ( 56.420 )
| |
| VPRS 4= .2177 ( 55.480 )
| |
| VPRS 5= .2128 ( 54.860 )
| |
| VPRS 6= .3175 ( 66.110 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2145 DATE = 1108 l
| |
| TEMPERATURE (DEGREES R.) = 528.7183 CORRECTED PRESSURE (PSIA) = 73.4861 VAPOR PRESSURE (PSIA) = .2378 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699660.7 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2200 1108 TEMP 1 = 526.4400 ( 66.770 )
| |
| TEMP 2 = 526.4100 ( 66.740 )
| |
| TEMP 3 = 526.3100 ( 66.640 )
| |
| TEMP 4 = 527.5900 ( 67.920 )
| |
| TEMP 5 = 527.9600 ( 68.290 )
| |
| TEMP 6 = 527.6100 ( 67.940 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.9500 ( 68.280 )
| |
| TEMP 9 = 527.9200 ( 68.250 )
| |
| TEMP 10 = 528.0100 ( 68.340 )
| |
| TEMP 11 = 528.1100 ( 68.440 )
| |
| TEMP 12 = 530.7800 ( 71.110 )
| |
| TEMP 13 = 531.0900 ( 71.420 )
| |
| TEMP 14 = 529.7800 ( 70.110 )
| |
| TEMP 15 = 528.0100 ( 68.340 )
| |
| TEMP 16 = 528.1600 ( 68.490 )
| |
| TEMP 17 = 527.9600 ( 68.290 )
| |
| TEMP 18 = 530.8500 ( 71.180 )
| |
| PRES 1= 73.7128 ( 74247.0 )
| |
| PRES 2= 73.7249 ( 72542.0 )
| |
| VPRS 1= .2236 ( 56.220 )
| |
| VPRS 2= .2240 ( 56.270 )
| |
| VPRS 3= .2266 ( 56.590 )
| |
| VPRS 4= .2187 ( 55.610 )
| |
| VPRS 5= .2155 ( 55.200 )
| |
| VPRS 6= .3157 ( 65.950 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2200 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.6767 CORRECTED PRESSURE (PSIA) = 73.4805 VAPOR PRESSURE (PSIA) = .2384 VOLUME (CU.FT.) = 1865000.0
| |
| ; AIR MASS (LBM) = 699662.5 1
| |
| 0
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2215 1108 TEMP 1 = 526.4600 ( 66.790 )
| |
| TEMP 2 = 526.4300 ( 66.760 )
| |
| TEMP 3 = 526.3300 ( 66.660 )
| |
| TEMP 4 = 527.6100 ( 67.940 )
| |
| TEMP 5 = 527.9800 ( 68.310 )
| |
| TEMP 6 = 527.6400 ( 67.970 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 527.9800 ( 68.310 )
| |
| TEMP 9 = 527.9600 ( 68.290 )
| |
| TEMP 10 = 528.0300 ( 68.360 )
| |
| TEMP 11 = 528.1300 ( 68.460 )
| |
| TEMP 12 = 530.6300 ( 70.960 )
| |
| TEMP 13 = 530.9200 ( 71.250 )
| |
| TEMP 14 = 529.6800 ( 70.010 )
| |
| TEMP 15 = 528.0200 ( 68.350 )
| |
| TEMP 16 = 528.1600 ( 68.490 )
| |
| TEMP 17 = 527.9900 ( 68.320 )
| |
| TEMP 18 = 530.7100 ( 71.040 )
| |
| PRES 1= 73.7078 ( 74242.0 )
| |
| PRES 2= 73.7198 ( 72537.0 )
| |
| () VPRS VPRS 1=
| |
| 2=
| |
| .2240
| |
| .2237
| |
| (
| |
| (
| |
| 56.270 )
| |
| 56.230 )
| |
| VPRS 3= .2266 ( 56.590 )
| |
| VPRS 4= .2188 ( 55.620 )
| |
| VPRS 5= .2131 ( 54.890 )
| |
| VPRS 6= .3188 ( 66.230 )
| |
| l
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2215 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.6415 l CORRECTED PRESSURE (PSIA) = 73.4753 VAPOR PRESSURE (PSIA) = .2385 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699660.0 0
| |
| | |
| l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2230 1108 TEMP 1 = 526.4800 ( 66.810 )
| |
| TEMP 2 = 526.4600 ( 66.790 )
| |
| TEMP 3 = 526.3500 ( 66.680 )
| |
| TEMP 4 = 527.6300 ( 67.960 )
| |
| TEMP 5 = 527.9900 ( 68.320 )
| |
| TEMP 6 = 527.6700 ( 68.000 )
| |
| TEMP 7 = 536.4400 ( 76.770 ) -
| |
| TEMP 8 = 528.0000 ( 68.330 )
| |
| TEMP 9 = 527.9800 ( 68.310 )
| |
| TEMP 10 = 528.0600 ( 68.390 )
| |
| TEMP 11 = 528.1500 ( 68.480 )
| |
| TEMP 12 = 530.5300 ( 70.860 ) l TEMP 13 = 530.8100 ( 71.140 ) l TEMP 14 = 529.5900 ( 69.920 ) i TEMP 15 = 528.0200 ( 68.350 ) t TEMP 16 = 528.1500 ( 68.480 )
| |
| TEMP 17 = 527.9800 ( 68.310 )
| |
| TEMP 18 = 530.5800 ( 70.910 )
| |
| PRES 1= 73.7029 ( 74237.0 )
| |
| PRES 2= 73.7157 ( 72533.0 )
| |
| VPRS 1= .2241 ( 56.280 )
| |
| VPRS 2= .2244 ( 56.320 ) l VPRS 3= .2262 ( 56.540 )
| |
| VPRS 4= .2185 ( 55.580 ) !
| |
| VPRS 5= .2135 ( 54.950 )
| |
| VPRS 6= .3151 ( 65.890 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2230 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.6115 CORRECTED PRESSURE (PSIA) = 73.4714 VAPOR PRESSURE (PSIA) = .2379 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699662.4 1
| |
| l
| |
| | |
| (,
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2245 1108 TEMP 1.= 526.5000 ( 66.830 )
| |
| TEMP 2 = 526.4700 ( 66.800 )
| |
| TEMP 3 = 526.3600 ( 66.690 )
| |
| TEMP 4 = 527.6700 ( 68.000 )
| |
| TEMP 5 = 528.0200 ( 68.350 )
| |
| TEMP 6 = 527.7100 ( 68.040 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0000 ( 68.330 )
| |
| TEMP 9 = 528.0000 ( 68.330 )
| |
| TEMP 10 = 528.0800 ( 68.410 )
| |
| TEMP 11 = 528.1700 ( 68.500 )
| |
| TEMP 12 = 530.4100 ( 70.740 )
| |
| TEMP 13 = 530.6700 ( 71.000 )
| |
| TEMP 14 = 529.5200 ( 69.850 )
| |
| TEMP 15 = 528.0200 ( 68.350 )
| |
| TEMP 16 = 528.1400 ( 68.470 )
| |
| TEMP 17 = 528.0000 ( 68.330 )
| |
| TEMP 18 = 530.4600 ( 70.790 )
| |
| PRES 1= 73.6989 ( 74233.0 )
| |
| PRES 2= 73.7117 ( 72529.0 )
| |
| \- ) VPRS 1= .2238 ( 56.250 )
| |
| VPRS 2= .2245 ( 56.330 )
| |
| VPRS 3= .2272 ( 56.660 )
| |
| VPRS 4= .2187 ( 55.610 )
| |
| VPRS 5= .2151 ( 55.150 )
| |
| VPRS 6= .3153 ( 65.910 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2245 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.5825 CORRECTED PRESSURE (PSIA) = 73.4669 VAPOR PRESSURE (PSIA) = .2384 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699657.6 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2300 1108 l j
| |
| TEMP 1 = 526.5400 ( 66.870 )
| |
| TEMP 2 = 526.5000 ( 66.830 )
| |
| TEMP 3 = 526.3900 ( 66.720 )
| |
| TEMP 4 = 527.6900 ( 68.020 )
| |
| TEMP 5 = 528.0200 ( 68.350 )
| |
| TEMP 6 = 527.7200 ( 68.050 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0300 ( 68.360 )
| |
| TEMP 9 = 528.0100 ( 68.340 )
| |
| TEMP 10 = 528.1000 ( 68.430 )
| |
| TEMP 11 = 528.1900 ( 68.520 ) )
| |
| TEMP 12 = 530.3000 ( 70.630 )
| |
| TEMP 13 = 530.5700 ( 70.900 )
| |
| TEMP 14 = 529.4400 ( 69.770 )
| |
| TEMP 15 = 528.0100 ( 68.340 )
| |
| TEMP 16 - 528.1300 ( 68.460 )
| |
| TEMP 17 = 528.0200 ( 68.350 )
| |
| TEMP 18 = 530.3300 ( 70.660 )
| |
| PRES 1= 73.6949 ( 74229.0 )
| |
| PRES 2= 73.7076 ( 72525.0 )
| |
| VPRS 1= .2241 ( 56.280 )
| |
| VPRS 2= .2242 ( 56.290 )
| |
| VPRS 3= .2268 ( 56.610 )
| |
| VPRS 4= .2187 ( 55.610 )
| |
| VPRS 5= .2163 ( 55.310 )
| |
| VPRS 6= .3157 ( 65.950 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2300
| |
| , DATE = 1108 TEMPERATURE (DEGREES R.) = 528.5544 CORRECTED PRESSURE (PSIA) = 73.4626 VAPOR PRESSURE (PSIA) = .2386 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 699654.6 9
| |
| | |
| l l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 231B 1108 TEMP 1'= 526.5600 ( 66.890 )
| |
| TEMP 2 = 526.5300 ( 66.860 )
| |
| TEMP .3 = 526.4100 ( 66.740.)
| |
| TEMP 4 = 527.7100 ( 68.040-)
| |
| TEMP 5 = 528.0400 ( 68.370 )
| |
| TEMP '6 = 527.7400 ( 68.070 )
| |
| . TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0700 ( 68.400 )
| |
| TEMP 9 = 528.0300 ( 68.360 )
| |
| TEMP 10 = 528'1300 . ( 68.460 )
| |
| TEMP 11.= 528.2200 ( 68.550.}
| |
| TZMP 12 = 530.2000 ( 70.530 )
| |
| TEMP la = 530.4500 ( 70.780 )
| |
| TEMP 14 = 529.3700 (. 69.700 )
| |
| TEMP 15 = 528.0200 ( 68.350 )
| |
| TEMP 16 =.528.1300- ( 68.460 )
| |
| TEMP-17 = 528.0400 ( 68.370 )
| |
| TEMP 18 = 530.2300 ( 70.560 )
| |
| PRES 1= 73.7168 ( 74251.0 )
| |
| PRES 2= 73.7259 ( 72543.0 )
| |
| VPRS 1= .2244 ( 56.320 )
| |
| VPRS 2= .2238 ( 56.250 )
| |
| VPRS 3= .2272 ( 56.660 )
| |
| VPRS 4= .2188 ( 55.620 )
| |
| VPRS 5= .2140 ( 55.010 )
| |
| VPRS 6= .3179 ( 66.150 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2315 DATE = 1108 TEMPERATURE (DEGREES R. ' ~ 528.5331 CORRECTED PRESSURE (PSIA, 73.4826 VAPOR PRESSURE (PSIA) = .2387 VOLUME (CU.FT;.) = 1865000.0 AIR MASS /' tH) = 699873.4 O
| |
| | |
| \ l l
| |
| l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2330 1108 TEMP 1 = 526.6800 ( 67.010 ) >
| |
| TEMP 2 = 526-6400 ( 66.970 )
| |
| TEMP 3 = 52 .5400 ( 66.870 )
| |
| TEMP 4 = 527.8500 ( 68.180 )
| |
| TEMP 5 = 528.1700 ( 68.500 ) ]
| |
| TEMP 6 = 527.8800 ( 68.210 ) 1 TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.2300 ( 68.560 )
| |
| TEMP 9 = 528.1900 ( 68.520 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3500 ( 68.680 ) l TEMP 12 = 530.2700 ( 70.600 ) l TEMP 13 = 530.5500 ( 70.880 )
| |
| TEMP 14 = 529.4800 ( 69.810 )
| |
| TEMP 15 = 528.2200 ( 68.550 )
| |
| TEMP 16 = 528.3400 ( 68.670 )
| |
| TEMP 17 = 528.2300 ( 68.560 )
| |
| TEMP 18 = 530.3400 ( 70.670 )
| |
| PRES 1= 73.8378 ( 74373.0 )
| |
| PRES 2= 73.8487 ( 72664.0 )
| |
| VPRS 1= .2234 ( 56.190 )
| |
| VPRS 2= .2250 ( 56.390 )
| |
| VPRS 3= .2274 ( 56.680 )
| |
| VPRS 4= .2198 ( 55.750 ) 1 VPRS 5= .2144 ( 55.060 )
| |
| VPRS 6= .3135 ( 65.750 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2330 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.6731 CORRECTED PRESSURE (PSIA) = 73.6050 VAPOR PRESSURE (PSIA) = .2382 VOLUME (CU.FT.) = 1865000.0 l AIR MASS (LBM) = 700853.4 h
| |
| l L___-_______
| |
| | |
| i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 2345 1108 TEMP 1 = 526.6200 ( 66.950 )
| |
| TEMP 2 = 526.5900 ( 66.920 )
| |
| TEMP 3 = 526.5000 ( 66.830 )
| |
| TEMP 4 = 527.8100 ( 68.140 )
| |
| TEMP 5 = 528.1500 .( 68.480 )
| |
| TEMP 6 = 527.8300 ( 68.160 )
| |
| TEMP 7 = 536.4400- '( 76.770 )
| |
| TEMP 8 = 528.2000 (~'68.530 )
| |
| TEMP .9 = 528.1500 ( 68.480 )
| |
| TEMP 10 = S28.2200 ( 68.550 )
| |
| TEMP 11 = 528.3000 ( 68.630 )
| |
| TEMP 12 = 530.1500 ( 70.480 )
| |
| TEMP 13 = 530.4300 ( -70.760 )
| |
| TEMP 14 = 529.4200 ( 69.750 )
| |
| TEMP 15 =-528.2200 ( 68.550 )
| |
| TEMP 16 = 528.3500 ( 68.680 )
| |
| TEMP 17 = 528.2000 ( 68;530 )
| |
| TEMP 18 = 530.2000 ( 70.530 )
| |
| PRES 1= 73.8259 ( 74361.0.)
| |
| PRES 2= 73.8365 ( 72652.0 )
| |
| -( VPRS VPRS
| |
| : 1. =
| |
| 2'=
| |
| .2246
| |
| .2247
| |
| (
| |
| (
| |
| 56.340 )
| |
| 56.350 )
| |
| VPRS 3= .2270 ( 56.640 )
| |
| VPRS 4= .2190 ( 55.650 )
| |
| VPRS 5= .2132 ( 54.910 )
| |
| VPRS 6= .3123 ( 65.640 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 2345 DATE = 1108 TEMPERATURE (DEGREES R.) = 528.6165 CORRECTED PRESSURE (PSIA) = 73.5935
| |
| = .2377 VAPOR PRESSURE (PSIA)
| |
| VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700818.9 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 0 1109 TEMP 1 = 526.6100 ( 66.940 )
| |
| TEMP 2 = 526.5800 ( 66.910 )
| |
| TEMP 3 = 526.4700 ( 66.800 )
| |
| TEMP 4 = 527.8000 ( 68.130 )
| |
| TEMP 5 = 528.1400 ( 68.470 )
| |
| TEMP 6 = 527.8200 ( 68.150 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1500 ( 68.480 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2100 ( 68.540 )
| |
| TEMP 11 = 528.3000 ( 68.630 )
| |
| TEMP 12 = 530.0500 ( 70.380 )
| |
| TEMP 13 = 530.2800 ( 70.610 )
| |
| TEMP 14 = 529.3300 ( 69.6CO )
| |
| TEMP 15 = 528.1700 ( 68.500 )
| |
| TEMP 16 = 528.3100 ( 68.640 )
| |
| TEMP 17 = 528.1500 ( 68.480 )
| |
| TEMP 18 = 530.0600 ( 70.390 )
| |
| PRES 1= 73.8180 ( 74353.0 )
| |
| PRES 2= 73.8294 ( 72645.0 )
| |
| VPRS 1= .2244 ( 56.320 )
| |
| VPRS 2= .2249 ( 56.380 )
| |
| VPRS 3= .2275 ( 56.700 )
| |
| VPRS 4= .2193 ( 55.690 )
| |
| VPRS 5= .2174 ( 55.440 )
| |
| VPRS 6= .3119 ( 65.600 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 0 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.5563 CORRECTED PRESSURE (PSIA) = 73.5852 VAPOR PRESSURE (PSIA) = .2385 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700819.1 1
| |
| | |
| 1.
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 15 1109 TEMP 1 = 526;6200 ( 66.950 )
| |
| TEMP 2 = 526.6000 ( 66.930 )
| |
| TEMP 3 = 526.4700 ( 66.800 )
| |
| TEMP 4 = 527.8100 ( 68.140 )
| |
| TEMP 5 = 528.1500 ( 68.480 )
| |
| TEMP 6 = 527.8400 ( 68.170 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1500 ( 68.480 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2100 ( 68.540 )
| |
| TEMP 11 = 528.3000 ( 68.630 )
| |
| TEMP 12 = 529.9200 ( 70.250 )
| |
| TEMP 13 = 530.1600 ( 70.490 )
| |
| TEMP 14 = S29.2500 ( 69.580 ) '
| |
| TEMP.15 = 528.1400 ( 68.470 )
| |
| TEMP 16 = 528.2800 ( 68.610 )
| |
| TEMP 17 = 528.1300 ( 68.460 )
| |
| TEMP 18 = 529.9300 ( 70.260 )
| |
| PRES 1= 73.8110 ( 74346.0 )
| |
| PRES 2= 73.8233 ( 72639.0 )
| |
| ( VPRS 1= .2248 ( 56.370 )
| |
| VPRS 2= .2250 ( 56.390 )
| |
| VPRS 3= .2279 ( 56.750 )
| |
| VPRS 4= .2193 ( 55.690 )
| |
| VPRS 5= .2177 ( 55.480 ).
| |
| VPRS 6= .3118 ( 65.590 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRETED DATA TIME = 15 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.5123 CORRECTED PRESSURE (PSIA) = 73.5785 VAPOR PRESSURE (PSIA) = .2387 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700813.7 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 30 1109 l
| |
| TEMP 1 = 526.6400 ( 66.970 )
| |
| TEMP 2 = 526.6100 ( 66.940 )
| |
| TEMP 3 = 526.4600 ( 66.790 )
| |
| TEMP 4 = 527.8000 ( 68.130 )
| |
| TEMP 5 = 528.1300 ( 68.460 )
| |
| TEMP 6 = 527.8400 ( 68.170 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1500 ( 68.480 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2100 ( 68.540 )
| |
| TEMP 11 = 528.3000 ( 68.630 )
| |
| TEMP 12 = 529.8300 ( 70.160 )
| |
| TEMP 13 = 530.0500 ( 70.380 )
| |
| TEMP 14 = 529.1500 ( 69.480 )
| |
| TEMP 15 = 528.1100 ( 68.440 )
| |
| TEMP 16 = 528.2500 ( 68.580 )
| |
| TEMP 17 = 528.1200 ( 68.450 )
| |
| TEMP 18 = 529.8200 ( 70.150 )
| |
| PRES 1= 73.8061 ( 74341.0 )
| |
| PRES 2= 73.8183 ( 72634.0 )
| |
| VPRS 1= .2249 ( 56.380 )
| |
| VPRS 2= .2258 ( 56.490 )
| |
| VPRS 3= .2276 ( 56.710 )
| |
| VPRS 4= .2201 ( 55.780 )
| |
| VPRS 5= .2167 ( 55.350 )
| |
| VPRS 6= .3117 ( 65.580 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 30 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.4699 CORRECTED PRESSURE (PSIA) = 73.5735 VAPOR PRESSURE (PSIA) = .2387 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700822.1 O
| |
| | |
| I f
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 45 1109 TEMP 1 = 526.6500 ( 66.1$80 )
| |
| TEMP 2 = 526.6200 ( 66.950 )
| |
| TEMP 3 = 526.4800 ( C6.810 )
| |
| TEMP. 4 = 527.8100 ( 68.140-)
| |
| TEMP 5 = 528.1300 ( 68.460 )-
| |
| TEMP 6 = 527.8500 ( 68.180 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 (- 68.450 )
| |
| TEMP 10.= 528.2200 ( 68.550-)
| |
| TEMP 11 = 528.3000 ( 68.630 )
| |
| TEMP 12 = 529.7300 ( 70.060 )
| |
| TEMP-13 = 529.9600 ( 70.290 )
| |
| TEMP 14 = 529.0700 ( 69.400')
| |
| TEMP 15 = 528.0900 ( 68.420 )
| |
| TEMP 16 = 528.2300 ( 68.560 )
| |
| TEMP 17 = 528.1200 ( 68.450 )
| |
| TEMP 18 = 529.7200 ( 70.050 )
| |
| PRES 1= 73.8011 ( 74336.0 )
| |
| PRES 2= 73.8142 ( 72630.0 )
| |
| [#
| |
| \~
| |
| VPRS VPRS 1=
| |
| 2=
| |
| .2255. (
| |
| .2244 (
| |
| 56.450 )
| |
| 56.320 )
| |
| VPRS 3= .2280 ( 56.760 )
| |
| VPRS 4= .2201 ( 55.790 )
| |
| VPRS 5= .2163 ( 55.300 )
| |
| VPRS 6= .3106 ( 65.480 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 45 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.4382 CORRECTED PRESSURE (PSIA) = 73.5693 VAPOR PRESSURE (PSIA) =
| |
| .2384 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700824.4 C.
| |
| | |
| l l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 100 1109 l
| |
| TEMP 1 = 526.6700 ( 67.000 ) J 66.970 )
| |
| TEMP 2 = 526.6400 (
| |
| TEMP 3 = 526.5200 ( 66.850 )
| |
| TEM,P. 4 = 527.8100 ( 68.140 )
| |
| TEMP 5 = 528.1300 ( 68.460 )
| |
| TEMP 6 = 527.8600 ( 68.190 ) !
| |
| l TEMP 7 = 336.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2200 ( 68.550 )
| |
| TEMP 11 = 528.3300 ( 68.660 )
| |
| TEMP 12 = 529.6600 ( 69.990 )
| |
| TEMP 13 = 529.8600 ( 70.190 )
| |
| TEMP 14 = 529.0100 ( 69.340 )
| |
| TEMP 15 = 528.0700 ( 68.400 )
| |
| TEMP 16 = 528.2000 ( 68.530 )
| |
| TEMP 17 = 528.1300 ( 68.460 )
| |
| TEMP 18 = 529.6400 ( 69.970 )
| |
| PRES 1= 73.7971 ( 74332.0 )
| |
| PRES 2= 73.8102 ( 72626.0 )
| |
| VPRS 1= .2252 ( 56.420 )
| |
| VPRS 2= .2260 ( 56.520 )
| |
| VPRS 3= .2274 ( 56.690 )
| |
| VPRS 4= .2201 ( 55.790 )
| |
| VPRS 5= .2162 ( 55.290 )
| |
| VPRS 6= .3084 ( 65.280 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 100 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.4136 CORRECTED PRESSURE (PSIA) = 73.5655 VAPOR PRESSURE (PSIA) = .2381 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700821.3 O
| |
| i
| |
| _ _ _ - _ - _ _ _ _ - a
| |
| | |
| I i
| |
| G Q
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 115 1109 TEMP 1 = 526.6700 ( 67.000 )
| |
| TEMP 2 = 526.6400 ( 66.970 )
| |
| TEMP 3 = 526.5400 ( 66.870 )
| |
| TEMP 4 = 527.8300 ( 68.160 )
| |
| TEMP 5 = 528.1400 ( 68.470 )
| |
| TEMP 6 = 527.8700 ( 68.200 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2300 ( 68.560 )
| |
| TEMP 11 = 523.3300 ( 68.660 )
| |
| TEMP 12 = 529.5800 ( 69.910 )
| |
| TEMP 13 = 529.7800 ( 70.110 )
| |
| TEMP 14 = 528.9400 ( 69.270 )
| |
| TEMP 15 = 528.0700 ( 68.400 )
| |
| TEMP 16 = 528.1700 ( 68.500 )
| |
| TEMP 17 = 528.1300 ( 68.460 )
| |
| TEMP 18 = 529.5500 ( 69.880 )
| |
| PRES 1= 73.7932 ( 74328.0 )
| |
| PRES 2= 73.8051 ( 72621.0 )
| |
| VPRS 1-= .2256 ( 56.460 )
| |
| s/ VPRS 2= .2240 ( 56.270 )
| |
| VPRS 3= .2279 ( 56.750 )
| |
| VPRS 4= .2205 ( 55.830 )
| |
| VPRS 5= .2161 ( 55.280 )
| |
| VPRS 6= .3073 ( 65.170 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 115 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.3870 CORRECTED PRESSURE (PSIA) = 73.5614 VAPOR PRESSURE (PSIA) = .2377 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700817.0 l
| |
| O l l l
| |
| l _-__--_- _ _
| |
| | |
| i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 130 1109 TEMP 1 = 526.6800 ( 67.010 )
| |
| TEMP 2 = 526.6500 ( 66.980 )
| |
| TEMP 3 = 526.5400 ( 66.870 )
| |
| TEMP 4 = 527.8300 ( 68.160 )
| |
| TEMP 5 = 528.1300 ( 68.460 )
| |
| Ti'MP 6 = 527.8700 ( 68.200 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2300 ( 68.560 )
| |
| TEMP 11 = 528.3300 ( 68.660 )
| |
| TEMP 12 = 529.5100 ( 69.840 )
| |
| TEMP 13 = 529.6900 ( 70.020 )
| |
| TEMP 14 = 528.8900 ( 69.220 )
| |
| TEMP 15 = 528.0300 ( 68.360 )
| |
| TEMP 16 = 528.1500 ( 68.480 )
| |
| TEMP 17 = 528.1300 ( 68.460 )
| |
| TEMP 18 = 529.4600 ( 69.790 )
| |
| PRES 1= 73.7892 ( 74324.0 )
| |
| PRES 2= 73.8010 ( 72617.0 )
| |
| VPRS 1= .2259 ( 56.500 )
| |
| VPRS 2= .2252 ( 56.420 )
| |
| VPRS 3= .2286 ( 56.830 )
| |
| VPRS 4= .2205 ( 55.830 )
| |
| VPRS 5= .2151 ( 55.150 )
| |
| VPRS 6= .3073 ( 65.170 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 130 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.3558 CORRECTED PRESSURE (PSIA) = 73.5572 VAPOR PRESSURE (PSIA) = .2379 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700818.4 l
| |
| l
| |
| _ _ _____U
| |
| | |
| p
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 145 1109 TEMP 1 = 526.7000 ( 67.030 )
| |
| TEMP 2 = 526.6500 ( 66.980 )
| |
| TEMP 3 = 526.5600 ( 66.890 )
| |
| TEMP 4 = 527.8300 ( 68.160 )
| |
| TEMP 5 = 528.1300 ( 68.460 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2400 ( 68.570 )
| |
| TEMP 11 = 528.3400 ( 68.670 )
| |
| TEMP 12 = 529.4300 ( 69.760 )
| |
| TEMP 13 = 529.6300 ( 69.960 )
| |
| TEMP 14 = 528.8200 ( 69.150 )
| |
| TEMP 15 = 528.0600 ( 68.390 )
| |
| TEMP 16 = 528.1400 ( 68.470 )
| |
| TEMP 17 = 528.1300 ( 68.460 ) i TEMP 18.= 529.4000 ( 69.730 ) '
| |
| PRES 1= 73.7852 ( 74320.0 )
| |
| PRES 2= 73.7980 ( 72614.0 )
| |
| ( VPRS 1= .2260 ( 56.520 )
| |
| \ VPRS 2= .2257 ( 56.480 )
| |
| VPRS 3= .2290 ( 56.880 )
| |
| VPRS 4= .2207 ( 55.860 )
| |
| VPRS 5= .2165 ( 55.330 )
| |
| VPRS 6= .3069 ( 65.140 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 145 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.3381 CORRECTED PRESSURE (PSIA) = 73.5533 VAPOR PRESSURE (PSIA) = .2383 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700804.5 l
| |
| | |
| TEMP 1 = 526.7000 ( 67.030 )
| |
| TEMP 2 = 526.6600 ( 66.990 )
| |
| TEMP 3 = 526.5600 ( 66.890 )
| |
| TEMP 4 = 527.8300 ( 68.160 )
| |
| TEMP 5 = 528.1400 ( 68.470 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2400 ( 68.570 )
| |
| TEMP 11 = 528.3400 ( 68.670 )
| |
| : TEMP 12 = 529.3700 ( 69.700 )
| |
| TEMP 13 = 529.5400 ( 69.870 )
| |
| TEMP 14 = 528.7700 ( 69.100 )
| |
| TEMP 15 = 528.0200 ( 68.350 )
| |
| TEMP 16 = 528.1200 ( 68.450 )
| |
| TEMP 17 = 528.1300 ( 68.460 )
| |
| TEMP 18 = 529.3200 ( 69.650 )
| |
| PRES 1= 73.7813 ( 74316.0 )
| |
| PRES 2= 73.7939 ( 72610.0 )
| |
| VPRS 1= .22E3 ( 56.570 )
| |
| VPRS 2= .2252 ( 56.420 )
| |
| VPRS 3= .2287 ( 56.840 )
| |
| l l
| |
| VPRS 4= .2206 ( 55.850 )
| |
| VPRS 5= .2169 ( 55.380 )
| |
| VPRS 6= .3058 ( 65.030 )
| |
| l
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA l TIME = 200 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.3096 CORRECTED PRESSURE (PSIA) = 73.5495 VAPOR PRESSURE (PSIA) = .2731 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700806.5 O
| |
| l u_________
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 215 1109 TEMP 1 = 526.7100 ( 67.040 )
| |
| TEMP 2 = 526.6700 ( 67.000 )
| |
| TEMP 3 = 526.5600 ( 66.890 )
| |
| TEMP 4 = 527.8500 ( 68.180 )
| |
| TEMP 5 = 528.1400 ( 68.470 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 ) l TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2500 ( 68.580 )
| |
| TEMP 11 = 528.3500 ( 68.680 )
| |
| TEMP 12 = 529.3000 ( 69.630 )
| |
| TEMP 13 = 529.4700 ( 69.800 )
| |
| TEMP 14 = 528.6900 ( 69.020 )
| |
| TEMP 15 = 528.0300 ( 68.360 )
| |
| TEMP 16 = 528.1200 ( 68.450 )
| |
| TEMP 17 = 528.1200 ( 68.450 )
| |
| TEMP 18 = 529.2600 ( 69.590 )
| |
| PRES 1= 73.7783 ( 74313.0 )
| |
| P7ES 2= 73.7919 ( 72608.0 )
| |
| # ) VPRS 1= .2263 ( 56.550 )
| |
| VPRS 2= .2256 ( 56.460 )
| |
| VPRS 3= .2297 ( 56.960 ) ,
| |
| VPRS 4= .2216 ( 55.970 )
| |
| VPRS 5= .2196 ( 55.720 ) !
| |
| VPRS 6= .3049 ( 64.950 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 215 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.2874 CORRECTED PRESSURE (PSIA) = 73.5463 VAPOR PRESSURE (PSIA) = .2388 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700805.3
| |
| )
| |
| | |
| 1
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 230 1109 i
| |
| TEMP 1 = 526.7300 ( 67.060 )
| |
| TEMP 2 = 526.6700 ( 67.000 )
| |
| TEMP 3 = 526.5800 ( 66.910 )
| |
| L TEMP 4 = 527.8500 ( 68.180 )
| |
| TEMP 5 = 528.1400' ( 68.470 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| , TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2500 ( 68.580 )
| |
| TEMP 11 = 528.3500 ( 68.680 )
| |
| TEMP 12 = 529.2400 ( 69.570 )
| |
| TEMP 13 = 529.4100 ( 69.740 )
| |
| TEMP 14 = 528.6400 ( 68.970 )
| |
| TEMP 15 = 528.0300 ( 68.360 )
| |
| TEMP 16 = 528.1100 ( 68.440 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 529.1800 ( 69.510 )
| |
| PRES 1= 73.7763 ( 74311.0 )
| |
| PRES 2= 73.7878 ( 72604.0 )
| |
| VPRS 1= .2267 ( 56.600 )
| |
| VPRS 2= .2268 ( 56.610 )
| |
| VPRS 3= .2297 ( 56.970 )
| |
| VPRS 4= .2213 ( 55.940 )
| |
| VPRS 5= .2175 ( 55.460 )
| |
| VPRS 6= .3043 ( 64.890 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 230 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.2669 CORRECTED PRESSURE (PSIA) = 73.5435 VAPOR PRESSURE (PSIA) = .2385 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700806.1 h
| |
| l
| |
| ___ _ _-___________ ___ _ _ L
| |
| | |
| l t '
| |
| | |
| ==SUMMARY==
| |
| 'OF MEASURED DATA AT 245 1109 TEMP 1 = 526.7400 ( 67.070 )
| |
| TEMP 2 = 526.6800 ( 67.010 )-
| |
| TEMP 3 = 526.5800 ( 66.910 )
| |
| TEMP 4 = 527.8500 ( 68.180 )
| |
| TEMP 5'= 528.1500 ( 68.480 )
| |
| TEMP 6 = 527.9000 ( 68.230 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1500 ( 68.480 )
| |
| TEMP 9.= 528.1200 ( 68.450 )
| |
| ' TEMP-10 = 528.2500 ( 68.580 )
| |
| TEMP-11 =.528.3500 ( 68.680 )
| |
| TEMP 12 = 529.1700 (' 69.500 )
| |
| TEMP 13 = 529.3300 ( 69.660 )
| |
| TEMP 14 = 528.6000 ( 68.930 )
| |
| TEMP 15 =-528.0200 ( 68.350 )
| |
| TEMP 16 = 528.1100 ( 68.440 )
| |
| TEMP 17 = 528.1300 ( 68.460 )
| |
| TEMP 18 = 529.1100 ( 69.440 )
| |
| PRES 1= 73.7723 ( 74307.0 )
| |
| PRES 2.= 73.7848 ( 72601.0 )
| |
| () VPRS VPRS 1=
| |
| 2=
| |
| .2266
| |
| .2277
| |
| (
| |
| (
| |
| 56.590 )
| |
| 56.720 )
| |
| VPRS' 3= .2304 ( 57.050 )
| |
| VPRS 4= .2207 ( 55.860 )
| |
| VPRS. 5= .2186 ( 55.600 )
| |
| VPRS 6= .3048 ( 64.940 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA-TIME = 245 DATE = 110f TEMPERATURE (DEGREES R., = 528.2454 CORRECTED PRESSURE (PSIA) = 73.5396 VAPOR PRESSURE (PSIA) = .2390 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700797.0 O
| |
| i
| |
| - - . _ . _ . - _ _ _ - _ _ - - _ . - - _ _ _ _ . . _ - - _ _ _ _ _ _ _ J
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 300 1109 TEMP 1 = 526.7400 ( 67.070 )
| |
| TEMP 2 = 526.7000 ( 67.030 ) ,
| |
| TEMP 3 = 526.6000 ( 66.930 )
| |
| TEMP 4 = 527.8600 ( 68.190 )
| |
| TEMP 5 = 528.1600 ( 68.490 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2500 ( 68.580 )
| |
| TEMP 11 = 528.3500 ( 68.680 )
| |
| TEMP 12 = 529.1200 ( 69.450 )
| |
| TEMP 13 = 529.2800 ( 69.610 )
| |
| TEMP 14 = 528.5400 ( 68.870 )
| |
| TEMP 15 = 528.0100 ( 68.340 )
| |
| TEMP 16 = 528.1000 ( 68.430 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 529.0500 ( 69.380 )
| |
| PRES 1= 73.7703 ( 74305.0 )
| |
| PRES 2= 73.7817 ( 72598.0 )
| |
| VPRS 1= .2272 ( 56.660 )
| |
| VPRS 2= .2265 ( 56.580 )
| |
| VPRS 3= .2308 ( 57.100 )
| |
| VPRS 4= .2224 ( 56.070 )
| |
| VPRS 5= .2186 ( 55.590 )
| |
| VPRS 6= .3017 ( 64.650 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 300 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.2267 CORRECTED PRESSURE (PSIA) = 73.5374 VAPOR PRESSURE (PSIA) = .2387 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700800.8 i
| |
| I
| |
| | |
| (~h
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 315 1109 Q
| |
| TEMP 1 = 526.7700 ( 67.100 )
| |
| TEMP 2 = 526.7000 ( 67.030 )
| |
| TEMP 3 = 526.6000 ( 66.930 )
| |
| TEMP 4 = 527.8600 ( 68.190 )
| |
| TEMP 5 = 528.1600 ( 68.490 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 ) -
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2600 ( 68.590 )
| |
| TEMP 11 = 528.3600 ( 68.690 )
| |
| TEMP 12 = 529.0600 ( 69.390 )
| |
| TEMP 13 = 529.2200 ( 69.550 )
| |
| TEMP 14 = 528.5000 ( 68.830 )
| |
| TEMP 15 = 528.0100 ( 68.340 )
| |
| TEMP 16 = 528.0900 ( 68.420 )
| |
| TEMP 17 = 528.1200 ( 68.450 )
| |
| TEMP 18 = 528.9800 ( 69.310 )
| |
| PRES 1= 73.7674 ( 74302.0 )
| |
| PRES 2= 73.7787 ( 72595.0 )
| |
| I VPRS 1= .2274 ( 56.680 )
| |
| VPRS 2= .2270 ( 56.640 ) i 57.190 )
| |
| VPRS 3= .2316 (
| |
| VPRS 4= .2222 ( 56.050 )
| |
| VPRS 5= .2200 ( 55.770 )
| |
| VPRS 6= .3021 ( 64.680 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 315 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.2088 CORRECTED PRESSURE (PSIA) = 73.5338 VAPOR PRESSURE (PSIA) = .2392 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700791.0 0
| |
| \ - _ _ - _ _ - - _ _ -
| |
| | |
| I i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 330 1109 TEMP 1 = 526.7800 ( 67.110 )
| |
| TEMP 2 = 526.7100 ( 67.040 )
| |
| TEMP 3 = 526.6200 ( 66.950 )
| |
| TEMP 4 = 527.8500 ( 68.180 )
| |
| TEMP 5 = 528.1500 ( 68.480 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1900 ( 68.520 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2600 ( 68.590 )
| |
| TEMP 11 = 528.3600 ( 68.690 )
| |
| TEMP 12 = 529.0000 ( 69.330 )
| |
| TEMP 13 = 529.1500 ( 69.480 )
| |
| TEMP 14 = 528.4600 ( 68.790 )
| |
| TEMP 15 = 528.0000 ( 68.330 )
| |
| TEMP 16 = 528.0900 ( 68.420 )
| |
| TEMP 17 = 528.1200 ( 68.450 )
| |
| TEMP 18 = 528.9300 ( 69.260 )
| |
| PRES 1= 73.7644 ( 74299.0 )
| |
| PRES 2= 73.7766 ( 72593.0 )
| |
| VPRS 1= .2278 ( 56.740 )
| |
| VPRS 2= .2283 ( 56.800 )
| |
| VPRS 3= .2320 ( 57.240 )
| |
| VPRS 4= .2227 ( 56.110 )
| |
| VPRS 5= .2189 ( 55.630 )
| |
| VPRS 6= .3005 ( 64.530 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 330 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.1916 CORRECTED PRESSURE (PSIA) = 73.5314 VAPOR PRESSURE (PSIA) = .2391 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700790.3 h
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 345 1109 TEMP 1 = 526.7800 ( 67.110 )
| |
| TEMP l2 = 526.7100 (. 67.040 )
| |
| TEMP 3 = 526.6400 ( 66.970 )
| |
| TEMP 4 = 527.8600 ( 68.190 ).
| |
| TEMP 5 = 528.1600 ( 68.490 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1900 ( 68.520 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2600 ( 68.590 )
| |
| TEMP 11 = 528.3700 ( 68.700 )
| |
| TEMP 12 = 528.9500 ( 69.280 )
| |
| TEMP 13 = 529.0800 ( 69.410 )
| |
| TEMP 14 = 528.4100 ( 68.740 )
| |
| TEMP 15.= 528.0000 ( 68.330 )
| |
| TEMP 16 = 528.0800 ( 68.410 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 528.8700 ( 69.200 )
| |
| PRES 1= 73.7614 ( 74296.0 )
| |
| PRES -2 = '73.7746 ( 72591.0 )
| |
| O VPRS VPRS VPRS 1=
| |
| 2=
| |
| 3=
| |
| .2283
| |
| .2286
| |
| .2318
| |
| (
| |
| (
| |
| (
| |
| 56.800 )
| |
| 56.830 )
| |
| 57.220 )
| |
| VPRS 4= .2241 ( 56.280 )
| |
| VPRS 5= .2201 ( 55.780 )
| |
| VPRS 6= .2996 ( 64.450 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 345 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.1725 CORRECTED PRESSURE (PSIA) = 73.5285 VAPOR PRESSURE (PSIA) = .2395 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700788.2 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 400 1109 TEMP 1 = 526.7900 ( 67.120 )
| |
| TEMP 2 = 526.7200 ( 67.050 )
| |
| TEMP 3 = 526.6500 ( 66.980 )
| |
| TEMP 4 = 527.8700 ( 68.200 )
| |
| TEMP 5 = 528.1500 ( 68.480 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1900 ( 68.520 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3700 ( 68.700 )
| |
| TEMP 12 = 528.8900 ( 69.220 )
| |
| TEMP 13 = 529.0400 ( 69.370 )
| |
| TEMP 14 = 528.3800 ( 68.710 )
| |
| TEMP 15 = 528.0000 ( 68.330 )
| |
| TEMP 16 = 528.0700 ( 68.400 )
| |
| TEMP 17 = 528.1200 ( 68.450 )
| |
| TEMP 18 = 528.8000 ( 69.130 )
| |
| PRES 1= 73.7594 ( 74294.0 )
| |
| PRES 2= 73.7716 ( 72588.0 )
| |
| VPRS 1= .2279 ( 56.750 )
| |
| VPRS 2= .2281 ( 56.770 )
| |
| VPRS 3= .2330 ( 57.360 )
| |
| VPRS 4= .2247 ( 56.360 )
| |
| VPRS 5= .2193 ( 55.680 )
| |
| VPRS 6= .2992 ( 64.410 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 400 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.1573 CORRECTED PRESSURE (PSIA) = 73.5260 VAPOR PRESSURE (PSIA) = .2395 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700784.6 O
| |
| | |
| ;.- (
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 415 1109 TEMP 1 = 526.8000 ( 67.130 )
| |
| *EMP 2 = 526,7300 ( 67.060 )
| |
| TEMP 3 = 526.6600 ( 66.990 )
| |
| TEMP 4 = 527.8700 ( 68.200 )
| |
| TEMP 5 = 528.1600 ( 68.490 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| -TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2700 ( 68.600 )
| |
| TEMP 11 = 528.3600 ( 68.690-)
| |
| TEMP 12 = 528.8500 ( 69.180 )
| |
| TEMP 13 = 528.9900 ( 69.320 )
| |
| TEMP 14 = 528.3500 ( 68.680 )
| |
| TEMP 15 = 528.0000 ( 68.330 )
| |
| TEMP 16 = 528.0700 ( 68.400 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 528,7600 ( 69.090 )
| |
| PRES 1= 73.7565 ( 74291.0 )
| |
| PRES 2= 73.7685 ( 72585.0 )
| |
| () VPRS VPRS 1=
| |
| 2=
| |
| .2285
| |
| .2291
| |
| (
| |
| (
| |
| 56.820 )
| |
| 56.890 )
| |
| VPRS 3= .2341 ( 57.490 )
| |
| VPRS 4= .2251 ( 56.410 )
| |
| VPRS 5= .2201 ( 55.790 )
| |
| VPRS 6= .2989 ( 64.380 )
| |
| I
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA l
| |
| TIME = 415 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.1423 CORRECTED PRESSURE (PSIA) = 73.5224 VAPOR PRESSURE (PSIA) = .2401 VOLUME ( CTJ . FT . ) = 1865000.0 AIR MASS (LBM) = 700769.9 O
| |
| | |
| i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 430 1109 TEMP 1 = 526.8100 ( 67.140 ) l TEMP 2 = 526.7400 ( 67.070 )
| |
| TEMP 3 = 526.6500 ( 66.980 )
| |
| TEMP 4 = 527.8700 ( 68.200 )
| |
| TEMP 5 = 528.1500 ( 68.480 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2700 ( 68.600 )
| |
| TEMP 11 = 528.3700 ( 68.700 )
| |
| TEMP 12 = 528.8000 ( 69.130 )
| |
| TEMP 13 = 528.9300 ( 69.260 )
| |
| TEMP 14 = 528.2800 ( 68.610 )
| |
| TEMP 15 = 528.0100 ( 68.340 )
| |
| TEMP 16 = 528.0600 ( 68.390 )
| |
| TEMP 17 = 528.1200 ( 68.450 )
| |
| TEMP 18 = 528.7000 ( 69.030 )
| |
| PRES 1= 73.7545 ( 74289.0 )
| |
| PRES 2= 73.7665 ( 72583.0 )
| |
| VPRS 1= .2297 ( 56.970 )
| |
| VPRS 2= .2280 ( 56.760 )
| |
| VPRS 3= .2345 ( 57.540 )
| |
| VPRS 4= .2243 ( 56.310 )
| |
| VPRS 5= .2187 ( 55.610 )
| |
| VPRS 6= .2969 ( 64.190 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 430 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.1229 CORRECTED PRESSURE (PSIA) = 73.5211 VAPOR PRESSURE (PSIA) = .2394 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700783.4 O
| |
| | |
| L ,
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 445 1109 l TEMP 1 = F26.8200 ( 67.150 )
| |
| TEMP 2e 526.7500 ( 67.080 )
| |
| TEMP 3 = 526.6700 ( 67.000 )'
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5 = 528.1600 ( 68.490 ) '
| |
| TEMP- 6 = 527.9400 ( 68.270-)
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 528.7500 ( 69.080 )
| |
| TEMP 13 = 528.8900 '( 69.220 )
| |
| TEMP 14 = 528.2400 ( 68.570 )
| |
| TEMP.15 = 527.9900 ( 68.320 )
| |
| TEMP 16 = 528.0600 ( 68.390.}
| |
| TEMP 17 = 528.1100. ( 683440 )
| |
| TEMP 18 = 528.6500 ( 68.980 )
| |
| PRES 1= 73.7515 ( 74286.0 )
| |
| PRES 2= 73.7635, ( 72580.0 )
| |
| b O
| |
| VPRS VPRS 1=
| |
| 2=
| |
| .2291
| |
| .2297-(
| |
| (
| |
| 56.890 )
| |
| 56.960 )
| |
| VPRS 3= .2347 ( 57.560 )
| |
| VPRS 4= .2247 ( 56.360 )
| |
| VPRS 5= .2193 ( 55.680 )
| |
| VPRS 6= .2963 ( 64.130 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 445 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.1088 CORRECTED PRESSURE (PSIA) = 73.5178 VAPOR PRESSURE (PSIA) = .2397 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700770.6 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 500 1109 TEMP 1 = 526.8300 ( 67.160 )
| |
| TEMP 2 = 526.7700 ( 67.100 )
| |
| TEMP 3 = 526.6800 ( 67.010 )
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5 = 528.1900 ( 68.520 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 528.7000 ( 69.030 )
| |
| TEMP 13 = 528.8400 ( 69.170 )
| |
| TEMP 14 = 528.2100 ( 68.540 )
| |
| TEMP 15 = 527.9800 ( 68.310 )
| |
| TEMP 16 = 528.0400 ( 68.370 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 528.6100 ( 68.940 )
| |
| PRES 1= 73.7495 ( 74284.0 )
| |
| PRES 2= 73.7614 ( 72578.0 )
| |
| VPRS 1= .2297 ( 56.970 )
| |
| VPRS 2= .2302 ( 57.020 )
| |
| VPRS 3= .2347 ( 57.560 )
| |
| VPRS 4= .2251 ( 56.400 )
| |
| VPRS 5= .2228 ( 56.120 )
| |
| VPRS 6= .2939 ( 63.900 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 500 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0946 CORRECTED PRESSURE (PSIA) = 73.5154 VAPOR PRESSURE (PSIA) = .2401 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700766.4 i
| |
| \
| |
| l E________________.___________
| |
| | |
| r_--______--______-_. ---
| |
| 1
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 515 1109 TEMP 1 = 526.8300 ( 67.160 ).
| |
| TEMP 2 = 526.7700 ( 67.100 )
| |
| TEMP 3 = 526.7000 ( 67.030 )
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5 = 528.1900 ( 68.520 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1900 ( 68.520 )
| |
| TEMP 9 = 528.1400 ( 68.470 )
| |
| TEMP 10 = 528.2700 ( 68.600 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.6500 ( 68.980 )
| |
| TEMP 13 = 528.7800 ( 69.110 )
| |
| TEMP 34 = 528.2000 ( 68.530 )
| |
| TEMP 15 = 527.9800 ( 68.310 )
| |
| TEMP 16 = 528.0400 ( 68.370 )
| |
| TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 528.5600 ( 68.890 )
| |
| PRES 1= 73.7475 ( 74282.0 )
| |
| PRES 2= 73.7594 ( 72576.0 )
| |
| ) VPRS 1= .2303 ( 57.040 )
| |
| VPRS 2= .2306 ( 57.070 )
| |
| VPRS 3= .2363 ( 57.750 )
| |
| VPRS 4= .2265 ( 56.580 )
| |
| VPRS 5= .2211 ( 55.910 )
| |
| VPRS 6= .2931 ( 63.820 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 515 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0807 CORRECTED PRESSURE (PSIA) = 73.5131 VAPOR PRESSURE (PSIA) = .2403 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700763.4 O
| |
| | |
| a
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 530 1109 Ol TEMP 1 = 526.8400 ( 67.170 ) i TEMP 2 = 526.7800 ( 67.110 )
| |
| TEMP 3 = 526.7000 ( 67.030 )
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5 = 528.1900 ( 68.520 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.6100 ( 68.940 )
| |
| TEMP 13 = 528.7400 ( 69.070 )
| |
| TEMP 14 = 528.1600 ( 68.490 ) "
| |
| TEMP 15 = 527.9900 ( 68.320 )
| |
| TEMP 16 = 528.0300 ( 68.360 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 528.5100 ( 68.840 )
| |
| PRES 1= 73.7445 ( 74279.0 )
| |
| PRES 2= 73.7574 ( 72574.0 )
| |
| VPRS 1= .2303 ( 57.040 ) i VPRS 2= .2319 ( 57.230 )
| |
| VPRS 3= .2366 ( 57.790 )
| |
| VPRS 4 = .2263 ( 56.550 )
| |
| VPRS 5= .2230 ( 56.150 )
| |
| VPRS 6= .2917 ( 63.680 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 530 DATE = 1109 I
| |
| TEMPERATURE (DEGREES R.) = 528.0656 CORRECTED PRESSURE (PSIA) = 73.5103 VAPOR PRESSURE (PSIA) = .2407 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700756.5 O
| |
| | |
| 1 I
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT- 545~1109
| |
| ~
| |
| TEMP 1 = 526.8500 (- 67.180 )
| |
| TEMP - 2 = 526.7900 ( 67.120 )
| |
| TEMP ~3'= 526.7000 ( 67.030 )
| |
| TEMP 4 = 527.8800' ( 68.210 )
| |
| TEMP '5 = 528.1600- ( 68.490 )
| |
| L TEMP 6 = 527.9400 :( 68.270 )
| |
| TEMP 7 = 536.4400 .( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.5800 ( 68.910 J' TEMP 13 = 528.6900 ( 69.020 )
| |
| TEMP 14 = 528.1600 ( 68.490 )
| |
| 68.320-)
| |
| -TEMP 15 = 527.9900 (
| |
| TEMP 16 = 528.0200 ( 68.350 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 528.4700 ( 68.800 )
| |
| PRES 1= 73.7426 ( 74277.0 )
| |
| PRES. 2= 73.7543- ( 72571;0 )
| |
| -() VPRS VPRS 1=
| |
| 2=
| |
| .2314
| |
| .2315
| |
| .(
| |
| (-
| |
| 57.170 )
| |
| 57.180 )
| |
| VPRS 3= .2369 (' 57.820 )
| |
| VPRS 4= .2274 ( 56.690 )
| |
| VPRS 5= .2244 ( 56.320 )
| |
| VPRS 6= .2887 ( 63.390 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA-TIME = 545 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0551 CORRECTED PRESSURE'(PSIA) = 73.5077 VAPOR PRESSURE (PSIA) = .2407 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700746.1 O
| |
| | |
| l 1
| |
| 1
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 600 1109 l
| |
| l TEMP 1 = 526.8600 ( 67.190 )
| |
| TEMP 2 = 526.8000 ( 67.130 )
| |
| TEMP 3 = 526.7100 ( 67.040 )
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5' 528.1700 ( 68.500 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )~
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.5300 ( 68.860 )
| |
| TEMP 13 = 528.6400 ( 68.970 )
| |
| TEMP 14 = 528.1400 ( 68.470 )
| |
| TEMP 15 = 527.9800 ( 68.310 )
| |
| TEMP 16 = 528.0200 ( 68.350 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 528.4200 ( 68.750 )
| |
| PRES 1= 73.7406 ( 74275.0 ) >
| |
| PRES 2= 73.7523 ( 72569.0 ) ,
| |
| VPRS 1= .2322 ( 57.270 )
| |
| VPRS 2= .2327 ( 57.320 )
| |
| VPRS 3= .2397 ( 58.150 ) i VPRS 4= .2283 ( 56.790 ) I VPRS 5= .2269 ( 56.630 )
| |
| VPRS 6= .2881 ( 63.330 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 600 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0409 CORRECTED PRESSURE (PSIA) = 73.5044 VAPOR PRESSURE (PSIA) = .2420 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700733.6 1
| |
| 0
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 615 1109 TEMP 1 = 526.8700 ( 67.200 )
| |
| TEMP 2 = 526.8000 .(. 67.130 )
| |
| TEMP '3 = 526.7200 ( 67.050 )
| |
| TEMP 4 = 527.8900 ( 68.220 )
| |
| TEMP 5 = 528.1900 ( 68.520 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 (. 68.490 )
| |
| TEMP 9 = 528.1200_ ( 68.450 )
| |
| TEMP 10 = 528.'2800 ( 68.610')
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.4800 ( 68.810 )
| |
| TEMP 13 = 538.6000 ( 68.930-)
| |
| TEMP 14 = 528.1200 ( 68.450 )
| |
| TEMP 15 = 527.9900 ( 68.320 )
| |
| TEMP 16 = 528.0300 ( 68.360 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 528.3800 ( 68.710 )
| |
| PRES 1= 73.7386 ( 74273.0 )
| |
| PRES 2= 73.7503 ( 72567.0 )
| |
| I VPRS 1 =~ .2328 ( 57.330 )
| |
| VPRS 2= .2349 ( .57.590 )
| |
| VPRS 3= .2414 ( 58.350 )
| |
| VPRS_ 4= .2293 ( 56.920 )
| |
| .VPRS 5= .2232 ( 56.170 )
| |
| VPRS 6= .2849 ( 63.010 )
| |
| l-
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA l TIME = 615 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0323 CORRECTED PRESSURE (PSIA) = 73.5027 VAPOR PRESSURE (PSIA) = .2417 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700728.6
| |
| '( )
| |
| | |
| i f
| |
| l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 630 1109 TEMP 1 = 526.8900 ( 67.220 )
| |
| TEMP 2 = 526.8100 ( 67.140 )
| |
| TEMP 3 = 526.7300 ( 67.060 )
| |
| TEMP 4 = 527.8900 ( 68.220 )
| |
| TEMP 5 = 528.2000 ( 68.530 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.4500 ( 68.780 )
| |
| TEMP 13 = 528.5600 ( 68.890 )
| |
| TEMP 14 = 528.1200 ( 68.450 )
| |
| TEMP 15 = 527.9800 ( 68.310 )
| |
| TEMP 16 = 528.0200 ( 68.350 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 528.3400 ( 68.670 )
| |
| PRES 1= 73.7366 ( 74271.0 )
| |
| PRES 2= 73.7482 ( 72565.0 )
| |
| VPRS 1= .2333 ( 57.400 )
| |
| VPRS 2= .2346 ( 57.550 )
| |
| VPRS 3= .2412 ( 58.320 )
| |
| VPRS 4= .2294 ( 56.930 )
| |
| VPRS 5= .2268 ( 56.610 )
| |
| VPRS 6= .2828 ( 62.800 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 630 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0224 CORRECTED PRESSURE (PSIA) = 73.5005 VAPOR PRESSURE (PSIA) = .2419 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700720.4 0
| |
| | |
| i I
| |
| ;(3 Q
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 645 1109 TEMP 1 = 526.8900 ( 67.220 )
| |
| TEMP 2 = 526.8200 ( 67.150 )
| |
| TEMP -3 = 526.7400 ( 67.070 )
| |
| TEMP 4 = 527.9100 ( 68.240 ) ;
| |
| TEMP 5 = 528.1900 ( 68.520 ) l TEMP 6 = 527.9500 ( 68.280 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1500 ( 68.480 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.4100 ( 68.740 )
| |
| TEMP 13 = 528.5200 ( 68.850 )
| |
| TEMP 14 = 528.1000 ( 68.430 )
| |
| TEMP 15 = 527.9800 ( 68.310 )
| |
| TEMP 16 = 528.0100 ( 68.340 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 528.3000 ( 68.630 )
| |
| PRES 1= 73.7336 ( 74268.0 )
| |
| PRES 2= 73.7462 ( 72563.0 )
| |
| VPRS 1= .2335 ( 57.420 )
| |
| VPRS 2= .2355 ( 57.660 )
| |
| VPRS 3= .2417 ( 58.380 )
| |
| VPRS 4= .2304 ( 57.050 )
| |
| VPRS 5= .2265 ( 56.580 )
| |
| VPRS 6= .2816 ( 62.680 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 645 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0109 CORRECTED PRESSURE (PSIA) = 73.4978 VAPOR PRESSURE (PSIA) = .2421 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700709.9
| |
| (
| |
| L - - - - - - - - - - - - - -- - - - - _ - - - - - - - -
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 700 1109 TEMP 1 = 526.8900 ( 67.220 )
| |
| TEMP 2 = 526.8300 ( 67.160 )
| |
| TEMP 3 = 526.7500 ( 67.080 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP 5 = 528.2000 ( 58.530 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.3900 ( 68.720 )
| |
| TEMP 13 = 528.4800 ( 68.810 )
| |
| TEMP 14 = 528.0900 ( 68.420 )
| |
| TEMP 15 = 527.9900 ( 68.320 )
| |
| TEMP 16 = 528.0100 ( 68.340 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 528.2700 ( 68.600 )
| |
| PRES 1= 73.7316 ( 74266.0 )
| |
| PRES 2= 73.7442 ( 52561.0 )
| |
| VPRS 1= .2349 ( 57.580 )
| |
| VPRS 2= .2363 ( 57.750 )
| |
| VPRS 3= .2447 ( 58.720 )
| |
| VPRS 4= .2326 ( 57.310 )
| |
| VPRS 5= .2223 ( 56.060 )
| |
| VPRS 6= .2785 ( 62.370 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 700 DATE = 1109 TEMPERATURE (DEGREES R.) = 528.0028 CORRECTED PRESSURE (PSIA) = 73.4959 VAPOR PRESSURE (PSIA) = .2420 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700702.5 i
| |
| i I
| |
| 1 l
| |
| l
| |
| | |
| -l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 715 1109 TEMP 1 = 526.8900 ( '67.220 )
| |
| TEMP 2 = 526.8300 ( 67.160 )
| |
| TEMP 3 = 526.7500 ( 67.080 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP 5 = 528.2000 ( 68.530 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1500 ( 68.480 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.4100 ( 68.740 )
| |
| TEMP 12 = 528.3300 ( 68.660 )
| |
| TEMP 13 = 528.4600 ( 68.790 )
| |
| TEMP 14 = 528.0700 ( 68.400 )
| |
| TEMP 15 = 527.9900 ( 68.320 )
| |
| TEMP 16 = 528.0100 ( 68.340 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 528.2300 ( 68.560 )
| |
| PRES 1= 73.7297 ( 74264.0 )
| |
| PRES 2.= 73.7421 ( 72559.0 )
| |
| ( VPRS 1= .2353 ( 57.630 )
| |
| VPRS 2= .2375 ( 57.890 )
| |
| VPRS 3= .2452 ( 58.780 )
| |
| VPRS 4= .2317 ( 57.200 )
| |
| VPRS 5= .2270 ( 56.640 )
| |
| VPRS 6= .2738 ( 61.880 )
| |
| i
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA l TIME = 715 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.9907 CORRECTED PRESSURE (PSIA) = 73.4937 VAPOR PRESSURE (PSIA) = .2422 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700697.8 I
| |
| l l
| |
| O
| |
| | |
| 8 l
| |
| l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 730 1109 TEMP 1 = 526.9100 ( G7.240 )
| |
| TEMP 2 = 526.8500 ( 67.180 )
| |
| TEMP 3 = 526.7800 ( 67.110 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP 5 = 528.2000 ( 68.530 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 53J.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1100 ( 68.440 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.3000 ( 68.630 )
| |
| TEMP 13 = 528.4100 ( 68.740 )
| |
| TEMP 14 = 528.0700 ( 68.400 )
| |
| TEMP 15 = 527.9800 ( 68.310 )
| |
| TEMP 16 = 528.0000 ( 68.330 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 528.1700 ( 68.500 )
| |
| PRES 1= 73.7277 ( 74262.0 )
| |
| PRES 2= 73.7401 ( 72557.0 )
| |
| VPRS 1= .2365 ( 57.770 ) h VPRS 2= .2372 ( 57.860 )
| |
| VPRS 3= .2461 ( 58.880 )
| |
| VPRS 4= .2328 ( 57.340 )
| |
| VPRS 5= .2272 ( 56.660 )
| |
| VPRS 6= .2720 ( 61.700 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 730 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.9807 CORRECTED PRESSURE (PSIA) = 73.4915 VAPOR PRESSURE (PSIA) = .2424 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700690.3 h
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT. 745 1109 TEMP 1 = 526.9200 ( 67.250 )
| |
| TEMP 2 = 526.8500 ( 67.180L)
| |
| TEMP 3 = 526.7800 ( 67.110 )
| |
| TEMP 4 = 527.9000 .( 68.230:)
| |
| TEMP- 5 = 528.;2"JO ( 68.540 )
| |
| TEMP 6 = 527.9500 ( 68.280 )
| |
| TEMP- 7 = 536.4400- ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 (. 68.610 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.2600 ( 68.590 )
| |
| TEMP 13 = 528.3700 ( 68.700 )'
| |
| TEMP 14-= 528.0600 ( 68.390 ).
| |
| TEMP 15 = 527.9700 ( 68.300 )
| |
| TEMP 16 = 528.0000 ( 68.330 )
| |
| TEMP 17 = 528.0900 (. 68.420 )
| |
| TEMP 18 = 528.1400 ( 68.470 )
| |
| PRES 1= 73.7257 ( 74260.0 )
| |
| PRES 2= 73.7381 ( 72555.0 )
| |
| i VPRS 1= .2368 ( 57.81G )
| |
| VPRS 2= .2383' ( .57.980 )
| |
| VPRS 3= .2480 .( 59.100 )
| |
| VPRS 4= .2341 ( 57.490 )
| |
| VPRS 5= .2278 ( 56.740 )
| |
| VPRS 6= .2665 ( 61.120 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 745 DATE = 1109 TEMPERATURE (CEGREES R.) = 527.9705 CORRECTED PRESSURE (PSIA) = 73.4896 VAPOR PRESSURE (PSIA) = .2423 L VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700685.3 l
| |
| l h
| |
| | |
| l l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 800 1109 TEMP 1 = 526.9300 ( 67.260 )
| |
| TEMP 2 = 526.8500 ( 67.180 )
| |
| TEMP 3 = 526.7900 ( 67.120 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| l TEMP 5 = 528.2000 ( 68.530 )
| |
| TEMP 6 = 527.9500 ( 68.280 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1300 ( 68.460 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528 1900 ( 68.720 )
| |
| TEMP 12 = 528.2400 ( 68.570 )
| |
| TEMP 13 = 528.3400 ( 68.670 )
| |
| TEMP 14 = 528.0600 ( 68.390 )
| |
| TEMP 15 = 527.9600 ( 68.290 :
| |
| TEMP 16 = 528.0000 ( 68.330 )
| |
| TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 528.1100 ( 68.440 )
| |
| PRES 1= 73.7237 ( 74258.0 )
| |
| PRES 2= 73.7360 ( 72553.0 )
| |
| VPRS 1= .2380 ( 57.950 )
| |
| VPRS 2= .2400 ( 58.180 )
| |
| VPRS 3= .2478 ( 59.080 )
| |
| VPRS 4= .2351 ( 57.610 )
| |
| VPRS 5= .2292 ( 56.900 )
| |
| VPRS 6= .2656 ( 61.020 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 800 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.9636 CORRECTED PRESSURE (PSIA) = 73.4869 VAPOR PRESSURE (PSIA) = .2429 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700669.4 O
| |
| | |
| i i
| |
| l l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 815 1109 TEMP 1 = 526.9300 ( 67.260 )
| |
| TEMP 2 = 526.8600 ( 67.190 )
| |
| TEMP 3 = S26.8000 ( 67.130 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.2000 ( 68.530 )
| |
| TEMP. 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.2100 ( 68.540 )
| |
| TEMP 13 = 528.3000 ( 68.630 )
| |
| TEMP 14 = 528.0600 ( 68.390 ) l TEMP 15 = 527.9500 ( 68.280 ) ,
| |
| TEMP 16 = 527.9900 ( 68.320 ) i TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 528.0900 ( 68.420 )
| |
| PRES 1= 73.7217 ( 74256.0 )
| |
| PRES 2= 73.7340 ( 72551.0 )
| |
| VPRS 1= .2383 ( 57.980 )
| |
| []
| |
| \ VPRS 2= .2395 ( 58.120 )
| |
| VPRS 3= .2491 ( 59.220 )
| |
| VPRS 4= .2369 ( 57.820 )
| |
| VPRS 5= .2294 ( 56.930 )
| |
| VPRS 6= .2590 ( 60.310 )
| |
| | |
| ==SUMMARY==
| |
| OF CORREOTED DATA TIME = 815 DATE = 1109 l TEMPERATURE (DEGREES R.) = 527.9541 CORRECTED PRESSURE (PSIA) = 73.4856 VAPOR PRESSURE (PSIA) = .2423 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700668.9 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 830 1109 I TEMP 1 = 526.9500 ( 67.280 ) ,
| |
| TEMP 2 = 526.8700 ( 67.200 ) ;
| |
| TEMP 3 = 526.8200 ( 67.150 ) !
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.2100 ( 68.540 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1200 ( 68.450 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.1700 ( 68.500 )
| |
| TEMP 13 = 528.2700 ( 68.600 )
| |
| TEMP 14 = 528.0400 ( 68.370 )
| |
| TEMP 15 = 527.9500 ( 68.280 )
| |
| TEMF 16 = 527.9700 ( 68.300 )
| |
| TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 528.0400 ( 68.370 )
| |
| PRES 1= 73.7197 ( 74254.0 )
| |
| PRES 2= 73.7330 ( 72550.0 )
| |
| VPRS 1= .2395 ( 58.120 )
| |
| VPRS 2= .2397 ( 58.150 )
| |
| VPRS 3= .2495 ( 59.270 )
| |
| VPRS 4= .2388 ( 58.040 )
| |
| VPRS 5= .2288 ( 56.860 )
| |
| VPRS 6= .2547 ( 59.840 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 830 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.9431 CORRECTED PRESSURE (PSIA) = 73.4844 VAPOR PRESSURE (PSIA) = .2420 )
| |
| VOLUME (CU.FT.) = 1865000.0 i AIR MASS (LBM) = 700671.9 l
| |
| l O
| |
| 1
| |
| )
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 845 1109 TEMP .1 = 526.9400 ( 67.270 )
| |
| TEMP 2 = 526.8900 ( 67.220 )
| |
| TEMP 3 = 526.8200 ( 67.150~)'
| |
| TEMP 4 = 527.9200: ( 68.250-)
| |
| TEMP 5 = 528.2100 ( 68.540 )
| |
| TEMP. 6 = 527.9500 (_ 68.280.)
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 ) -
| |
| TEMP 9 = 528.1200 ( 68.450')
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3900 -( 68.720 )
| |
| TEMP 12 = 528.1600 ( 68.490 )
| |
| TEMP 13 = 528.2300 ( 68.560 )
| |
| TEMP 14 = 528.0200 ( 68.350 )
| |
| TEMP 15 = 527.9500 ( 68.280 )
| |
| TEMP 16 = 527.9600 ( 68.250 )
| |
| TEMP.17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 528.0200 ( 68.350 )
| |
| PRES 1= 73.7177 ( 74252.0 )
| |
| PRES 2= 73.7310 ( 72548.0 )
| |
| 1 VPRS 1= .2399 ( 58.170-)
| |
| VPRS 2= .2409 ( 58.290 )
| |
| VPRS 3= .2504 ( 59.370 )
| |
| VPRS 4= .2410 ( 58.300 )
| |
| VPRS 5= .2271 ( 56.650 )
| |
| VPRS 6= .2535 ( 59.710 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 845 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.9373 CORRECTED PRESSURE (PSIA) = 73.4821 VAPOR PRESSURE (PSIA) = .2423
| |
| , VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700657.7 w
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 900 1109 TEMP 1 = 526.9600 ( 67.290 )
| |
| TEMP 2 = 526.8900 ( 67.220 )
| |
| TEMP 3 = 526.8200 ( 67.150 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.1900 ( 68.520 )
| |
| TEMP 6 = 527.9500 ( 68.280 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1100 ( 68.440 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.1300 ( 68.460 )
| |
| TEMP 13 = 528.2100 ( 68.540 )
| |
| TEMP 14 = 527.9900 ( 68.320 )
| |
| TEMP 15 = 527.9600 ( 68.290 )
| |
| TEMP 16 = 527.9400 ( 68.270 )
| |
| TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 527.9900 ( 68.320 )
| |
| PRES 1= 73.7158 ( 74250.0 )
| |
| PRES 2= 73.7299 ( 72547.0 )
| |
| VFRS 1= .2408 ( 58.270 )
| |
| VPRS 2= .2433 ( 58.560 )
| |
| VPRS 3= .2502 ( 59.350 )
| |
| VPRS 4= .2389 ( 58.050 )
| |
| VPRS 5= .2318 ( 57.220 )
| |
| VPRS 6= .2510 ( 59.440 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 900 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.9241 CORRECTED PRESSURE (PSIA) = 73.4801 VAPOR PRESSURE (PSIA) = .2428 VOLUME (CU.FT.) = 1865000.0 AIR MASS (L5M) = 700656.3 l
| |
| O
| |
| | |
| l s j
| |
| h.
| |
| -(m-
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 915 1109 l
| |
| TEMP 1 = $26.9600 ( 67.290 ) i TEMP 2 = 526.8900 ( 67.220 )
| |
| TEMP 3 = 526.8200 ( 67.150 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.1700 (. 68.500 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 528.1100 ( 68.440 )
| |
| TEMP 10 =.528.2900 ( 68.620 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.1100 ( 68.440 )
| |
| TEMP 13 = 528.1700 ( 68.500 )
| |
| TEMP 14 = 527.9800 ( 68.310 )
| |
| TEMP 15 = 527.9400 ( 68.270 )
| |
| TEMP 16 = 527.9100' ( 68.240 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 527.9700 ( 68.300 )
| |
| PRES 1= 73.7138 ( 74248.0 )
| |
| PRES 2= 73.7279 ( 72545.0 )
| |
| (- VPRS 1= .2408 ( 58.280 ) j VPRS 2= .2431 ( 58.540 )
| |
| VPRS 3= .2501 ( 59.330 )
| |
| VPRS 4= .2383 ( 57.990 )
| |
| VPRS 5= .2328 ( 57.340 )
| |
| VPRS 6= .2477 ( 59.060 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 915 DATE = 1109
| |
| = 527.9119 TEMPERATURE (DEGREES R.)
| |
| CORRECTED PRESSURE (PSIA) = 73.4786
| |
| = .2422 VAPOR PRESSURE (PSIA)
| |
| VOLUME (CU.FT.) = 1865000.0
| |
| = 700658.7 AIR MASS (LBM)
| |
| O 4
| |
| _ _ _ _ _ _ _ _ i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 930 1109 TEMP 1 = 526.9700 ( 67.300 )
| |
| TEMP 2 = 526.8900 ( 67.220 )
| |
| TEMP 3 = 526.8500 ( 67.180 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.2000 ( 68.530 )
| |
| TEMP 6 = 527.9500 ( 68.280 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1400 ( 68.470 )
| |
| TEMP 9 = 528.1100 ( 68.440 )
| |
| TEMP 10 = 528.2800 ( 68.610 )
| |
| TEMP 11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 528.0900 ( 68.420 )
| |
| TEMP 13 = 528.1500 ( 68.480 )
| |
| TEMP 14 = 527.9600 ( 68.290 )
| |
| TEMP 15 = 527.9400 ( 68.270 )
| |
| TEMP 16 = 527.9200 ( 68.250 )
| |
| TEMP 17 = 528.1000 ( 68.430 )
| |
| TEMP 18 = 527.9400 ( 68.270 )
| |
| PRES 1= 73.7128 ( 74247.0 )
| |
| PRES 2= 73.7269 ( 72544.0 )
| |
| VPRS 1= .2417 ( 58.380 )
| |
| VPRS 2= .2441 ( 58.650 )
| |
| VPRS 3= .2502 ( 59.340 )
| |
| VPRS 4= .2392 ( 58.090 )
| |
| VPRS 5= .2322 ( 57.260 )
| |
| VPRS 6= .2476 ( 59.050 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 930 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.9075 CORRECTED PRESSURE (PSIA) = 73.4773 VAPOR PRESSURE (PSIA) = .2425 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700652.2 1
| |
| i l
| |
| \ __ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
| |
| | |
| r 'I t
| |
| r
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 945 1109 TEMP 1 = 526.9800 ( 67.310 )
| |
| TEMP 2 = 526.9200 ( 67.250,)
| |
| TEMP 3 = 526.8500 ( 67.180 )
| |
| TEMP 4 = 527.9200 ( 68.250 )
| |
| TEMP 5 = 528.1900 ( '.68.520 )
| |
| TEMP 6.= 527.9400 ( 68.270 )-
| |
| 1 TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1400 (- 68.470 )
| |
| TEMP 9 = 528.1000 ( 68.430 )
| |
| TEMP 10_= 528.2700 ( 68.600 )
| |
| TEMP'11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 528.0800 ( 68.410 )
| |
| TEMP 13 = 528.1200 ( 68.450 )
| |
| TEMP 14 = 527.9400 ( 68.270 )
| |
| TEMP 15 =:527.9400 ( 68.270 )
| |
| TEMP 16 = 527.9100 ( 68.240 )
| |
| TEMP 17 = 528.1100 ( 68.440 )
| |
| TEMP 18 = 527.9000 ( 68.230 )
| |
| PRES 1= 73.7108 ( 74245.0 )
| |
| PRES 2= 73.7239 ( 72541.0 )
| |
| VPRS 1= .2429 ( 58.520 )
| |
| VPRS 2= .2435 ( 58.590 )
| |
| VPRS 3= .2499 ( 59.310-)
| |
| VPRS 4= .2414 ( 58.340 )
| |
| VPRS 5= .2332 ( 57.380 )
| |
| VPRS 6= .2465 ( 58.930 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 94S"
| |
| 'DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8989 CORRECTED PRESSURE (PSIA) = 73.4744
| |
| =
| |
| VAPOR PRESSURE (PSIA) .2429 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700635.9 O
| |
| | |
| l ll l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1000 1109 l TEMP 1 = 526.9900 ( 67.320 )
| |
| TEMP 2 = 526.9200 ( 67.250 )
| |
| TEMP 3 = 526.8500 ( 67.180 )
| |
| TEMP 4 = 527.9200 ( 68.250 )
| |
| TEMP 5 = 528.2000 ( 68.530 )
| |
| TEMP 6 = 527.9500 ( 68.280 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 - 528.1500 ( 68.480 )
| |
| TEMP 9 = 528.0900 ( 68.420 )
| |
| TEMP 10 = 528.2700 ( 68.600 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.0700 ( 68.400 )
| |
| TEMP 13 = 528.1100 ( 68.440 )
| |
| TEMP 14 = 527.0100 ( 68.240 )
| |
| TEMP 15 = 527.9100 ( 68.240 )
| |
| TEMP 16 = 527.8900 ( 68.220 )
| |
| TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 527.8800 ( 68.210 )
| |
| PRES 1= 73.7088 ( 74243.0 )
| |
| PRES 2= 73.7228 ( 72540.0 )
| |
| VPRS 1= .2434 ( 58.570 )
| |
| VPRS 2= .2442 ( 58.670 )
| |
| VPRS 3= .2495 ( 59.270 )
| |
| VPRS 4= .2389 ( 58.060 )
| |
| VPRS 5= .2340 ( 57.480 )
| |
| VPRS 6= .2448 ( 58.730 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1000 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8887 CORRECTED PRESSURE (PSIA) = 73.4734 VAPOR PRESSURE (PSIA) = .2424 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700639.9 O
| |
| | |
| I l
| |
| | |
| ==SUMMARY==
| |
| dF MEASURED DATA AT 1015 1109 TEMP 1 = 527.0000 ( 67.330 )
| |
| TEMP 2 = 526.9300 ( 67.260 )-
| |
| TEMP 3 = 526.8600 ( 67.190 )
| |
| TEMP 4 = 527.9200 ( 68.250 )
| |
| TEMP 5 = 528.1900 ( 68.520 )
| |
| TEMP 6.= 527.9200 (- 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1400 ( 68.470 )
| |
| TEMP 9 = 528.0800 ( 68.410 )
| |
| TEMP 10 = 528.2700 ( 68.600 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.0400 ( 68.370 )
| |
| TEMP 13.= 528.0900 ( 68.420 )
| |
| TEMP 14 = 527.9000 ( 68.230 )
| |
| TEMP 15 = 527.9000 ( 68.230 )
| |
| TEMP 16 = 527.8800 ( 68.210 )
| |
| TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 527.8600 ( 68.190 )
| |
| PRES 1= 73.7068 ( 74241.0 )
| |
| PRES 2= 73.7208 ( 72538.0 )
| |
| VPRS 1= .2433 ( 58.560 )
| |
| O. VPRS 2= .2454 ( 58.800 )
| |
| VPRS 3= .2487 ( 59.180 )
| |
| VPRS 4= .2395 ( 58.120 )
| |
| VPRS 5= .2299 ( 56.990 )
| |
| VPRS 6= .2448 ( 58.730 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1015 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8783 CORRECTED PRESSURE (PSIA) = 73.4720 VAPOR PRESSURE (PSIA) = .2418 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700640.4 O
| |
| | |
| _ _ _ _ _ _ = _ _ _ _ _ _ _ _ _ _ _ _ _
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1030 1109 TEMP 1 = 527.0000 ( 67.330 )
| |
| TEMP 2 = 526.9300 ( 67.260 )
| |
| TEMP 3 = 526.8900 ( 67.220 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.1900 ( 68.520 ) ,
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1300 ( 68.460 )
| |
| TEMP 9 = 528.0800 ( 68.410 )
| |
| TEMP 10 = 528.2600 ( 68.590 )
| |
| TEMP 11 = 528.4000 ( 68.730 )
| |
| TEMP 12 = 528.0200 ( 68.350 )
| |
| TEMP 13 = 528.0700 ( 68.400 )
| |
| TEMP 14 = 527.8800 ( 68.210 )
| |
| TEMP 15 = 527.9100 ( 68.240 )
| |
| TEMP 16 = 527.8700 ( 60.200 )
| |
| TEMP 17 = 528.0800 ( 68.410 )
| |
| TEMP 18 = 527.8500 ( 68.180 )
| |
| PRES 1= 73.7058 ( 74240.0 )
| |
| PRES 2= 73.7188 ( 72536.0 )
| |
| VPRS 1= .2441 ( 58.660 ) '
| |
| VPRS 2= .2437 ( 58.610 )
| |
| VPRS 3= .2478 ( 59.070 )
| |
| VPRS- 4= .2396 ( 58.140 )
| |
| VPRS 5= .2329 ( 57.350 )
| |
| VPRS 6= .2447 ( 58.720 ) .
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1030 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8734 CORRECTED PRESSURE (PSIA) = 73.4703 VAPOR PRESSURE (PSIA) = .2420 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700630.5 O
| |
| I
| |
| | |
| l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1045 1109 TEMP 1 = 527.0100 ( 67.340 )
| |
| TEMP '2 = 526.9300 ( 67.260 )
| |
| TZMP 3 = 526.8900 ( 67.220 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.1900 ( 68.520 )
| |
| TEMP 6 = 527.9400 ( 68.270 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1300 ( 68.460 )
| |
| TEMP 9 = 528.0800 ( 68.410 )
| |
| TEMP 10 = 528.2500 ( 68.580 )
| |
| TEMP 11 = 528.3900 ( 68.720 )
| |
| TEMP 12 = 528.0100 ( 68.340 )
| |
| TEMP 13 = 526.0600 ( 68.390 )
| |
| TEMP 14 = 527.8700 ( 68.200 )
| |
| TEMP 15 = 527.9000 ( 68.230 )
| |
| TEMP 16 = 527.8700 ( 68.200 )
| |
| TEMP 17 = 528.0900 ( 68.420 )
| |
| TEMP 18 = 527.8300 ( 68.160 )
| |
| PRES 1= 73.7029 ( 74237.0 )
| |
| PRES 2= 73.7168 ( 72534.0 )
| |
| /~ VPRS 1= .2443 ( 58.680 )
| |
| k- VPRS 2= .2446 ( 58.710 ) ;
| |
| VPRS 3= .2479 ( 59.090 )
| |
| VPRS 4= .2395 ( 58.130 ) i VPRS 5= .2347 ( 57.560 )
| |
| VPRS 6= .2447 ( 58.720 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1045 DATE = 1109 ,
| |
| TEMPERATURE (DEGREES R.) = 527.8688 CORRECTED PRESSURE (PSIA) = 73.4673 VAPOR PRESSURE (PSIA) = .2425 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700608.0 l
| |
| O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1100 1109 TEMP 1 = 527.0100 ( 67.340 )
| |
| TEMP 2 = 526.9400 ( 67.270 )
| |
| TEMP 3 = 526.8900 ( 67.220 )
| |
| TEMP 4 = 527.9100 ( 68.240 )
| |
| TEMP 5 = 528.1700 ( 68.500 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1400 ( 68.470 )
| |
| TEMP 9 = 528.0700 ( 68.400 )
| |
| TEMP 10 = 528.2400 ( 68.570 )
| |
| TEMP 11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 528.0000 ( 68.330 )
| |
| TEMP 13 = 528.0300 ( 68.360 )
| |
| TEMP 14 = 527.8500 ( 68.180 )
| |
| TEMP 15 = 527.9000 ( 68.230 )
| |
| TEMP 16 = 527.8500 ( 68.180 )
| |
| TEMP 17 = 528.0400 ( 68.370 )
| |
| TEMP 18 = 527.8200 ( 68.150 )
| |
| PRES 1= 73.7009 ( 74235.0 )
| |
| PRES 2= 73.7157 ( 72533.0 )
| |
| VPRS 1= .2441 ( 58.660 )
| |
| VPRS 2= .2441 ( 58.660 )
| |
| VPRS 3= .2475 ( 59.040 )
| |
| VPRS 4= .2392 ( 58.090 )
| |
| VPRS 5= .2349 ( 57.580 )
| |
| VPRS 6= .2434 ( 58.580 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1100 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8546 CORRECTED PRESSURE (PSIA) = 73.4662 VAPOR PRESSURE (PSIA) = .2421 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700616.5 O
| |
| | |
| s 3
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1115 1109 i
| |
| TEMP 1 = 527.0100 ( 67.340 )
| |
| ~
| |
| TEMP 2 = 526.9400 ( 6. 270 )
| |
| TEMP 3 = 526.8900 ( 67.220 )
| |
| TEMP 4 = 527.8900 ( 68.220 )
| |
| TEMP 5 = 528.1600 ( 68.490 ) 1 TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1100 ( 68.440 )
| |
| TEMP 9 = 528.0600 ( 68.390 )
| |
| TEMP 10 = 528.2400 ( 68.570 )
| |
| TEMP 11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 527.9800 ( 68.310 )
| |
| TEMP 13 = 528.0000 ( 68.330 ) .
| |
| TEMP 14 = 527.8300 ( 68.160 ) l TEMP 15 = 527.8800 ( 68.210 )
| |
| TEMP 16 = 527.8400 ( 68.170 )
| |
| TEMP 17 = 528.0600 ( 68.390 )
| |
| TEMP 18 = 527.7800 ( 68.110 )
| |
| PRES 1= 73.6999 ( 74234.0 )
| |
| PRES 2= 73.7137 ( 72531.0 )
| |
| VPRS 1= .2444 58.690 )
| |
| O' VPRS 2= .2446
| |
| (
| |
| ( 58.710 )
| |
| VPRS 3= .2470 ( 58.990 )
| |
| VPRS 4= .2395 ( 58.120 )
| |
| VPRS 5= .2323 ( 57.280 )
| |
| VPRS 6= .2431 ( 58.540 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA l TIME = 1115 DATE = 1109 !
| |
| 1 TEMPERATURE (DEGREES R.) = 527.8113 CORRECTED PRESSURE (PSIA) = 73.4652 VAPOR PRESSURE (PSIA) = .2416 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700624.1 O
| |
| | |
| I
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1130 1109 TEMP 1 = 527.0300 ( 67.360 )
| |
| TEMP 2 = 526.9500 ( 67.280 )
| |
| TEMP 3 = 526.8900 ( 67.220 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP 5 = 528.1400 ( 68.470 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = ~
| |
| 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0800 ( 68.410 )
| |
| TEMP 9 = 528.0400 ( 68.370 )
| |
| TEMP 10 = 528.2300 ( 68.560 )
| |
| TEMP 11 = 528.3700 ( 68.700 )
| |
| TEMP 12 = 527.9700 ( 68.300 )
| |
| TEMP 13 = 527.9800 ( 68.310 )
| |
| TEMP 14 = 527.8200 ( 68.150 )
| |
| TEMP 15 = 527.8700 ( 68.200 )
| |
| TEMP 16 = 527.8300 ( 68.160 )
| |
| TEMP 17 = 528.0600 ( 68.390 )
| |
| TEMP 18 = 527.7700 ( 68.100 )
| |
| PRES 1= 73.6979 ( 74232.0 )
| |
| PRES 2= 73.7127 ( 72530.0 )
| |
| VPRS 1= .2445 ( 58.700 )
| |
| VPRS 2= .2441 ( 58.650 )
| |
| VPRS 3= .2471 ( 59.000 )
| |
| VPRS 4= .2387 ( 58.030 )
| |
| VPRS 5= .2353 ( 57.630 )
| |
| VPRS 6= .2431 ( 58.540 )
| |
| i
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1130 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8328 CORRECTED PRESSURE (PSIA) = 73.4633 VAPOR PRESSURE (PSIA) = .2420 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700617.8 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1145 1109 TEMP -1 = 527.0300 ( 67.360 )
| |
| TEMP 2-= 526.9500 ( 67.280 )
| |
| TEMP 3 = 526.9100 ( 67.240 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP .5 = 528.1400 ( 68.470 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1000 ( 68.430-)
| |
| TEMP 9 = 528.0300 ( 68.360 )
| |
| TEMP 10 = 528.2200 ( 68.550 )
| |
| TEMP 11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 527.9400 (' 68.270 )
| |
| TEMP 13 = 527.9700 ( 68.300 )
| |
| TEMP 14 = 527.8200 ( 68.150 )
| |
| TEMP 15'= 527.8500 ( 68.180 )
| |
| TEMP 16 = 527.8200 ( 68.150 )
| |
| TEMP 17 = 528.0600' ( 68.390 )
| |
| TEMP 18 = 527.7600 ( 68.090 )
| |
| PRES 1= 73.6959 ( 74230.0 )
| |
| PRES 2= 73.7117 ( 72529.0 )
| |
| [ )
| |
| \/
| |
| VPRS 1= .2441 ( 58.650 )
| |
| VPRS 2= .2434 ( 58.570 )
| |
| VPRS 3= .2468 ( 58.960 )
| |
| VPRS 4.= .2383 ( 57.990 )
| |
| VPRS 5= .2357 ( 57.680 )
| |
| VPRS 6= .2426 ( 58.480 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA l TIME = 1145 l- DATE = 1109
| |
| , TEMPERATURE (DEGREES R.) = 527.8276 CORRECTED PRESSURE (PSIA) = 73.4622 VAPOR PRESSURE (PSIA) = .2416 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700613.4 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1200 1109 TEMP 1 = 527.0400 ( 67.370 )
| |
| TEMP 2 = 526.9600 ( 67.290 )
| |
| TEMP 3 = 526.9300 ( 67.260 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP 5 = 528.1400 ( 68.470 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0800 ( 68.410 )
| |
| TEMP 9 = 528.0300 ( 68.360 )
| |
| TEMP 10 = 528.2200 ( 68.550 )
| |
| TEMP 11 = 528.3600 ( 68.690 )
| |
| TEMP 12 = 527.9200 ( 68.250 )
| |
| TEM? 13 = 527.9600 ( 68.290 )
| |
| TEMP 14 = 527.8000 ( 68.130 )
| |
| TEMP 15 = 527.8500 ( 68.180 )
| |
| TEMP 16 = 527.8100 ( 68.140 )
| |
| TEMP 17 = 528.0400 ( 68.370 )
| |
| TEMP 18 = 527.7500 ( 68.080 )
| |
| PRES 1= 73.6949 ( 74229.0 )
| |
| PRES 2= 73.7096 ( 72527.0 )
| |
| VPRS 1= .2441 ( 58.660 )
| |
| VPRS 2= .2444 ( 58.690 )
| |
| VPRS 3= .2467 ( 58.950 )
| |
| VPRS 4= .2395 ( 58.120 )
| |
| VPRS 5= .2341 ( 57.490 )
| |
| VPRS 6= .2434 ( 58.580 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1200 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8203 CORRECTED PRESSURE (PSIA) = 73.4604 VAPOR PRESSURE (PSIA) = .2419 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700606.4 9
| |
| | |
| i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1215 1109 TEMP 1 = 527.0500 ( 67.380 )
| |
| TEMP 2 = 526.9600 ( 67.290 )
| |
| TEMP 3 = 526.9300 ( 67.260 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP 5'= 528.1300 ( 68.460 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1000 ( 68.430 )
| |
| TEMP 9 = 528.0200 ( 68.350 )
| |
| TEMP 10 = 528.2100 ( 68.540 )
| |
| TEMP 11 = 528.3600 ( 68.690 )
| |
| TEMP 12 = 527.9100 ( 68.240 )
| |
| TEMP 13 = 527.9400 ( 68.270 )
| |
| TEMP 14 = 527.7800 ( 68.110 )
| |
| TEMP 15 = 527.8400 ( 68.170 )
| |
| TEMP 16 = 527.8000 ( 68.130 )
| |
| TEMP 17 = 528.0300 ( 68.360 )
| |
| TEMP 18 = 527.7300 ( 68.060 )
| |
| PRES 1= 73.6929 ( 74227.0 )
| |
| PRES 2= 73.7086 ( 72526.0 )
| |
| ) VPRS VPRS 1=
| |
| 2=
| |
| .2441
| |
| .2440
| |
| (
| |
| (
| |
| 58.660 )
| |
| 58.640 )
| |
| VPRS 3= .2464 ( 58.920 )
| |
| VPRS 4m .2389 ( 58.050 )
| |
| VPRS 5= .2308 ( 57.100 )
| |
| VPRS 6= .2426 ( 58.480 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1215 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8117 CORRECTED PRESSURE (PSIA) = 73.4599 VAPOR PRESSURE (PSIA) = .2409 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700612.7 O
| |
| | |
| l l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1230 1109 l
| |
| l TEMP 1 = 527.0600 ( 67.390 )
| |
| TEMP 2 = 526.9700 ( 67.300 )
| |
| TEMP 3 = 526.9500 ( 67.280 )
| |
| TEMP 4 = 527.9000 ( 68.230 )
| |
| TEMP 5 = 528.1200 ( 68.450 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0700 ( 68.400 )
| |
| TEMP 9 = 528.0100 ( 68.340 )
| |
| TEMP 10 = 528.2103 ( 68.540 )
| |
| TEMP 11 = 528.3800 ( 68.710 )
| |
| TEMP 12 = 527.9000 ( 68.230 )
| |
| TEMP 13 = 527.9200 ( 68.250 )
| |
| TEMP 14 = 527.7800 ( 68.110 )
| |
| TEMP 15 = 527.8400 ( 68.170 )
| |
| TEMP 16 = 527.7800 ( 68.110 )
| |
| TEMP 17 = 528.0600 ( 68.390 )
| |
| TEMP 18 = 527.7200 ( 68.050 )
| |
| PRES 1= 73.6900 ( 74224.0 )
| |
| PRES 2= 73.7046 ( 72522.0 )
| |
| VPRS 1= .2436 ( 58.600 )
| |
| VPRS 2= .2437 ( 58.610 )
| |
| VPRS 3= .2468 ( 58.960 )
| |
| VPRS 4= .2382 ( 57.970 )
| |
| VPRS 5= .2349 ( 57.590 )
| |
| VPRS 6= .2421 ( 58.420 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA ,
| |
| TIME = 1230 j DATE = 1109 TEMPERATURE (DEGREES R.) = 527.8102 CORRECTED PRESSURE (PSIA) = 73.4559 {
| |
| VAPOR PRESSURE (PSIA) = .2414 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700576.8 l
| |
| 1 4
| |
| l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1245.1109.
| |
| TEMP 1 = 527.0600 ( 67.390 )
| |
| TEMP 2 = 526.9700 ( 67.300 )
| |
| TEMP 3 = 526.9400 ( 67.270 )
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5 = 528.1200 ( 68.450 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| ' TEMP .7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0800.'( 68.410 )
| |
| TEMP 9 = 528.0100 (. 68.340 )
| |
| TEMP 10 = 528.2100' ( 68.540 )
| |
| TEMP 11 = 528.3500 -(- 68.680 )
| |
| TEMP 22 = 527.8900- ( 68.220 )
| |
| TEMP 13 = 527.9100 ( 68.240 )
| |
| TEMP 14 = 527.7600 ( 68.090 )
| |
| TEMP 15 = 527.8300 ( 68.160 )
| |
| TEMP 16 = 527.7700 ( 68.100 )
| |
| TEMP 17 = 528.0200. ( 68.350 )
| |
| TEMP.18 = 527.7000 ( 68.030 )
| |
| PRES 1= 73.6860 ( 74220.0 )
| |
| PRES 2= 73.7005 ( 72518.0 )
| |
| VPRS 1= .2438 ( 58.620 )
| |
| O-- VPRS 2= .2431 ( 58.540 )
| |
| VPRS' 3_ = .2468 ( 58.960 )
| |
| 'VPRS 4= .2377 ( 57.910 )
| |
| VPRS 5= .2354 ( 57.650 )
| |
| VPRS 6= .2421 ( 58.420 )
| |
| 1
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1245 DATE = 1109 TEMPERATURE-(DEGREES R.) = 527.7961 CORRECTED PRESSURE (PSIA) = 73.4519 VAPOR PRESSURE (PSIA) = .2413 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) w 700557.9 h
| |
| | |
| [ T j l
| |
| I j
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1300 1109 4 TEMP 1 = 527.0600 ( 67.390 )
| |
| TEMP 2 = 526.9800 ( 67.310 )
| |
| TEMP 3 = 526.9500 ( 67.280 )
| |
| TEMP 4 = 527.8900 ( 68.220 )
| |
| l TEMP 5 = 528.1300 ( 68.460 )
| |
| l TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0900 ( 68.420 )
| |
| TEMP 9 = 527.9900 ( 68.320 )
| |
| TEMP 10 = 528.2000 ( 68.530 )
| |
| TEMP 11 = 528.3700 ( 68.700 )
| |
| TEMP 12 = 527.8700 ( 68.200 )
| |
| TEMP 13 = 527.8900 ( 68.220 )
| |
| TEMP 14 = 527.7400 ( 68.070 )
| |
| TEMP 15 = 527.8100 ( 68.140 )
| |
| TEMP 16 = 527.7700 ( 68.100 )
| |
| TEMP 17 = 528.0400 ( 68.370 )
| |
| TEMP 18 = 527.7000 ( 68.030 )
| |
| PRES 1= 73.6820 ( 74216.0 )
| |
| PRES 2= 73.6985 ( '/2516.0 )
| |
| VPRS 1= .2437 ( 58.610 ) h VPRS 2= .2434 ( 58.580 )
| |
| VPRS 3= .2464 ( 58.920 )
| |
| VPRS 4= .2383 ( 57.990 )
| |
| VPRS 5= .2349 ( 57.580 )
| |
| VPRS 6= .2426 ( 58.480 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1300 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7926 CORRECTED PRESSURE (PSIA) = 73.4488 VAPOR PRESSURE (PSIA) = .2414 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700532.9 9
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1315 1109 TEMP 1 = 527.0800 ( 67.410 )
| |
| TEMP 2 = 526.9800 ( 67.310 )
| |
| TEMP 3 = 526.9500 ( 67.280 )
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5 = 528.1100 ( 68.440 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0400 ( 68.370 )
| |
| TEMP 9 = 527.9900 ( 68.320 ) ,
| |
| TEMP 10 = 528.1700 ( 68.500 ) '"
| |
| TEMP 11 = 528.3600 ( 68.690 )
| |
| TEMP 12 = 527.8500 ( 68.180 )
| |
| TEMP 13 = 527.8900 ( 68.220 )
| |
| TEMP 14 = 527.7300 ( 68.060 )
| |
| TEMP 15 = 527.8100 ( 68.140 )
| |
| TEMP 16 = 527.7600 ( 68.090 )
| |
| TEMP 17 = 528.0400 ( 68.370 )
| |
| TEMP 18 = 527.6900 ( 68.020 )
| |
| PRES 1= 73.6790 ( 74213.0 )
| |
| PRES 2= 73.6944 ( 72512.0 )
| |
| VPRS 1= .2445 ( 58.700 )
| |
| O. VPRS 2= .2428 ( 58.510 )
| |
| VPRS 3= .2463 ( 58.910 )
| |
| VPRS 4= .2381 ( 57.960 )
| |
| VPRS 5= .2328 ( 57.340 )
| |
| VPRS 6= .2427 ( 58.490 )
| |
| | |
| ==SUMMARY==
| |
| OF COBRECTED DATA TIME = 1315 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7844 CORRECTED PRESSURE (PSIA) = 73.4457 VAPOR PRESSURE (PSIA) = .2410 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700514.3 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1330 1109 TEMP 1 = 527.0800 ( 67.410 )
| |
| TEMP 2 = 526.9900 ( 67.320 )
| |
| TEMP 3 = 526.9600 ( 67.290 )
| |
| TEMP 4 = 527.8800 ( 68.210 )
| |
| TEMP 5 = 528.1000 ( 68.430 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1300 ( 68.460 )
| |
| TEMP 9 = 527.9800 ( 68.310 )
| |
| TEMP 10 = 528.1700 ( 68.500 )
| |
| TEMP 11 = 528.3600 ( 68.690 )
| |
| TEMP 12 = 527.8500 ( 68.180 )
| |
| TEMP 13 = 527.8800 ( 68.210 )
| |
| TEMP 14 = 527.7200 ( 68.050 )
| |
| TEMP 15 = 527.8000 ( 68.130 )
| |
| TEMP 16 = 527.7400 ( 68.070 )
| |
| TEMP 17 = 528.0400 ( 68.370 )
| |
| TEMP 18 = 527.6700 ( 68.000 )
| |
| PRES 1= 73.6761 ( 74210.0 )
| |
| PRES 2= 73.6924 ( 72510.0 )
| |
| VPRS 1= .2434 ( 58.580 )
| |
| VPRS 2= .2434 ( 58.580 )
| |
| VPRS 3= .2460 ( 58.870 )
| |
| VPRS 4= .2377 ( 57.910 )
| |
| VPRS 5= .2318 ( 57.220 )
| |
| VPRS 6= .2422 ( 58.440 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1330 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7820 CORRECTED PRESSURE (PSIA) = 73.4436 VAPOR PRESSURE (PSIA) = .2406 '
| |
| VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700497.4
| |
| __ - a
| |
| | |
| ,/m b)
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1345 1109 TEMP 1 = 527.0900 ( 67.420 )
| |
| TEMP 2 = 527.0000 ( 67.330 )
| |
| TEMP 3 = 526.9600 ( 67.290 )
| |
| TEMP 4 = 527.8700 ( 68.200 )
| |
| TEMP 5 = 528.1100 ( 68.440 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.0700 ( 68.400 )
| |
| TEMP 9 = 527.9700 ( 68.300 )
| |
| TEMP 10 = 528.1500 ( 68.480 )
| |
| TEMP 11 = 528.3400 ( 68.670 )
| |
| TEMP 12 = 527.8500 ( 68.180 )
| |
| TEMP 13 = 527.8700 ( 68.200 )
| |
| TEMP 14 = 527.7100 ( 68.040 )
| |
| TEMP 15 = 527.8100 ( 68.140 )
| |
| TEMP 16 = 527.7300 ( 68.060 )
| |
| TEMP 17 = 528.0100 ( 68.340 )
| |
| TEMP 18 = 527.6700 ( 68.000 )
| |
| PRES 1= 73.6731 ( 74207.0 )
| |
| PRES 2= 73.6883 ( 72506.0 )
| |
| [\~'} VPRS VPRS 1=
| |
| 2=
| |
| .2439
| |
| .2428
| |
| (
| |
| (
| |
| 58.630 )
| |
| 58.510 )
| |
| VPRS 3= .2462 ( 58.890 )
| |
| VPRS 4= .2383 ( 57.990 )
| |
| VPRS 5= .2326 ( 57.310 )
| |
| VPRS 6= .2421 ( 58.430 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1345 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7753 CORRECTED PRESSURE (PSIA) = 73.4399 VAPOR PRESSURE (PSIA) = .2408 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700470.8
| |
| ('h v
| |
| i l
| |
| 1 - - - - -
| |
| | |
| d
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1400 1109 TEMP 1 = 527.1000 ( 67.430 )
| |
| TEMP 2 = 527.0000 ( 67.330 )
| |
| TEMP 3 = 526.9700 ( 67.300 )
| |
| TEMP 4 = 527.8600 ( 68.190 )
| |
| TEMP 5 = 528.0900 ( 68.420 )
| |
| TEMP 6 = 527.9000 ( 68.230 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1200 ( 68.450 )
| |
| TEMP 9 = 527.9700 ( 68.300 )
| |
| TEMP 10 = 528,1400 ( 68.470 ) ,
| |
| TEMP 11 = 528.3400 ( 68.670 ) j 68.160 )
| |
| TEMP 12 = 527.8300 (
| |
| TEMP 13 = 527.8700 ( 68.200 )
| |
| TEMP 14 = 527.7100 ( 68.040 )
| |
| TEMP 15 = 527.7800 ( 68.110 )
| |
| TEMP 16 = 527.7300 ( 68.060 )
| |
| TEMP 17 = 528.0100 ( 68.340 )
| |
| TEMP 18 = 527.6500 ( 67.980 )
| |
| PRES 1= 73.6701 ( 74204.0 )
| |
| PRES 2= 73.6843 ( 72502.0 )
| |
| VPRS 1= .2441 ( 58.660 )
| |
| VPRS 2= .2436 ( 58.600 )
| |
| VPRS 3= .2459 ( 58.860 )
| |
| VPRS 4= .2371 ( 57.850 )
| |
| VPRS 5= .2323 ( 57.280 )
| |
| VPRS 6= .2421 ( 58.420 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1400 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7700 CORRECTED PRESSURE (PSIA) = 73.4366 VAPOR PRESSURE (PSIA) = .2406 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700445.8 i
| |
| i e
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1415 1109 TEMP 1 = 527.1000 ( 67.430 )
| |
| TEMP 2 = 527.0100 ( 67.340 )
| |
| TEMP 3 = 526.9800 ( 67.310 )
| |
| TEMP 4 = 527.8500 ( 68.180 )
| |
| TEMP 5 = 528.0900 ( 68.420 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 527.9600 ( 68.290 )
| |
| TEMP 10 = 528.1600 ( 68.490')
| |
| TEMP 11 = 528.3400 ( 68.670 )
| |
| TEMP 12 = 527.8200 ( 68.150 ) j TEMP 13 = 527.8500 ( 68.180 ) l TEMP 14 = 527.7000 ( 68.030 )
| |
| TEMP 15 = 527.8100 ( 68.140 )
| |
| TEMP 16 = 527.7200 ( 68.050 )
| |
| TEMP 17 = 528.0100 ( 68.340 )
| |
| TEMP 18 = 527.6400 ( 67.970 )
| |
| PRES 1= 73.6671 ( 74201.0 )
| |
| PRES 2= 73.6812 ( 72499.0 )
| |
| VPRS 1= .2436 ( 58.600 )
| |
| VPRS 2= .2436 ( 58.600 )
| |
| VPRS 3= .2455 ( 58.820 )
| |
| VPRS 4= .2377 ( 57.920 )
| |
| VPRS 5= .2313 ( 57.160 )
| |
| VPRS 6= .2424 ( 58.460 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1415 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7705 CORRECTED PRESSURE (PSIA) = 73.4337 VAPOR PRESSURE (PSIA) = .2405 VOLUME (CU.FT.) = 1865000.O AIR MASS (LBM) = 700417.7
| |
| ()
| |
| | |
| l l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1430 1109 TEMP 1 = 527.1000 ( 67.430 )
| |
| TEMP 2 = 527.0300 ( 67.360 ) i TEMP 3 = 526.9700 ( 67.300 )
| |
| TEMP 4 = 527.8500 ( 68.180 )
| |
| TEMP 5 = 528.0900 ( 68.420 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1400 ( 68.470 )
| |
| TEMP 9 = 527.9500 ( 68.280 )
| |
| TEMP 10 = 528.1400 ( 68.470 )
| |
| TEMP 11 = 528.3400 ( 68.670 )
| |
| TEMP 12 = 527.8200 ( 68.150 )
| |
| TEMP 13 = 527.8400 ( 68.170 )
| |
| TEMP 14 = 527.6900 ( 68.020 )
| |
| TEMP 15 = 527.7800 ( 68.110 )
| |
| TEMP 16 = 527.7200 ( 68.050 )
| |
| TEMP 17 = 528.0200 ( 68.350 )
| |
| TEMP 18 = 527.6300 ( 67.960 )
| |
| PRES 1= 73.6642 ( 74198.0 )
| |
| PRES 2= 73.6782 ( 72496.0 )
| |
| VPRS 1= .2436 ( 58.600 )
| |
| VPRS 2= .2429 ( 58.520 )
| |
| VPRS 3= .2462 ( 58.890 )
| |
| VPRS 4 = .2376 ( 57.900 )
| |
| VPRS 5= .2346 ( 57.550 )
| |
| VPRS 6= .2426 ( 58.480 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1430 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7639 CORRECTED PRESSURE (PSIA) = 73.4301 VAPOR PRESSURE (PSIA) = .2411 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700392.2 0
| |
| | |
| - (}
| |
| ( ,/
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1445 1109 TEMP. 1 = 527.1100 ( 67.440 )
| |
| TEMP P = 527.0300 ( 67.360 )
| |
| TEMP 3 = 526.9900 ( 67.320 )
| |
| TEMP 4 = 527.8400 ( 68.170 )
| |
| TEMP 5 = 528.0900 ( 68.420 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1100 ( 68.440 )
| |
| TEMP 9 = 527.9500 ( 68.280 )
| |
| TEMP 10 = 528.1400 ( 63.470 ) l TEMP 11 = 528.3000 ( 68.630 )
| |
| TEMP 12 = 527.8100 ( 68.140 )
| |
| TEMP 13 = 527.8300 ( 68.160 )
| |
| TEMP 14 = 527.6900 ( 68.020 )
| |
| TEMP 15 = 527.8000 ( 68.130 )
| |
| TEMP 16 = 527.7200 ( 68.050 )
| |
| TEMP 17 = 527.9900 ( 68.320 )
| |
| TEMP 18 = 527.6300 ( 67.960 )
| |
| PRES 1= 73.6612 ( 74195.0 )
| |
| PRES 2= 73.6761 ( 72494.0 )
| |
| ) VPRS VPRS 1=
| |
| 2=
| |
| .2435
| |
| .2426
| |
| (
| |
| (
| |
| 58.590 )
| |
| 58.480 )
| |
| VPRS 3= .2459 ( 58.860 )
| |
| VPRS 4= .2376 ( 57.900 )
| |
| VPRS 5= .2333 ( 57.390 )
| |
| VPRS 6= .2413 ( 58.330 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1445 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7599 CORRECTED PRESSURE (PSIA) = 73.4282 VAPOR PRESSURE (PSIA) = .2405 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700379.2 i
| |
| V 1
| |
| l t
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1500 1109 TEMP 1 = 527.1100 ( 67.440 )
| |
| TEMP 2 = 527.0400 ( 67.370 )
| |
| TEMP 3 = 526.9900 ( 67.320 )
| |
| TEMP 4 = 527.8400 ( 68.170 )
| |
| TEMP 5 = 528.0800 ( 68.410 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| ~
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1300 ( 68.460 )
| |
| TEMP 9 = 527.9500 ( 68.280 )
| |
| TEMP 10 = 528.1300 ( 68.460 )
| |
| TEMP 11 = 528.3300 ( 68.660 )
| |
| TEMP 12 = 527.8100 ( 68.140 )
| |
| TEMP 13 = 527.8200 ( 68.150 )
| |
| TEMP 14 = 527.6700 ( 68.000 )
| |
| TEMP 15< 527.7700 ( 68.100 )
| |
| TEMP 16 = 527.7100 ( 68.040 )
| |
| TEMP 17 = 528.0000 ( 68.330 )
| |
| TEMP 18 = 527.6100 ( 67.940 )
| |
| PRES 1= 73.6582 ( 74192.0 )
| |
| PRES 2= 73.6731 ( 72491.0 )
| |
| VPRS 1= .2430 ( 58.530 )
| |
| VPRS 2= .2426 ( 58.480 )
| |
| VPRS 3= .2459 ( 58.860 )
| |
| VPRS 4= .2381 ( 57.960 )
| |
| VPRS 5= .2333 ( 57.400 )
| |
| VPRS 6= .2422 ( 58.440 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1500 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7343 CORRECTED PRESSURE (PSIA) = 73.4249 VAPOR PRESSURE (PSIA) = .2407 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700355.8 9
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1515 1109 TEMP 1 = 527.1200 -( 67.450 )
| |
| TEMP 2 = 527.0500 ( 67.380 )
| |
| TEMP 3 = 527.0000 ( 67.330 )
| |
| TEMP '4 = 527.8500- ( 68.180 )
| |
| TEMP 5 = 528.0800 ( 68.410 )
| |
| TEMP 6 = 527.9200 ( 68.250 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1900 ( 68.520 )
| |
| TEMP 9 =.527.9400 ( 68.270 )
| |
| TEMP 10 = 528.1300 ( 68.460 )
| |
| TEMP 11 = 528.3000 ( 68.630 )
| |
| TEMP 12 = 527.7800 ( 68.110 )
| |
| TEMP 33 ='527.8200 ( 68.150 )
| |
| TEMP 14 = 527.6700 ( 68.000 )
| |
| TEMP 15 = 527.7800 ( 68.110')
| |
| TEMP 16 = 527.7000 ( 68.030 )
| |
| TEMP 17 = 527.9700 ( 68.300 )
| |
| TEMP 18 = 527.6100 ( 67.940 )
| |
| PRES 1= 73.6562 ( 74190.0 )
| |
| PRES 2= 73.6711 ( 72489.0 )
| |
| '() VPRS VPRS 1=
| |
| 2=
| |
| .2433
| |
| .2431
| |
| (
| |
| (
| |
| 58.560 )
| |
| 58.540 )
| |
| VPRS 3= .2459 ( 58.860 )
| |
| VPRS 4= .2375 ( 57.890 )
| |
| VPRS 5= .2329 ( 57.350 )
| |
| VPRS 6= .2419 ( 58.400 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1515 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7524 CORRECTED PRESSURE (PSIA) = 73.4231 VAPOR PRESSURE (PSIA) = .2406 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700340.4 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1530 1109 TEMP 1 = 527.1400 ( 67.470 )
| |
| TEMP 2w 527.0500 ( 67.380 )
| |
| TEMP 3 = 527.0000 ( 67.330 )
| |
| TEMP 4 = 527.8400 ( 68.170 )
| |
| TEMP 5 = 528.0700 ( 68.400 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.2000 ( 68.530 )
| |
| TEMP 9 = 527.9200 ( 68.250 )
| |
| TEMP 10 = 528.1200 ( 68.450 )
| |
| TEMP 11 = 528.3100 ( 68.640 )
| |
| TEMP 12 = 527.7790 ( 68.100 )
| |
| TEMP 13 = 527.8100 ( 68.140 )
| |
| TEMP 14 = 527.6700 ( 68.000 )
| |
| TEMP 15 = 527.7700 ( 68.100 )
| |
| TEMP 16 = 527.7000 ( 68.030 )
| |
| TEMP 17 = 527.9800 ( 68.310 )
| |
| TEMP 18 = 527.6000 ( 67.930 )
| |
| PRES 1= 73.6532 ( 74187.0 )
| |
| PRES 2= 73.6680 ( 72486.0 )
| |
| VPRS 1= .2431 ( 58.540 )
| |
| VPRS 2= .2426 ( 58.480 )
| |
| VPRS 3= .2455 ( 58.810 )
| |
| VPRS 4= .2380 ( 57.950 )
| |
| VPRS 5= .2363 ( 57.750 )
| |
| VPRS 6= .2411 ( 58.310 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1530 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7485 CORRECTED PRESSURE (PSIA) = 73.4197 VAPOR PRESSURE (PSIA) = .2409 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700313.3 O
| |
| | |
| 7 i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1545 3109 TEMP' 1 = 527.1400 '(- 67.470 )
| |
| TEMP 2 = 527.0500 .( 67.380 )
| |
| TEMP 3 rs. 526.9900 ( 67,320 )
| |
| TEMP 4 = 527.8400 ( 68.170 ).
| |
| TEMP 5 = 528.0700 ( 68.400 )
| |
| TEMP 6 = 527.9000 ( 68.230 )
| |
| TEMP 7 = 536.4400 ( 76.770 ) -
| |
| TEMP 8 = 528.1100 ( 68.440-)
| |
| TEMP 9 = 527.9200. ( 68.250-)
| |
| TEMP 10 = 528.1100' ( 68.440 }
| |
| TEMP 11 = 528.2800 ( 68.610 )
| |
| r TEMP 12 =.527.7600 .( 68.090 )
| |
| -TEMP 13 = 527.8100- (' 68.140 )
| |
| TEMP 14 = 527.6700 ( 68.000 )
| |
| TEMP 15 = 527.7700 ( 68.100 )
| |
| TEMP 16 ='527.7000 ( 68.030 )
| |
| TEMP 17 = 527.9800 (' 68.310 )
| |
| TEMP 18 = 527.6000 ( 67.930 )
| |
| PRES 1- 73.6503 ( 74184.0 ).
| |
| PRES 2= 73.6650 ( 72483.0 )
| |
| ( VPRS 1=' .2430 ( 58.530 )
| |
| VPRS 2= .2423 ( 58.450 )
| |
| VPRS 3= .2448 ( 58.730 )
| |
| VPRS 4= .2376 ( 57.900 )
| |
| VPRS 5= .2344 ( 57.530 )
| |
| VPRS ~6 = .2414 ( 58.340 )
| |
| | |
| ==SUMMARY==
| |
| -OF CORRECTED DATA-TIME = 1545 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7418 I
| |
| CORRECTED PRESSURE (PSIA) = 73.4172 VAPOR PRESSURE (PSIA) = .2404 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700298'.8 O
| |
| | |
| I l
| |
| l l
| |
| l
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1600 1109 TEMP 1 = 527.1400 ( 67.470 )
| |
| TEMP 2 = 527.0600 ( 67.390 )
| |
| TEMP 3 = 527.0300 ( 61.360 )
| |
| TEMP 4 = S27.8400 ( GB.170 )
| |
| TEMP 5 = 528.0600 ( 68.390 )
| |
| 68.240 )
| |
| TEMP 6 = 527.9100 (
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1300 ( 68.460 )
| |
| TEMP 9 = 527.9200 ( 68.250 )
| |
| TEMP 10 = 528.1100 ( 68.440 )
| |
| TEMP 11 = 528.2800 ( 68.610 )
| |
| TEMP 12 = 527.7700 ( 68.100 )
| |
| TEMP 13 = 527.7800 ( 68.110 )
| |
| TEMP 14 = 527.6700 ( 68.000 )
| |
| TEMP 15 = 527.7800 ( 68.110 ) l TEMP 16 = 527.6900 ( 68.020 )
| |
| TEMP 17 = 527.9500 ( 68.280 )
| |
| TEMP 18 = 527.6000 ( 67.930 )
| |
| PRES 1= 73.6473 ( 74181.0 )
| |
| PRES 2= 73.6619 / 72480.0 )
| |
| VPRS 1= .2428 ( 58.510 )
| |
| VPRS 2= .2421 ( 58.420 )
| |
| VPRS 3= .2456 ( 58.830 )
| |
| VPRS 4= .2371 ( 57.850 )
| |
| VPRS 5= .2301 ( 57.010 )
| |
| VPRS 6= .2418 ( 58.390 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1600 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7413 CORRECTED PRESSURE (PSIA) = 73.4149 VAPOP PRESSURE (PSIA) = .2397 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700277.1 0
| |
| | |
| r~% .
| |
| )
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1615 1109 TEMP 1 = 527.1400 ( 67.470 )
| |
| TEMP 2 = 527.0600 ( 67.390 )
| |
| TEMP 3 = 527.0000 ( 67.330 )
| |
| TEMP 4 = 527.8300 ( 68.160 )
| |
| TEMP 5 = 528.0400 ( 60.370 )
| |
| TEMP 6 = 527.9000 ( 68.230 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1700 ( 68.500 )
| |
| TEMP 9 = 527.9100 ( 68.240 )
| |
| TEMP 10 = 528.1100 ( 68.440 )
| |
| TEMP 11 = 528.2800 ( 68.610 )
| |
| TEMP 12 = 527.7600 ( 68.090 )
| |
| TEMP 13 = 527.7800 ( 68.110 )
| |
| TEMP 14 = 527.6500 ( 67.980 )
| |
| TEMP 15 = 527.7700 ( 68.100 )
| |
| TEMP 16 = 527.6700 ( 68.000 )
| |
| TEMP 17 = 527.9400 -( 68.270 )
| |
| TEMP 18 = 527.5800 ( 67.910 )
| |
| PRES 1= 73.6443 ( 74178.0 )
| |
| PRES 2= 73.6599 ( 72478.0 )
| |
| VPRS 1= .2432
| |
| (-- VPRS 2= .2411
| |
| (
| |
| (
| |
| 58.550 )
| |
| 58.310 )
| |
| VPRS 3= .2455 ( 58.810 )
| |
| VPRS 4= .2376 ( 57.900 )
| |
| VPRS 5= .2334 ( 57.410 )
| |
| VPRS 6= .2417 ( 58.380 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1615 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7310 CORRECTED PRESSURE (PSIA) = 73.4119 VAPOR PRESSURE (PSIA) = .2402 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700262.1 O
| |
| V
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1630 1109 l
| |
| TEMP 1 = 527.1600 ( 67.490 )
| |
| TEMP 2 = 527.0700 ( 67.400 )
| |
| TEMP 3 = 527.0100 ( 67.340 )
| |
| TEMP 4 = 527.8300 ( 68.160 )
| |
| TEMP 5 = 528.0300 ( 68.360 )
| |
| TEMP 6 = 527.9100 ( 68.240 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.2700 ( 68.600 )
| |
| TEMP 9 = 527.9000 ( 68.230 )
| |
| TEMP 10 = 528.1000 ( 68.430 )
| |
| TEMP 11 = 528.2700 ( 68.600 )
| |
| TEMP 12 = 527.7600 ( 68.090 )
| |
| TEMP 13 = 527.7800 ( 68.110 )
| |
| TEMP 14 = 527.6400 ( 67.970 )
| |
| TEMP 15 = 527.7700 ( 68.100 )
| |
| TEMP 16 = 527.6700 ( 68.000 )
| |
| TEMP 17 = 527.9500 ( 68.280 )
| |
| TEMP 18 = 527.5700 ( 67.900 )
| |
| PRES 1= 73.6413 ( 74175.0 )
| |
| PRES 2= 73.6569 ( 72475.0 )
| |
| VPRS 1= .2434 ( 58.570 )
| |
| VPRS 2= .2416 ( 58.370 )
| |
| VPRS 3= .2447 ( 58.720 )
| |
| VPRS 4= .2389 ( 58.050 )
| |
| VPRS 5= .2315 ( 57.180 )
| |
| VPRS 6= .2414 ( 58.340 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1630 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7345 CORRECTED PRESSURE (PSIA) = 73.4091 VAPOR PRESSURE (PSIA) = .2400 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700230.8 9
| |
| | |
| l f
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1645 1109' l
| |
| TEMP 1 = 527.1700 ( 67.500 )
| |
| TEMP 2 = 527.0700 ( 67.400 )
| |
| TEMP 3 = 527.0100 ( 67.340 )
| |
| TEMP 4 = 527.8300 ( 68.160 )
| |
| TEMP 5 = 528.0400 ( 68.370 )
| |
| TEMP 6 = 527.9000 ( 68.230 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP S = 528.2700 ( 68.600 )
| |
| TEMP 9 = 527.9000 ( 68.230 )
| |
| TEMP 10 = 528.1000 ( 68.430 )
| |
| TEMP 11 = 528.2600 ( 68.590 )
| |
| TEMP 12 = 527.7500 ( 68.080 )
| |
| TEMP 13 = 527.7700 ( 68.100 )
| |
| TEMP 14 = 527.6400 ( 67.970 )
| |
| TEMP 15 = 527.7600 ( 68.090 )
| |
| TEMP 16 = 527.6700 ( 68.000 )
| |
| TEMP ~17 = 527.9500 ( 68.280 )
| |
| TEMP 18 = 527.5600 ( 67.890 )
| |
| PRES 1= 73.6384 ( 74172.0 )
| |
| PRES 2= 73.6538 ( 72472.0 )
| |
| () VPRS VPRS 1=
| |
| 2=
| |
| .2431
| |
| .2424
| |
| (
| |
| (
| |
| 58.540 )
| |
| 58.460 )
| |
| VPRS 3= .2449 ( 58.750 )
| |
| VPRS 4= .2368 ( 57.810 )
| |
| VPRS 5= .2279 ( 56.750 )
| |
| VPRS 6= .2413 ( 58.330 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1645 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7308 CORRECTED PRESSURE (PSIA) = 73.4069 VAPOR PRESSURE (PSIA) = .2391 VOLUME (CU.FT.) = 1803000.0 AIR MASS (LBM) = 700215.2
| |
| | |
| SUM!tARY OF MEASURED DATA AT 1700 1109 TEMP 1 = 527.1700 ( 67.500 )
| |
| TEMP 2 = 527.0800 ( 67.410 )
| |
| TEMP 3 = 527.0300 ( 67.360 )
| |
| TEMP 4 = 527.8400 ( 68.170 )
| |
| TEMP 5 = 528.0300 ( 68.360 )
| |
| TEMP 6 = 527.9000 ( 68.230 )
| |
| TEMP 7m 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.2500 ( 68.580 )
| |
| TEMP 9 = 527.9000 ( 68.230 )
| |
| TEMP 10 = 528.0800 ( 68.410 )
| |
| TEMP 11 = 528.2500 ( 68.580 )
| |
| TEMP 12 = 527.7300 ( 68.060 )
| |
| TEMP 13 = 527.7600 ( 68.090 )
| |
| TEMP 14 = 527.6200 ( 67.950 )
| |
| TEMP 15 = 527.7500 ( 68.080 )
| |
| TEMP 16 = 527.6700 ( 68.000 )
| |
| TEMP 17 = 527.9200 ( 68.250 )
| |
| TEMP 18 = 527.5600 ( 67.890 )
| |
| PRES 1= 73.6364 ( 74170.0 )
| |
| PRES 2= 73.6518 ( 72470.0 )
| |
| VPRS 1= .2429 ( 58.510 )
| |
| VPRS 2= .2427 ( 58.500 )
| |
| VPRS 3= .2451 ( 58.770 )
| |
| VPRS 4= .237( ( 57.830 )
| |
| VPRS 5= .2310 ( 57.120 )
| |
| VPRS 6= .2417 ( 58.380 )
| |
| i
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1700 DATE = 1109 I
| |
| I TEMPERATURE (DEGREES R.) = 527.7231 CORRECTED PRESSURE (PSIA) = 73.4042 VAPOR PRESSURE (PSIA) = .2399 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700199.5 O
| |
| l 1
| |
| | |
| i
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1715 1109 TEMP 1 = 527.1700 ( 67.500')
| |
| TEMP 2 = 527.0800 (~ 67.410 )
| |
| TEMP 3 = 527.0100 ( 67.340 )
| |
| TEMP 4 = 527.8300 ( .68.160 )
| |
| TEMP 5 = 528.0200' ( 68.350 ) j TEMP 6 = 527.9000 ( 68.230 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1400 ( 68.470 )
| |
| TEMP 9 = 527.8900 ( 68.220 )
| |
| TEMP 10 = 528.0900 ( 68.420 )
| |
| TEMP 11 = 528.2700 ( 68.600 )
| |
| TEMP 12 = 527.7300 ( 68.060 )
| |
| TEMP 13 = 527.7500 ( 68.080 )
| |
| TEMP 14 = 527.6300 ( 67.960 )
| |
| TEMP 15 = 527.7500 ( 68.080 )
| |
| TEMP 16 = 527.6700 ( 68.000 )
| |
| TEMP 17 = 527.9400 ( 68.270 )
| |
| TEMP 18'= 527.5600 ( 67.890 )
| |
| PRES 1= 73.6334 ( 74167.0 )
| |
| PRES 2= 73.6487 ( 72467.0 )
| |
| VPRS 1= .2431 ( 58.540 )
| |
| VPRS 2= .2419 ( 58.400 )
| |
| VPRS 3= .2449 ( 58.750 )
| |
| VPRS 4= .2367 ( 57.800 )
| |
| VPRS 5= .2321 ( 57.250 )
| |
| VPRS 6= .2418 ( 58.390 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1715 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7190 CORRECTED PRESSURE (PSIA) = 73.4012 VAPOR PRESSURE (PSIA) = .2399 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700175.9 O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1730 1109 TEMP 1 = 527.1700 ( 67.500 )
| |
| TEMP 2 = 527.0900 ( 67.420 )
| |
| TEMP 3 = 527.0400 ( 67.370 )
| |
| TEMP 4 = 527.8200 ( 69 150 )
| |
| TEMP 5 = 528.0200 ( 69 350 )
| |
| TEMP 6 = 527.8900 ( '68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1900 ( 68.520 )
| |
| TEMP 9 = 527.8900 ( 68.220 )
| |
| TEMP 10 = 528.0800 ( 68.410 )
| |
| TEMP 11 = 528.2400 ( 68.570 )
| |
| TEMP 12 = 527.7300 ( 68.060 )
| |
| TEMP 13 = 527.7500 ( 68.080 )
| |
| TEMP 14 = 527.6300 ( 67.960 )
| |
| TEMP 15 - S27.7500 ( 68.080 )
| |
| TEMP 16 = 527.6700 ( 68.000 )
| |
| TEMP 17 = 527.9600 ( 68.290 )
| |
| TEMP 18 = 527.5500 ( 67.880 )
| |
| PRES 1= 73.6314 ( 74165.0 )
| |
| PRES 2= 73.6467 ( 72465.0 )
| |
| VPRS 1= .2429 ( 58.520 )
| |
| VPRS 2= .2421 ( 58.430 )
| |
| VPRS 3= .2448 ( 58.730 )
| |
| VPRS 4= .2369 ( 57.820 )
| |
| VPRS 5= .2289 ( 56.870 )
| |
| VPRS 6= .2412 ( 58.320 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1730 DATE = 1139 TEMPERATURE (DEGREES R.) = 527.7217 CORRECTED PRESSURE (PSIA) = 73.3998 VAPOR FRESSURE (PSIA) = .2392 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700159.5 i h 1
| |
| | |
| i i
| |
| r
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1745 1109 ,
| |
| TEMP 1 = 527.1800 ( 67.510 )
| |
| TEMP 2 = 527.1000 ( 67.430 )
| |
| TEMP 3 = 527.0400 ( 67.370 ) ;
| |
| TEMP 4 = 527.8200 ( 68.150 ) !
| |
| TEMP 5 = 528.0100 ( 68.340 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.2700 ( 68.600 )
| |
| TEMP 9 = 527.8800 ( 68.210 )
| |
| TEMP 10 = 418.0800 ( 68.410 )
| |
| TEMP 11 = 528.2600 ( 68.590 )
| |
| TEMP 12 = S27.7100 ( 68.040 )
| |
| TEMP 13 = 527.7500 ( 68.080 )
| |
| TEMP 14 = 527.6200 ( 67.950 )
| |
| TEMP 15 = 527.7500 ( 68.080 )
| |
| TEMP 16 = 527.6400 ( 67.970 )
| |
| TEMP 17 = 527.9200 ( 68.250 )
| |
| TEMP 18 = 527.5500 ( 67.880 )
| |
| PRES 1= 73.6284 ( 74162.0 )
| |
| PRES 2: = 73.6437 ( 72462.0 )
| |
| l () VPRS VPRS 1=
| |
| 2=
| |
| .2434
| |
| .2415
| |
| (
| |
| (
| |
| 58.580 )
| |
| 58.360 )
| |
| VPRS 3= .2453 ( 58.790 )
| |
| VPRS 4= .2363 ( 57.750 )
| |
| VPRS 5= .2341 ( '57.490 )
| |
| VPRS 6= .2408 ( 58.270 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1745 DATE = 1109 f' TEMPERATURE (DEGREES R.) = 527.7166 CORRECTED PRESSURE (PSIA) = 73.3960 VAPOR PRESSURE (PSIA) = .2400 VOLUME (CU.FT.) = 1365000.0 AIR MASS (LBM) = 700130.0
| |
| (~ '
| |
| V)
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1800 1109 TEMP 1 = 527.1800 ( 67.510 )
| |
| TEMP 2 = 527.1000 ( 67.430 )
| |
| TEMP 3 = 527.0500 ( 67.380 )
| |
| TEMP 4 = 527.8100 ( 68.140 )
| |
| TEMP 5 = 528.0000 ( 68.330 )
| |
| TEMP 6 = 527.8800 ( 68.210 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.1600 ( 68.490 )
| |
| TEMP 9 = 527.8700 ( 68.200 )
| |
| TEMP 10 = 528.1000 ( 68.430 )
| |
| TEMP 11 = 528.2500 ( 68.580 )
| |
| TEMP 12 = 527.7300 ( 68.060 )
| |
| TEMP 13 = 527.7500 ( 68.080 )
| |
| TEMP 14 = 527.6200 ( 67.950 )
| |
| TEMP 15 = 527.7500 ( 68.080 )
| |
| TEMP 16 = 527.6400 ( 67.970 )
| |
| TEMP 17 = 527.9200 ( 68.250 )
| |
| TEMP 18 = 527.5500 ( 67.880 )
| |
| k PRES 1= 73.6255 ( 74159.0 ) l PRES 2= 73.6416 ( 72460.0 )
| |
| VPRS 1= .2429 ( 58.520 )
| |
| VPRS 2= .2414 ( 58.350 )
| |
| VPRS 3= .2442 ( 58.670 )
| |
| VPRS 4= .2360 ( 57.720 )
| |
| VPRS 5= .2307 ( 57.080 )
| |
| VPRS 6= .2414 ( 58.350 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA I TIME = 1800 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7133 CORRECTED PRESSURE (PSIA) = 73.3943 VAPOR PRESSURE (PSIA) = .2392 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700118.1 l
| |
| l l
| |
| i I
| |
| | |
| ==SUMMARY==
| |
| .OF MEASURED DATA AT 1815.1109 TEMP- 1 = 527.2000 ( 67.530 )
| |
| TEMP 2 = 527.1100 ( 67.440-)
| |
| TEMP- 3 = 527.0700 ( 67.400 )
| |
| TEMP 4 = 527.8200 ( 68.150 )
| |
| TEMP: 5 = 528.0200 ( 68.350 )-
| |
| TEMP 6 = 527.8900 ( ~68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.3900 ( 68.720 )
| |
| TEMP 9 = 527.8800 ( 68.210 )
| |
| TEMP 10'= 528.0800 ( 68.410 )
| |
| TEMP 11 = 528.2400 ( 68.570 )
| |
| TEMP 12 = 527.7200 ( 68.050 )
| |
| TEMP 13 = 527.7500 ( 68.080 ).
| |
| TEMP 14 = 527.6100 ( 67.940.)
| |
| TEMP 15 = 527.7400 ( 68.070 )
| |
| TEMPR16 = 527.6500, ( 67.980 )
| |
| TEMP-17 = 527.9100 ( 68.240 )
| |
| TEMP 18.= 527.5300 ( 67.860 )
| |
| PRES 'l = 73.6235 ( 74157.0 )
| |
| -PRES 2= 73.6396 ( 72458.0 )
| |
| ) VPRS 1= .2428 ( 58.510 )
| |
| VPRS 2= .2417 ( 58.380 )
| |
| VPRS 3= .2447 ( 58.720 )
| |
| VPRS -4 = .2371 ( 57.840 )
| |
| VPRS 5= .2306 ( 57.070 )
| |
| VPRS 6= .2410 ( 58.300 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1815 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7210 CORRECTED PRESSURE (PSIA) = 73.3921 VAPOR PRESSURE (PSIA) = .2394 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700086.8 p
| |
| O
| |
| | |
| ==SUMMARY==
| |
| OF MEASURED DATA AT 1830 1109 TEMP 1 = 527.2100 ( 67.540 )
| |
| TEMP 2 = 527.1100 ( 67.440 )
| |
| TEMP 3 = 527.0600 ( 67.390 )
| |
| TEMP 4 = 527.8200 ( 68.150 )
| |
| TEMP 5 = 528.0000 ( 68.330 )
| |
| TEMP 6 = 527.8900 ( 68.220 )
| |
| TEMP 7 = 536.4400 ( 76.770 )
| |
| TEMP 8 = 528.2800 ( 68.610 )
| |
| TEMP 9 = 527.8900 ( 68.220 )
| |
| TEMP 10 = 528.0800 ( 68.410 )
| |
| TEMP 11 = 528.2400 ( 68.570 )
| |
| TEMP 12 = 527.7100 ( 68.040 )
| |
| TEMP 13 = 527.7300 ( 68.060 )
| |
| TEMP 14 = 527.6000 ( 67.930 )
| |
| TEMP 15 = 527.7200 ( 68.050 )
| |
| TEMP 16 = 527.6300 ( 67.960 )
| |
| TEMP 17 = 527.8800 ( 68.210 )
| |
| TEMP 18 = 527.5300 ( 67.860 )
| |
| PRES 1= 73.6205 ( 74154.0 )
| |
| PRES 2= 73.6376 ( 72456.0 )
| |
| VPRS 1= .2424 ( 58.460 )
| |
| VPRS 2= .2425 ( 58.470 )
| |
| VPRS 3= .2448 ( 58.730 )
| |
| VPRS 4= .2383 ( 57.980 )
| |
| VPRS 5= .2313 ( 57.160 )
| |
| VPRS 6= .2414 ( 58.340 )
| |
| | |
| ==SUMMARY==
| |
| OF CORRECTED DATA TIME = 1830 DATE = 1109 TEMPERATURE (DEGREES R.) = 527.7065 CORRECTED PRESSURE (PSIA) = 73.3891 VAPOR PRESSURE (PSIA) = .2399 VOLUME (CU.FT.) = 1865000.0 AIR MASS (LBM) = 700077.3 9
| |
| | |
| 'O APPENDIX I Type B & c Test Results r
| |
| l l
| |
| O I
| |
| O l
| |
| _ _ - - - - - - _ - _ - - _ - _ - - - - - - - _ - - - - - - - - - - - - ~
| |
| | |
| Tvoe B & C 'Ibst Tissults (Refuelirn Outace 8)
| |
| I
| |
| \ .
| |
| Isakage Rate, acxn L' Penetration Valve No. As Ebund As Inft 7A CV-1814
| |
| * 9.972 CV-1816 *
| |
| * CV-1818 4.18 18.65 7A SV-1840 8.72 8.72 7B CV-1054 *
| |
| * CV-1845 0.61 0.61 9 CV-1270 *
| |
| * CV-1271 *
| |
| * CV-1272 *
| |
| * CV-1273 *
| |
| * CV-1274 0.39 1.78 11 CV-4803 *
| |
| * CV-4804 2.01 2.01 14 CV-1214 3.53 20.28 CV-1216 6.13 21.61 14 CV-1221 0.0 4.45 O *
| |
| 'V 19 SF-42 *
| |
| * SF-43 108.01 108.01 19 SF-44 38.59 38.59 24A CV-7445 *
| |
| * SV-7456 *
| |
| * SV-7469 *
| |
| * SV-7510 29.73 43.7 24A CV-7446 34.5 34.5 24B CV-7450 *
| |
| * CV-7449 *
| |
| * SV-7459 33.96 119.69 25 SV-7454 *
| |
| * SV-7512 0.0 0.0 25 CV-7453 3.83 2.2 31 MU-35A *
| |
| * N2-3 *
| |
| * N2-61 1665.96 1.68
| |
| * Valves were tested simultaneously.
| |
| 1
| |
| | |
| +
| |
| Tvoe B & C Test Results (Refuelim Outaae 8) h'V F+reuatico Valve No.
| |
| I.eakage Rate, acam As Fourd As Isft 32 N2-5 *
| |
| * NJ-35B 551.04 0.53 33 CV-1416 8.55 2.50 39 CV-1065 9.84 9.84 40- CV-5611 *
| |
| * CV-5612 6.33 7.23 41 CV-1667 184.8 184.8 42 W-19 *
| |
| * W-20 1.99 0.31 43 BA-140 *
| |
| * BA-141 0.0 46.19 46 IA *
| |
| * IA-37 0.605 4.18 47 CV-2235 42.07 42.07 48 E -17 *
| |
| * E-18 0.92 0.45 49 Blanks 0.54 22.24 -
| |
| 51 CV-6202 1.3 3.64 52 CV-2234 10.36 5.5 53A CV-7443 *
| |
| * SV-7467 *
| |
| * CV-7444 4.65 86.31 53B CV-7447 *
| |
| * SV-7457 *
| |
| * CV-7448 525.92 '44.09
| |
| * Valves were tested simultaneously. l z
| |
| G
| |
| | |
| l Tvoe B & C Test Results (Refuelirn Outace 8)
| |
| [N_- Penetration Valve No.
| |
| Leakage Rate, accm As Fourd As left 54 CV-2233 1.65 8.59 59' CV-6205 *
| |
| * CV-6203 34.12 23.31 60 CV-2221 27.89 12.09 60 CV-2220 36.9 36.9 62 CV-2215 *
| |
| * CV-2214 11.8 11.8 68 CV-4446 44.37
| |
| * CV-4400 18,570. 274.25 I 70 CV-1053 *
| |
| * CV-1052 26.02 116.76 I
| |
| .1 4.77 12.54 i
| |
| C2 0.0 3.13 !
| |
| ,m C3 0.0 176.04 i ')
| |
| 'd' C4 0.0 0.0 V1 0.0 0.0 V2 0.0 0.0 E67 24.58 24.58 All other electrical penetrations had zero leakage.
| |
| * Valves were tested simultaneously.
| |
| 7he total Type B & C " maximum pathway as found" leakage is 21,936.405 accm.
| |
| The total Type B & C "maximtn pathway as left" leakage is 1,497.972 which is within the acceptance criteria of 44,023 acam (60% of Ia) .
| |
| Note: Valves SV-1443 ard SV-1440 associated with penetrations P66 and P67 respectively were local leakage rate tested, although they are not in the type "C" test prupcuu.
| |
| The results are as follows:
| |
| p P66 SV-1443 201.97 V P67 SV-1440 239.49
| |
| | |
| t 1
| |
| Tvoe B & C M Results (Refueli q 0utace 7)
| |
| O.- Per=L.ation Maxinann Pathway As Inft leakage, accm 7B 149.5 4 9 0.0 11 , 86.6 14 9.4 19 10.9 24A 0.0 24B
| |
| ~
| |
| 88.2 25 0.0 33 95.0 39 0.0 40 0.0 41 52.7 43 47.9 46 149.5 47 0.0 49 0.0
| |
| .51 0.0 52- 0.0 53A 141.3 53B 348.4 54 0.0 59 0- 60 62 0.0 0.0 0.0 68 48.2 70 56.2 C1 10.0 C2 0.0 C3 10.0 C1 2384.5 V1 441.0 V2 10.0 All electrical penetrations had zero leakage.
| |
| O
| |
| | |
| Air T__m_k ard Purae Valve TIRP Data 1/14/85 to 2/88 N~' Isildage, Exml Penetration Valve 'A3 As Date Number Number Found left )
| |
| l C1 17.34 17.34 12/20/84.
| |
| C4- Inner Seal 0.0 0.0 3/25/85 outer Seal 0.0 0.0 ,
| |
| l C4 outer Seal 0.0 0.0 1/2/85 C4 Inner Seal 0.0 0.0 1/17/85 outer Seal 0.0 0.0 V1 0.0 0.0 1/13/85 V2 0.0 0.0 C1 8.411 8.411 2/14/85 C4 Inner Seal 0.0 0.0 1/5/85 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 1/6/85 Outer Seal 0.0 0.0 Inner Seal 0.0 0.0 1/7/85 outer Seal 0.0 0.0 O Inner Oa.1 outer Seal Inner Seal 0.0 0.0 0.0 0.0-1/8/85 0.0 .. O . 0 1/9/85 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 1/4/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 3/20/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 3/4/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 5/4/85 outer Seal 0.0 0.0 C1 10.97 10.97 1/14/85 V1 0.0 0.0 2/14/85 V2 0.0 0.0 2/14/85 O !
| |
| l
| |
| __________________-____O
| |
| | |
| Air Irck ard Purne Valve LIRT Data 1/14/85 to 2/88 G Fcru kation Valve th2mber Isakage, acczn As Found As I. eft Date Number C4 Inner Seal 0.0 0.0 2/18/85 outer Seal o.O 0.0 Inner Seal 0.0 0.0 1/17/85 outer Seal 0.0 0.0 4 ,-
| |
| Inner Seal 0.0 0.0 1/9/85
| |
| ::; outer Seal 0.0 0.0 Inner Seal 0.0 0.0 1/15/85 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 1/16/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 3/1/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 3/3/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 3/18/85 outer Seal 0.0 0.0 V1 0.0 0.0 2/8/85 V2 93.9 93.9 C4 Inner Seal 0.0 0.0 4/7/85 outer Seal 0.0 0.0 C1 12.88 12.88 2/11,b5 C4 Inner Seal 0.0 0.0 5/21/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 6/1/85 outer Seal 0.0 0.0 V1 311.94 311.94 4/13/85 V2 0.0 0.0 C4 Inner Seal 0.0 0.0 4/2/85 outer Seal 0.0 0.0 0
| |
| | |
| Air Iock ard Pume Valve TIRI' Data 1/14/85 to 2/88 Isakage, acam
| |
| (]
| |
| * Penetration Valve As As Date Number Number R.uxi Inft C4 Inner Seal 0.0 0.0 4/15/85 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 4/14/85 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 4/14/85 l outer Seal 0.0 0.0 Inner Seal 0.0 0.0 4/10/85 Outer Seal 9.0 0.0 Inner Seal C.0 0.0 4/13/85 Outer Seal 0,0 0.0 Inner Seal 0.0 0.0 4/16/85 Out M Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 6/6/85 Outer Seal 0.0 0.0 Barrel 0.0 0.0 C4 Inner Seal 0.0 0.0 6/30/85 Outer Seal 0.0 0.0 Inner Seal 0.0 0.0 7/1/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 5/28/85 Outer Seal 0.0 0.0 C1 12.83 12.83 2/3/85 C4 Inner Seal 0.0 0.0 2/10/85 outer Seal 0.0 0.0 V1 0.0 0.0 1/25/85 v2 0.0 0.0 C4 Inner Seal 0.0 0.0 1/23/85 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 1/15/85 Outer Seal 0.0 0.0 Inner Seal 0.0 0.0 1/22/85 outer Seal 0.0 0.0 Inner Seal O.0 0.0 1/19/85 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 1/24/85 Outer Seal 0.0 0.0 C1 13.9 13.9 4/12/85 l
| |
| b
| |
| | |
| l Air Iock ard Pume Valve LTRP Data 1/14/85 to 2/88 l
| |
| (''T i, Isakage, acam V Penetration Valve As As Date l
| |
| Number Number Found Inft C2 Inner Seal 0.0 0.0 8/2/85 outer Seal 0.0 0.0 Barrel 0.0 0.0 C4 Inner Seal 0.5 0.5 8/13/85 l outer Seal 0.0 0.0 Inner Seal 0.0 0.0 8/13/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 9/9/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 8/12/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 7/29/85 outer Seal 0.0 0.0 Inri Seal 0.0 0.0 7/30/85 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 7/30/85 outer Seal 0.0 0.0 t'
| |
| C)/ V1 V2 0.0 0.0 0.0 0.0 9/24/85 V1 0.0 0.0 8/24/85 v2 0.0 0.0 C4 Inner Seal 0.0 0.0 9/2/85 outer Seal 0.0 0.0 C4 Ir.ner Seal 0.0 0.0 9/26/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 9/26/85 outer Seal 0.0 0.0 C1 15.7 15.7 9/24/85 C4 Inner Seal 0.0 0.0 9/24/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 10/3/85 outer Seal 0.0 0.0 Inner Scal 0.0 0.0 10/2/85 outer Seal 0.0 0.0 e~s v
| |
| | |
| _-__-___.______-_--._____--7 Air im_ic ard Purae Valve TIRP Data 1/14/85 to 2/88 1 Penetraticri Valve As As Data Ninnhar Number Founcl left-
| |
| ~ C4' Inner Seal 0.0 0.0 10/4/85 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 10/5/85 Outar Seal .0.0 0.0 Inner Seal 0.0 0.0 10/5/85-Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 10/27/85 Outer Seal 38.1 38.1 C4- Inner Seal 21.36 11.36 10/28/85 Outer Seal 60.4 60.4-C4 Inner Seal 0.0 0.0 8/25/85 Outer Seal 0.0 0.0 Inner Seal 0.0 0.0 8/26/85 Outer Seal 0.0 0.0 C4 Inner Seal O.0 0. 0 - 8/24/85- 'j Outer Seal 0.0 0.0 Inner Seal 0.0 0.0 8/25/85 Outer Seal 0.0 0.0 C4 ' Inner Seal 0.0 0.0 10/20/85 Outer Seal 0.0 0.0 C4 Inner Seal 11.56 11.36 12/4/85 Outer Seal 60.4 60.4 V1 0.0 0.0 1/31/86 V2 0.0 0.0-C2 Inner Seal 0.0 0.0 2/20/86 Outer Seal 10.1 0.0 Barrel 0.0 0.0 l
| |
| l C1 25.8 25.8 1/24/86 C4 Inner Seal 0.0 0.0 2/21/85 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 4/8/86 Outer Seal 0.0 0.0 0 .
| |
| | |
| ,a3 Air Ts_vk and'Purae Valve TIRP Data 1/14/85 to 2/88
| |
| ~
| |
| /)
| |
| b Penetration Valve Isakage, acczn As As Date M nnhm- M n*=t- Found Inft s
| |
| C4 Inner Seal 0.0 0.0 1/6/86-outer Seal 0.0 0.0 C4- Inner Seal 0.0 0.0 2/1/85 outer Seal: 0.0 0.0 Inner Seal 0.0 0.0 2/2/86 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 2/3/86 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 2/7/85 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 5/11/86 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 6/3/86 outer Seal 0.0 0.0 C2 Inner Seal 0.0 0.0 6/11/86 outer Seal 8.8 8.8 Barrel 393.8 393.8 C2 Inner Seal 0.0 0.0 6/3/86 ''
| |
| outer Seal 0.0 0.0 Barrel 0.0 0.0 C4 Inner Seal 0.0 0.0 7/30/86 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 7/31/86 outer Seal 0.0 0.0 Inner Seal 0.0 00 7/29/86 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 9/5/86 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 9/7/86 outer Seal 0.0 0.0 ;
| |
| Barrel 0.0 0.0 !
| |
| C4 Inner Seal 0.0 0.0 1/7/86 outer Seal 0.0 0.0 Barrel 2483.5 2483.5 0
| |
| | |
| Air I.ock and RIrae Valve LTRP Data 1/14/85 to 2/88 Isakage, acam LG- Fer= Lation Valve As As Date Number Number Found Inft C4 Inner Seal 0.0 0.0 12/;.4/86 outer seal 0.0 0.0 Barrel 0.0 0.0 V1 3658.8 3658.8 12/18/86 V2 0.0 0.0 C2 Inner Seal 0.0 0.0 1/17/87 outer seal 0.0 0.0 Barrel 0.0 0.0 C4 Inner seal 0.0 0.0 1/12/87 outer seal 0.0 0.0 Inner Seal 0.0 0.0 1/18/87 outer seal 0.0 0.0 Inner seal 0.0 0.0 1/19/87 outer seal 0.0 0.0 V1 0.0 0.0 12/26/86 v2 0.0 0.0
| |
| . C4 Inner seal 0.0 0.0 2/3/87 outer seal 0.0 0.0 i V1 596.28 596.28 1/17/86 v2 0.0 0.0 C4 Inner Seal 0.0 0.0 12/26/86 outer seal 0.0 0.0 Inner Seal 0.0 0.0 12/28/86 outer seal 0.0 0.0 Inner Seal 0.0 0.0 12/27/86 outer seal 0.0 0.0 Inner Seal 0.0 0.0 12/19/86 outer seal 0.0 0.0 Inner Seal 0.0 0.0 12/20/86 outer seal 0.0 0.0 Inner Seal 0.0 0.0 12/21/86 oute.r Seal 0.0 0.0 Inner Seal 0.0 0.0 12/22/86 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 12/23/86 i outer Seal 0.0 0.0 l C4 Inner Seal 0.0 0.0 1/1/87 outer seal 0.0 0.0 O
| |
| l l'
| |
| | |
| Air Trvik ard Purae Valve TIRP Data 1/14/85 to 2/88 Isakage, acczn Penetration . Valve' As. As Data punhar Mahar Found left C2 Inner Seal 0.0 0.0 6/5/87 Outer Seal 0.0 0.0 Barrel 0.0 0.0 C4 Inner Seal 0.0 0.0 6/2/87 Outer Seal 0.0 0.0 Barrel 0.0 0.0 C4 Inner Seal 0.0 0.0 8/9/S7 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 8/4/87 Outer Seal 0.0 0.0 Inner Seal 0. 0 - 0.0 8/4/87 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 8/15/87
| |
| ~
| |
| OutAir Seal O.0 0.0 C4 Inner Seal 0.0 0.0 8/24/87 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 8/12/87 I
| |
| Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 8/26/87 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 9/7/87 Outer Seal 0.0 0.0 C4 Outer Seal 0.0 0.0 1/7/87 C4 Inner Seal 0.0 0.0 10/17/87 l
| |
| Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 10/31/87 Outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 10/27/87 l Outer Seal 0.0 0.0 V1 0.0 0.0 11/2/87 V2 0.0 0.0 C1 7.63 7.63 11/1/87 O
| |
| _ _ _ _ _ - - - _ - _ - - _ - - - _ - - - _ - _ - - - - - - - - - - - - - - - _ - _ - - - - - - - _ _ - - - - - - - - - _ - - - - - - - - - - a
| |
| | |
| l .
| |
| l Air Inck and Pume Valve IIRI' Data 1/14/85 to 3/J3
| |
| () Penetration Valve Leakage, ac m
| |
| (/ As As Ihte IAmiber ihnaber Fourd Ieft C4 Inner Seal 0.0 0.0 2/3/87 outer Seal 0.0 0.0 Barrel 0.0 0.0 C2 Inner Seal 28.03 28.03 2/12/87 outer Seal 0.0 0.0 Barrel 0.0 0.0 C4 Inner Seal 0.0 0.0 11/3/87 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/4/87 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/12/87 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/13/87 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/2/87 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/5/87 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/6/87
| |
| ^ outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/11/87 outer Seal 0.0 0.0 Inner Seal 0.0 0.0 11/16/87 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 2/5/88 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 1/27/88 outer Seal 0.0 0.0 C1 98.64 98.64 1/27/88 C4 Inner Seal 0.0 0.0 2/19/88 outer Seal 0.0 0.0 C4 Inner Seal 0.0 0.0 2/19/88 outer Seal 0.0 0.0 g
| |
| | |
| ISG CALCULATION
| |
| ( ANSI /ANS 56.8 - 1981-)-
| |
| . ........... ....... ...... ........... . . .====___ ... ....==
| |
| CALIBRATION DATA-SENSOR DISPLAY
| |
| # OF. SENSORS SENSITIVITY (E) REPEATABILITY (r)-
| |
| TEMPERATURE (T) '17 0.050 deg. F 0.010 deg. F
| |
| ~ PRESSURE (P)J 2 0.0005 psia 0.001 psia VAPOR PRESS (Pv). 6 0.100 deg. F 0.010 deg. F LENGTH OF TEST (t) 10.00 hrs PRESSURE (P) 73.79' psia TEMPERATURE (T) 528.3 deg. R
| |
| . VAPOR PRESS (Pv) .0.00857 psi /deg. F ~(at 58 deg. F) 1 La 'O.200 wt%/ day INSTRUMENT MEASUREMENT ERRORS 2' 2- 1/2 1/2 eT = [(ET) + (rT) ] /[# of sensors]
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| eT = .0.01237 deg. F 2: 2- 1/2- 1/2 eP = [ (EP) + (rP) ] /[# of sensors]
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| eP = 0.00079 psia 2 2 1/2 1/2 ePv = [ (EPV) + (rPv) ] /[# of sensors] z ePv = 0.00035 psia INSTRUMENT SELECTION GUIDE I l
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| 2 2 2 1/2 l ISG = 2400/t[ 2 (eP/P) + 2 (ePv/P) + 2(eT/T) ]
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| ISG = 0.009 wt%/ day
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| .25La = 0.050 wt%/ day
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