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1 ASTM 5A CRUDE OILS ∆t = 12 ALFA 0.0003347 API GRAVITY 8.5 AT 72 ˚F RHO= 1009.7157 VCF= 0.9959792 API GRAVITY 7.96 AT 60 ˚F RHOT= 1009.5599 RHO60 1013.6356 HYC= 0.9998457 ASTM 5B OIL PRODUCTS RHO= 766.17993 1 API GRAVITY 53 AT 70 ˚F HYC= 0.9998716 rho60= 766.08154 API GRAVITY 51.81982 AT 60 ˚F ∆t = 10 alfa= 0.000646 rhot= 766.08154 vcf= 0.9935272 k0= 192.4571 k1= 0.2438 API 53.023697 ASTM 6A CRUDE OILS K0 341.0957 ALFA 0.0006557 API GRAVITY 64.5 AT 60 ˚F RO= 721.2255 DELTA 36 VCF TO 60˚F 0.97623 AT 96 ˚F ASTM 6B OIL PRODUCTS RHO= 992.00139 k0= 103.872 API GRAVITY 11 AT 60 ˚F ∆t = 58 k1= 0.2701 VCF TO 60˚F 0.97794 AT 118 ˚F alfa= 0.0003778 ASTM 6C OIL PRODUCTS TEC 910 AT 60 ˚F VCF TO 60˚F 1.0271 AT 30 ˚F ASTM 23A CRUDE OILS ∆t = 0 RHO60= 649.3578 REL. DENSITY 0.6500 AT 60 ˚F HYC= 1 ALFA= 0.0008089 REL. DENSITY 0.65000 AT 60 ˚F RHO= 649.3578 VCF= 1 ASTM 23B OIL PRODUCTS ∆t = -60 RHO60= 1042.7452 REL. DENSITY 1.0430 AT 0 ˚F HYC= 1.0007445 ALFA= 0.0003546 REL. DENSITY 1.02160 AT 60 ˚F RHO= 1041.9695 VCF= 1.0211316 FUEL OIL FUEL OIL ASTM 24A CRUDE OILS ∆t = 165 RHO60= 1074.9369 REL. DENSITY 1.076 AT 60 ˚F HYC= 0.9977225 ALFA= 0.0002952 VCF TO 60˚F 0.95065 AT 225 ˚F RHO= 1074.9369 VCF= 0.9506539 ASTM 24B OIL PRODUCTS ∆t = 135.5 RHO60= 669.33804 REL. DENSITY 0.67 AT 60 ˚F HYC= 0.9981545 ALFA= 0.0007938 VCF TO 60˚F 0.88975 AT 195.5 ˚F RHO= 669.33804 VCF= 0.8897469 GASOLINE ASTM 24C OIL PRODUCTS TEC 650 AT 60 ˚F VCF TO 60˚F 1.0194 AT 30 ˚F ASTM 53A CRUDE OILS ∆t = 10 RHO15= 778.81927 DENSITY 779.0 AT 25 ˚C HYC= 0.999768 ALFA= 0.0010122 DENSITY 786.65 AT 15 ˚C RHO= 778.81927 VCF= 0.9898477 ASTM 53B OIL PRODUCTS ∆t = -10.5 RHO15= 1008.2412

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ASTM tables

ASTM Tables12345678910ASTM5ACRUDE OILSt =12ALFA0.00033466630.00033198050.0003320020.00033200190.00033200190.00033200190.00033200190.00033200190.00033200190.0003320019API GRAVITY8.5AT72FRHO=1009.7157VCF=0.99597920660.9960115130.9960112540.99601125610.9960112560.9960112560.9960112560.9960112560.9960112560.996011256API GRAVITY7.96AT60FRHOT=1009.5599485261RHO601013.6355677211013.60268964621013.60295327741013.60295116341013.60295118041013.60295118021013.60295118021013.60295118021013.60295118021013.6029511802HYC=0.9998457472ASTM5BOIL PRODUCTSRHO=766.179934959412345678910API GRAVITY53AT70FHYC=0.99987158rho60=766.0815421321771.0725790718771.0245438515770.9951956511770.9976262321770.9991114836770.9989884703770.9989133012770.998919527770.9989233313http://www.bgicrew.com/API GRAVITY51.81982AT60Ft =10alfa=0.00064604990.00063988350.00063611550.00063642760.00063661830.00063660250.00063659280.00063659360.00063659410.0006365941-rhot=766.0815421321vcf=0.99352715030.99358904750.99362686880.99362373640.99362182230.99362198080.99362207770.99362206970.99362206480.9936220652 ., . 23, . ,k0=192.4571192.4571???????? , 5- ,k1=0.24380.2438????????. - 191002 API53.023696533151.829302372851.840723881351.847702809851.847124803551.846771603951.84680085751.846818732551.84681725251.8468163473ASTM6ACRUDE OILSK0341.0957ALFA0.0006557437.: +7 812 346 80 08API GRAVITY64.5AT60FRO=721.2255DELTA36: +7 812 346 73 32VCF TO 60F0.97623AT96FE-mail : [email protected] PRODUCTSRHO=992.0013894737k0=103.872 API GRAVITY11AT60Ft =58k1=0.2701PLACE FOR YOUR ADVERTISEMENTVCF TO 60F0.97794AT118Falfa=0.0003778317ASTM6COIL PRODUCTSTEC910AT60FVCF TO 60F1.0271AT30FASTM23ACRUDE OILSt =0RHO60=649.3578649.3578649.3578649.3578649.3578649.3578649.3578649.3578649.3578649.3578REL. DENSITY0.6500AT60FHYC=1ALFA=0.00080892470.00080892470.00080892470.00080892470.00080892470.00080892470.00080892470.00080892470.00080892470.0008089247REL. DENSITY0.65000AT60FRHO=649.3578VCF=1111111111ASTM23BOIL PRODUCTSt =-60RHO60=1042.74524146531021.16633754161020.60132748371020.58615501391020.58574730781020.58573635191020.58573605751020.58573604961020.58573604941020.58573604941020.58573604941020.58573604941020.58573604941020.58573604941020.58573604941020.58573604941020.58573604941020.5857360494REL. DENSITY1.0430AT0FHYC=1.00074448ALFA=0.00035455830.00036411210.00036436880.00036437570.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.00036437590.0003643759REL. DENSITY1.02160AT60FRHO=1041.969516VCF=1.02113162481.02169692851.02171211741.02171252561.02171253661.02171253691.02171253691.02171253691.02171253691.02171253691.02171253691.02171253691.02171253691.02171253691.02171253691.02171253691.02171253691.0217125369REL.D1.04377649261.02217624771.02161067881.02159549141.02159508331.02159507231.0215950721.0215950721.0215950721.0215950721.0215950721.0215950721.0215950721.0215950721.0215950721.0215950721.0215950721.021595072FUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILASTM24ACRUDE OILSt =165RHO60=1074.9369121074.936912Volume:500M3REL. DENSITY1.076AT60FHYC=0.997722505ALFA=0.00029519590.0002951959Volume at 15oC:475.3269370356M3VCF TO 60F0.95065AT225FRHO=1074.936912VCF=0.95065387410.9506538741Weight in Vac.at 15oC:0.5114517843M.T.Weight in Air at 15oC:-0.0114078465M.T.ASTM24BOIL PRODUCTSt =135.5RHO60=669.33804Volume:500M3REL. DENSITY0.67AT60FHYC=0.9981544764ALFA=0.0007938193Volume at 15oC:444.8734323475M3VCF TO 60F0.88975AT195.5FRHO=669.33804VCF=0.8897468647Weight in Vac.at 15oC:0.2980651997M.T.GASOLINEWeight in Air at 15oC:-0.1912955759M.T.ASTM24COIL PRODUCTSVolume:500M3TEC650AT60FVolume at 15oC:509.690611961M3VCF TO 60F1.0194AT30FASTM53ACRUDE OILSt =10RHO15=778.819272786.807168616786.6437167345786.6470106842786.6469442825786.6469456211786.6469455941786.6469455946786.6469455946786.6469455946786.6469455946786.6469455946786.6469455946786.6469455946786.6469455946786.6469455946786.6469455946786.6469455946DENSITY779.0AT25CHYC=0.999768ALFA=0.00101222110.00099177270.00099218490.00099217660.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.00099217680.0009921768DENSITY786.65AT15CRHO=778.819272VCF=0.98984770740.99005338180.99004923610.99004931970.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.9900493180.990049318ASTM53BOIL PRODUCTSt =-10.5RHO15=1008.241209361001.25276933841001.19100182611001.19045125671001.19044634881001.19044630511001.19044630471001.19044630471001.19044630471001.19044630471001.19044630471001.19044630471001.19044630471001.19044630471001.19044630471001.19044630471001.19044630471001.1904463047DENSITY1008.0AT4.5CHYC=1.000239295ALFA=0.00066615140.00067209370.00067214670.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.00067214710.0006721471DENSITY1001.19AT15CRHO=1008.24120936VCF=1.00697969611.00704182071.00704237451.00704237941.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.00704237951.0070423795FUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILFUEL OILASTM54ACRUDE OILSt =40RHO15=1050Volume:500M3DENSITY1050AT15CHYC=0.99947888ALFA=0.000556891Volume at 15oC:488.7912448337M3VCF TO 15C0.97758AT55CRHO=1050VCF=0.9775824897Weight in Vac.at 15oC:513.2308070754M.T.Weight in Air at 15oC:512.693136706M.T.ASTM54BOIL PRODUCTSt =-27.5RHO60=1062Volume:500M3DENSITY1062AT15CHYC=1.0003467612ALFA=0.0006235916Volume at 15oC:508.5286734227M3VCF TO 15C1.01706AT-12.5CRHO=1062VCF=1.0170573468Weight in Vac.at 15oC:540.0574511749M.T.FUEL OILFUEL OILWeight in Air at 15oC:539.4980696342M.T.ASTM54COIL PRODUCTSVolume:500M3TEC1644AT15CVolume at 15oC:526.6338234229M3VCF TO 15C1.0533AT-18CASTM54DLUBE OILSVolume:500M3Density in vac.:875AT15CVolume at 15oC:496.405M3VCF TO 15C0.9928AT25CWeight in Vac.at 15oC:434.354375M.T.Weight in Air at 15oC:433.8083295M.T.ASTM Tables ver 1,1 Oleg Boriskin 2009 e-mail: [email protected]://oleg352.mail333.su/

Oleg:THERMAL EXPANSION COEFFICIENT, X1,000,000 [1/DEG F]Oleg:THERMAL EXPANSION COEFFICIENT, X1,000,000 [1/DEG F]Oleg:THERMAL EXPANSION COEFFICIENT, X1,000,000 [1/DEG F]E-mail : [email protected]://oleg352.mail333.su/

ASTM1ASTMSG TO APIASTMAPI TO SGSG -Specific gravity = RD - Relative Density (60/60oF)SGAPI (60/60F)Dens 600FAPI (60/60F)SGDens 150CAPI - American Petroleum Institute0.946517.9981510829945.564858180.9464882943945.6364548495VCF - Volume Correction FactorASTM54ACRUDE OILVolume:500Density in vac.:0.8546at temp150CVolume at 15oC:499.79Real temp:15.40CWeight in Vac.at 15oC:427.120534VCF:0.9996Weight in Air at 15oC:426.570765http://www.bgicrew.com/ASTM54BOIL PRODUCTSVolume:500-Density in vac.:0.8546at temp150CVolume at 15oC:492.5436453384 ., . 23, . ,Real temp:330CWeight in Vac.at 15oC:420.9277993062 , 5- ,VCF:0.9851Weight in Air at 15oC:420.3860012963. - 191002 ASTM54CVolume:500.: +7 812 346 80 08Temp.Exp.Coef.640at temp150CVolume at 15oC:467.4681875641: +7 812 346 73 32Real temp:1150CWeight in Vac.at 15oC:?E-mail : [email protected]:0.9349Weight in Air at 15oC:?ASTM54DLUBE OILSVolume:500 Density in vac.:0.875at temp150CVolume at 15oC:496.405Real temp:250CWeight in Vac.at 15oC:434.354375VCF:0.9928Weight in Air at 15oC:433.8083295 ASTM c 1ASTM 54D Density at15CDen1Den2ASTM54DLUBE OILS0.8720.8730.874Density in vac.:0.873at temp150CTEMP124.50.99310.993150.9932Real temp:24.60C24.60.993060.993090.99312VCF:0.9931TEMP224.750.99300.9930.9930ASTM Tables ver 1,1 Oleg Boriskin 2009 e-mail: [email protected]://oleg352.mail333.su/

Oleg:999,35?Oleg:Thermal Expansion Coefficient x 1 000 000 (1/deg F)E-mail : [email protected]://oleg352.mail333.su/

rates .=3001 /7 / :254.51781.3 1 .V100%=2000m3V98%=1960m3 :24003/ 8000009,8 m/s2 .1000/3: 1000.81.6326530612

Temp correction 1. - 54 DVolume before1000m30.87515Volume:1000Dens. In Vac0.875at15oC25Volume at 15oC:992.81Temp. before25oC1 temp0.9928Weight in Vac.at 15oC:868.70875Temp. after:50oC0.87515Weight in Air at 15oC:867.616659Difference:18.57m350Volume after1018.57m32 temp0.9747Volume:1018.5696258374Volume at 15oC:992.81ASTM Tables ver 1,1 Oleg Boriskin 2009 e-mail: [email protected] in Vac.at 15oC:868.70875http://oleg352.mail333.su/Weight in Air at 15oC:867.616659

http://oleg352.mail333.su/

Formulas5AVOLUME IGENERALIZED CRUDE OILS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60F5AK0=341.0957PAGE X-80RANGEK1=0.0PAGE X-80APIF0400300WHEREt = t - 60(F)40500250CONVERT API GRAVITY TO DENSITY:501000200t = density at temperature tAPI = observed API gravity999,012 = density of water at 60F, Kg/m3PAGE X-65BVOLUME IIGENERALIZED PRODUCTS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60F5BCONVERT API GRAVITY TO DENSITY:t = density at temperature tRANGEAPI = observed API gravityAPIF999,012 = density of water at 60F, Kg/m304003004050025050850200PAGE X-366AVOLUME IGENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60F AGAINST API GRAVITY AT 60F6AWHEREt = t - 60(F)RANGEAPIF040030040500250501000200999,012 = density of water at 60F, Kg/m3PAGE X-916BVOLUME IIGENERALIZED PRODUCTS CORRECTION OFVOLUME TO 60F AGAINST API GRAVITY AT 60F6BWHEREt = t - 60(F)RANGEAPIF04003004050025050850200999,012 = density of water at 60F, Kg/m3PAGE X-1126CVOLUME IIIVOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 60F AGAINST THERMAL EXPANSION COEFFICIENTS AT 60F6CRANGEWHEREt = t - 60(F) * 106F60 = coefficient of thermal expansionPAGE X-13527051003005105300250530930020023AVOLUME IVGENERALIZED CRUDE OILS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60 / 60F23ADENSITY t at temperature t:t=relative density*999,012999,012 = density of water at 60F, Kg/m3RANGEREL.DENSITYF0,82551,07603000,780,82502500,6110,77950200WHEREt = t - 60(F)PAGE X-15123BVOLUME VGENERALIZED PRODUCTS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60/60F23BDENSITY t at temperature t:t=relative density*999,012999,012 = density of water at 60F, Kg/m3RANGEREL.DENSITYF0,82551,07603000,780,82502500,65350,77950200WHEREt = t - 60(F)PAGE X-18424AVOLUME IVGENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60F AGAINST RELATIVE DENSITY 60 / 60F24AWHEREt = t - 60(F)RANGEREL.DENSITYF0,82551,07603000,780,8250250WHERE60=relative density60/60F*999,012PAGE X-2230,6110,7795020024BVOLUME VGENERALIZED PRODUCTS CORRECTION OF VOLUME TO 60F AGAINST RELATIVE DENSITY 60/60F24BWHEREt = t - 60(F)RANGEREL.DENSITYFOR0,82551,07603000,780,8250250WHERE60=relative density60/60F*999,0120,65350,77950200999,012 = density of water at 60F, Kg/m3PAGE X-24324CVOLUME VIVOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 60F AGAINST THERMAL EXPANSION COEFFICIENTS AT 60F24CRANGEWHEREt = t - 60(F) * 106F60 = coefficient of thermal expansionPAGE X-26627051003005105300250530930020053AVOLUME VIIGENERALIZED CRUDE OILS CORRECTION OF OBSERVED DENSITY TO DENSITY AT 15C53ARANGEDENSITYC610,5778,5-1895779824-18125824,51075-18150where15 = density at the base temperaturet = t - 15(C)PAGE X-28353BVOLUME VIIIGENERALIZED PRODUCTS CORRECTION OF OBSERVED DENSITY TO DENSITY AT 15C53BRANGEDENSITYC653778,5-1890779824-18125824,51075-18150where15 = density at the base temperaturet = t - 15(C)PAGE X-31154AVOLUME VIIGENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 15C AGAINST DENSITY AT 15C54ARANGEwheret = t - 15(C)DENSITYC610,5778,5-1895779824-18125PAGE X-351824,51075-1815054BVOLUME VIIIGENERALIZED PRODUCTS CORRECTION OF VOLUME TO 15C AGAINST DENSITY AT 15C54BRANGEwheret = t - 15(C)DENSITYC653778-1895778,5824-18125PAGE X-371824,51075-1815054CVOLUME IXVOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 15C AGAINST THERMAL EXPANSION COEFFICIENTS AT 15C54CRANGEwheret = t - 15(C) * 106C486918-18150918954-18125PAGE X-3939541674-189554D

ConstantsCONSTANTS1. CRUDE OILSTABLEK0K1RANGE:REMARKS5A,6A341.095700100 API(KG/M3)2/F23A,24A341.095700,61101,0760 RELATIVE DENSITY(KG/M3)2/F53A, 54A613.97230610,51075,0 KG/M3(KG/M3)2/C2.PRODUCTSTABLEK0K1RANGE:REMARKS5B,6B103.8720.2701037 APIFUEL OIL(KG/M3)2/F330.301037,147,9 APIJET GROUP(KG/M3)2/F4852 APIA=-0,0018684; B=1489,067192.45710.243852,185 APIGASOLINES(KG/M3)2/F23B, 24B103.8720.27010,8391,076 RELATIVE DENSITYFUEL OIL(KG/M3)2/F330.30100,7890,8395 RELATIVE DENSITYJET GROUP(KG/M3)2/F0,7710,7885 RELATIVE DENSITYA=-0,0018684; B=1489,067192.45710.24380,65350,7705 RELATIVE DENSITYGASOLINES(KG/M3)2/F53B, 54B186.96960.48628391075 DENSITY, KG/M3FUEL OIL(KG/M3)2/C594.54180788838,5 DENSITY, KG/M3JET GROUP(KG/M3)2/C770,5787,5 DENSITY, KG/M3A=-0,00336312; B=2680,3206346.42280.4388653770 DENSITY, KG/M3GASOLINES(KG/M3)2/C54D00.6278AllLub.Oils(KG/M3)2/CASTM Tables ver 1,1 Oleg Boriskin 2009 e-mail: [email protected]://oleg352.mail333.su/

ExamplesExamples5ACRUDE OILS5BOIL PRODUCTSAPI GRAVITY AT OBSERVED TEMPERATUREAPI GRAVITY AT OBSERVED TEMPERATURE3535.53636.53737.555.54.66.577.5TEMP FCORRESPONDING API GRAVITY AT 60FTEMP FCORRESPONDING API GRAVITY AT 60F19525.726.126.526.927.327.8903.64.14.65.15.66195.525.626.126.526.927.327.790.53.64.14.655.5619625.62626.426.927.327.7913.644.555.56196.525.62626.426.827.227.791.53.544.555.5619725.52626.426.827.227.6923.544.555.55.9197.525.525.926.326.827.227.692.53.544.54.95.45.96ACRUDE OILS6BOIL PRODUCTS6COIL PRODUCTSAPI GRAVITY AT 60FAPI GRAVITY AT 60FCOEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F)5050.55151.55252.53535.53636.53737.5530532534536538540TEMP FFACTOR FOR CORRECTING VOLUME TO 60FTEMP FFACTOR FOR CORRECTING VOLUME TO 60FTEMP FFACTOR FOR CORRECTING VOLUME TO 60F750.99150.99150.99150.99140.99140.99131050.97910.9790.97890.97880.97870.9786750.9920.9920.9920.99190.99190.991975.50.99130.99120.99120.99110.99110.991105.50.9880.97880.97870.97860.97850.978475.50.99180.99170.99170.99170.99160.9916760.9910.99090.99090.99080.99080.99071060.97860.97850.97840.97840.97830.9781760.99150.99150.99140.99140.99140.991376.50.99070.99060.99060.99050.99050.9904106.50.97840.97830.97820.97810.9780.977976.50.99120.99120.99120.99110.99110.9911770.99040.99040.99030.99030.99020.99011070.97810.97810.9780.97790.97780.9777770.9910.99090.99090.99090.99080.990877.50.99010.99010.990.990.98990.9899107.50.97790.97880.97770.97760.97760.977477.50.99070.99070.99060.99060.99060.990523ACRUDE OILS23BOIL PRODUCTSRELATIVE DENSITY AT OBSERVED TEMPERATURERELATIVE DENSITY AT OBSERVED TEMPERATURE0.8270.8290.8310.8330.8350.8370.9410.9430.9450.9470.9490.951TEMP FCORRESPONDING RELATIVE DENSITY 60/60FTEMP FCORRESPONDING RELATIVE DENSITY 60/60F900.83890.84090.84290.84490.84680.84881950.99060.99260.99460.99650.99851.000590.50.83910.84110.84310.84510.8470.849195.50.99080.99280.99480.99670.99871.0007910.83930.84130.84330.84530.84720.84921960.9910.9930.9950.99690.99891.000891.50.83950.84150.84350.84550.84740.8494196.50.99120.99320.99510.99710.99911.001920.83970.84170.84370.84560.84760.84961970.99140.99330.99530.99730.99921.001292.50.83990.84190.84390.84580.84780.8498197.50.99160.00350.99550.99750.99941.001424ACRUDE OILS24BOIL PRODUCTS24COIL PRODUCTSRELATIVE DENSITY 60/60FRELATIVE DENSITY 60/60FCOEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F)0.6120.6140.6160.6180.620.6220.890.8920.8940.8960.8980.9490492494496498500TEMP FCORRESPONDING RELATIVE DENSITY 60/60FTEMP FFACTOR FOR CORRECTING VOLUME TO 60FTEMP FFACTOR FOR CORRECTING VOLUME TO 60F750.98630.98630.98640.98650.98660.98671350.96710.96720.96730.96740.96750.96751050.97780.97770.97760.97750.97740.977475.50.98580.98590.9860.98610.98620.9863135.50.96680.96690.9670.96710.96720.9673105.50.97760.97750.97740.97730.97720.9771760.98530.98540.98550.98560.98570.98581360.96660.96670.96680.96690.9670.96711060.97730.97720.97710.9770.97690.976876.50.98490.9850.98510.98520.98530.9854136.50.96640.96650.96660.96670.96680.9669106.50.97710.9770.97690.97680.97670.9766770.98440.98450.98460.98470.98480.98491370.96620.96630.96640.96650.96660.96671070.97680.97670.97660.97650.97640.976377.50.9840.98410.98420.98430.98440.9845137.50.9660.96610.96620.96630.96640.9665107.50.97660.97650.97640.97630.97620.976153ACRUDE OILS53BOIL PRODUCTSDENSITY AT OBSERVED TEMPERATUREDENSITY AT OBSERVED TEMPERATURE950.0952.0954.0956.0958.0960.0997999.01001.01003.01005.01007.0TEMP CCORRESPONDING DENSITY AT 15CTEMP CCORRESPONDING DENSITY AT 15C-18929.1931.1933.1935.2937.3939.3-0.5986.9988.9990.9992.9994.9996.9-17.75929.2931.3933.3935.4937.4939.5-0.25987.1989.1991.1993.1995.1997.1-17.5929.4931.4933.5935.5937.6939.60987.2989.2991.2993.3995.3997.3-17.25929.5931.6933.6935.7937.7939.80.25987.4989.4991.4993.4995.4997.4-17929.7931.7933.8935.8937.9939.90.5987.6989.6991.6993.6995.6997.6-16.75929.9931.9934936938940.10.75987.7989.7991.7993.7995.8997.854ACRUDE OILS54BOIL PRODUCTS54COIL PRODUCTSDENSITY AT 15 CDENSITY AT 15 CCOEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F)990992.0994.0996.0998.01000.0730732.0734.0736.0738.0740.0800804808812816820TEMP CFACTOR FOR CORRECTING VOLUME TO 15 CTEMP CCORRESPONDING DENSITY AT 15CTEMP CFACTOR FOR CORRECTING VOLUME TO 15C141.00061.00061.00061.00061.00061.0006400.96840.96860.96870.96880.9690.969162.50.96160.96140.96120.9610.96080.960614.251.00051.00051.00051.00051.00051.000540.250.96810.96830.96840.96850.96870.968862.750.96140.96120.9610.96080.96060.960414.51.00031.00031.00031.00031.00031.000340.50.96780.96790.96810.96820.96830.9685630.96120.9610.96080.96060.96040.960214.751.00021.00021.00021.00021.00021.000240.750.96750.96760.96780.96790.9680.968263.250.9610.96080.96060.96040.96020.9615111111410.96720.96730.96740.96760.96770.967963.50.96080.96060.96040.96020.960.959815.250.99980.99980.99980.99980.99980.999841.250.96690.9670.96710.96730.96740.967563.750.96060.96040.96020.960.95980.959654DOIL PRODUCTSDENSITY AT 15 C730732.0734.0736.0738.0740.0TEMP CCORRESPONDING DENSITY AT 15C400.96840.96860.96870.96880.9690.969140.250.96810.96830.96840.96850.96870.968840.50.96780.96790.96810.96820.96830.968540.750.96750.96760.96780.96790.9680.9682410.96720.96730.96740.96760.96770.967941.250.96690.9670.96710.96730.96740.9675

VCFVCF calculationDensity @ 15/vac=0.8668Density @CorrespondingMass5983.445Actual temp=39.50actual tempdcc (approximate)VolumeVCFTable 54A=0.97990.84940.000717044.51Table 54B=0.98000.84950.000717043.79Table 54D=0.98220.85140.000637028.01User infoDensity @ 15/vac=866.8General formula:Actual temp=39.5VCF=exp(b) and :a=(K0+K1xDensity @ 15/vac)/(Density @ 15/vac^2)diff temp=24.5b=-a x diff temp x (1+0,8 x a x diff temp)diff temp=actual temp-15Formula for Table 54B and 770