ASTM Tables

AABAAABBAABNASTM 5A CRUDE OILSAPI GRAVITY 8.5 AT 300 ˚CAPI GRAVITY -1.00 AT 60 ˚F

ASTM 5B OIL PRODUCTS

API GRAVITY 10.5 AT 135 ˚F


ASTM 6A CRUDE OILS Cell 0713792395


VCF TO 60˚F 0.97213 AT 92 ˚F

ASTM 6B OIL PRODUCTSAPI GRAVITY 63 AT 60 ˚F

VCF TO 60˚F 0.9895 AT 75 ˚F

ASTM 6C OIL PRODUCTSTEC 910 AT 60 ˚F

VCF TO 60˚F 1.0271 AT 30 ˚F

ASTM 23A CRUDE OILSREL. DENSITY 0.6500 AT 15 ˚CREL. DENSITY 0.65000 AT 15 ˚C

ASTM 23B OIL PRODUCTSREL. DENSITY 1.0430 AT 0 ˚CREL. DENSITY 1.02160 AT 60 ˚C

FUEL OIL

ASTM 24A CRUDE OILS Volume: 500

REL. DENSITY 1.076 AT 60 ˚F à 475.3269

VCF TO 60˚F 0.95065 AT 225 ˚F 0.511452 M.T.

-0.011408 M.T.

ASTM 24B OIL PRODUCTS Volume: 500

REL. DENSITY 870 AT 15 ˚C à 499.9981

VCF TO 60˚F 1.00000 AT 27.5 ˚C 434.9983 M.T.

FUEL OIL 434.4483 M.T.

ASTM 24C OIL PRODUCTS Volume: 500

TEC 650 AT 60 ˚F à 509.6906VCF TO 60˚F 1.0194 AT 30 ˚F

ASTM 53A CRUDE OILSDENSITY 779.0 AT 25 ˚CDENSITY 786.65 AT 15 ˚C

ASTM 53B OIL PRODUCTSDENSITY 1008.0 AT 4.5 ˚CDENSITY 1001.19 AT 15 ˚C

[email protected]

E-mail : [email protected]

M3

Volume at 15oC: M3

Weight in Vac.at 15oC:

Weight in Air at 15oC:

M3

Volume at 15oC: M3



M3

Volume at 15oC: M3

http://www.wma.go.tz/

mailto:[email protected]


B22

Oleg: THERMAL EXPANSION COEFFICIENT, X1,000,000 [1/DEG F]

B45


FUEL OIL

ASTM 54A CRUDE OILS Volume: 500

DENSITY 1050 AT 15 ˚C à 503.6118

VCF TO 15˚C 1.00722 AT 2 ˚C 528.7924 M.T.

528.2384 M.T.

ASTM 54B OIL PRODUCTS Volume: 500

DENSITY 870 AT 20 ˚C à 497.1747

VCF TO 15˚C 0.99435 AT 27 ˚C 432.542 M.T.

FUEL OIL 431.9951 M.T.

ASTM 54C OIL PRODUCTS Volume: 500

TEC 1644 AT 15 ˚C à 526.6338VCF TO 15˚C 1.0533 AT -18 ˚C

ASTM 54D LUBE OILS Volume: 1000

Density in vac.: 875 AT 15 ˚C à 992.81

VCF TO 15˚C 0.9928 AT 25 ˚C 868.7088 M.T.

867.6167 M.T.

ASTM Tables ver 1,1 © HENRY

M3

Volume at 15oC: M3



M3

Volume at 20 oC: M3



M3

Volume at 15oC: M3

M3

Volume at 15oC: M3



http://oleg352.mail333.su/

http://oleg352.mail333.su/

B67


E-mail : [email protected]


ASTM SG TO API ASTM

SG API (60/60F) API (60/60F) SG 0.9465 17.9981510829 945.564858 18 0.946488

ASTM 54A CRUDE OIL Volume:

Density in vac.: 0.8546 at temp 15

Real temp: 15.4

VCF: 0.9996

ASTM 54B OIL PRODUCTS Volume:


Real temp: 28.5

VCF: 0.9888

ASTM 54C Volume:

Temp.Exp.Coef. 640 at temp 15

Real temp: 115

VCF: 0.9349

ASTM 54D LUBE OILS Volume:


Real temp: 43

VCF: 0.9834

1 ASTM 54D

ASTM 54D LUBE OILS

Density in vac.: 0.873 at temp 15 TEMP1 24.5

Real temp: 24.6 24.6VCF: 0.9931 TEMP2 24.75


Dens 600F

0C Volume at 15oC:0C Weight in Vac.at 15oC:




0C Volume at 15oC:

0C Weight in Vac.at 15oC:




0C0C

D4

Oleg: 999,35?

B17

Oleg: Thermal Expansion Coefficient x 1 000 000 (1/deg F)

API TO SG

API - American Petroleum Institute945.636455 VCF - Volume Correction Factor

500

499.79

427.120534

426.570765

500

494.413595

422.525859

421.982004

500

467.468188

?

?

500

491.71

430.24625

429.705369

Density at 15 ˚CDen1 Den2

0.872 0.873 0.874

0.9931 0.99315 0.9932

0.99306 0.99309 0.993120.9930 0.993 0.9930

SG -Specific gravity = RD - Relative Density (60/60oF)

Dens 150C

0 300 мм1 м/с 7 м/с

254.5 1781.3

2000

19602400

8000001000 : 1000

81.6326531

V100%= m3

V98%= m3

9,8 m/s2

Volume before 1000 ###

Dens. In Vac 0.875 at 15

Temp. before 25 1 temp

Temp. after: 50 ###

Difference: 18.57 ###

Volume after 1018.57 2 temp


m3

oCoCoC

m3

m3

Volume at 15oC:


5A VOLUME I GENERALIZED CRUDE OILS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60°F

5A341.0957 PAGE X-80 RANGE

0.0 PAGE X-80 ˚API0…40

WHERE ∆t = t - 60 (˚F) 40…50CONVERT API GRAVITY TO DENSITY: 50…100

API = observed API gravity

PAGE X-6

5B VOLUME II

5B CONVERT API GRAVITY TO DENSITY:

RANGEAPI = observed API gravity ˚API

0…4040…5050…85

PAGE X-366A VOLUME I GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60°F AGAINST API GRAVITY AT 60°F

6AWHERE ∆t = t - 60 (˚F) RANGE

˚API0…4040…5050…100

PAGE X-91

6B VOLUME II

6BWHERE ∆t = t - 60 (˚F) RANGE

˚API0…4040…5050…85

PAGE X-112

6C VOLUME III

6C RANGE

WHERE ∆t = t - 60 (˚F)

PAGE X-135 270…510510…530

K0=

K1=

ρt = density at temperature t

999,012 = density of water at 60˚F, Kg/m3

GENERALIZED PRODUCTS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60°F

ρt = density at temperature t



GENERALIZED PRODUCTS CORRECTION OFVOLUME TO 60°F AGAINST API GRAVITY AT 60°F


VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 60°F AGAINST THERMAL EXPANSION COEFFICIENTS AT 60°F

α * 106

α60 = coefficient of thermal expansion

)]8.01([ 6060 ttEXPVCF

60

1260

060

KK

APIt

5.131

012.999*5.141

APIt

5.131

012.999*5.141

60

1260

060

KK

)]8.01([ 6060 ttEXPVCF

)]8.01([ 606060 ttEXPt

)]8.01([ 606060 ttEXPt

)]8.01([ 6060 ttEXPVCF

60

1260

060

KK

6060 5.131

012.999*5.141

API

)]8.01([ 6060 ttEXPVCF

60

1260

060

KK

6060 5.131

012.999*5.141

API

)]8.01([ 6060 ttEXPVCF

260

601060

KK

260

60 B

A

530…93023A VOLUME IV GENERALIZED CRUDE OILS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60 / 60°F

23ARANGE

REL.DENSITY0,8255…1,076

0,78…0,8250,611…0,7795

WHERE ∆t = t - 60 (˚F) PAGE X-151

23B VOLUME V

23BRANGE


0,78…0,8250,6535…0,7795

WHERE ∆t = t - 60 (˚F) PAGE X-184

24A VOLUME IV GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60°F AGAINST RELATIVE DENSITY 60 / 60°F

24AWHERE ∆t = t - 60 (˚F) RANGE


0,78…0,825

WHERE PAGE X-223 0,611…0,7795

24B VOLUME V

24BWHERE ∆t = t - 60 (˚F) RANGE

REL.DENSITYOR 0,8255…1,076

0,78…0,825

WHERE 0,6535…0,7795

PAGE X-243

24C VOLUME VI

24C RANGE

WHERE ∆t = t - 60 (˚F)

PAGE X-266 270…510510…530530…930

53A VOLUME VII GENERALIZED CRUDE OILS CORRECTION OF OBSERVED DENSITY TO DENSITY AT 15°C

53ARANGE

DENSITY ρt at temperature t:

ρt=relative density*999,012 999,012 = density of water at 60˚F, Kg/m3

GENERALIZED PRODUCTS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60/60°F

DENSITY ρt at temperature t:

ρt=relative density*999,012 999,012 = density of water at 60˚F, Kg/m3

ρ60=relative density60/60˚F*999,012

GENERALIZED PRODUCTS CORRECTION OF VOLUME TO 60°F AGAINST RELATIVE DENSITY 60/60°F

ρ60=relative density60/60˚F*999,012



α * 106

α60 = coefficient of thermal expansion

60

1260

060

KK

)]8.01([ 6060 ttEXPVCF )]8.01([ 606060 ttEXPt

60

1260

060

KK

)]8.01([ 6060 ttEXPVCF )]8.01([ 606060 ttEXPt

)]8.01([ 6060 ttEXPVCF

60

1260

060

KK

)]8.01([ 6060 ttEXPVCF

60

1260

060

KK

)]8.01([ 6060 ttEXPVCF

15

1215

015

KK

260

601060

KK

260

60 B

A

DENSITY610,5…778,5

779…824824,5…1075

where∆t = t - 15 (˚C) PAGE X-283

53B VOLUME VIII GENERALIZED PRODUCTS CORRECTION OF OBSERVED DENSITY TO DENSITY AT 15°C

53BRANGE

DENSITY653…778,5779…824

824,5…1075

where∆t = t - 15 (˚C) PAGE X-311

54A VOLUME VII GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 15°C AGAINST DENSITY AT 15°C

54A RANGEwhere ∆t = t - 15 (˚C) DENSITY

610,5…778,5779…824

PAGE X-351 824,5…1075

54B VOLUME VIII GENERALIZED PRODUCTS CORRECTION OF VOLUME TO 15°C AGAINST DENSITY AT 15°C

54B RANGEwhere ∆t = t - 15 (˚C) DENSITY

653…778778,5…824

PAGE X-371 824,5…1075

54C VOLUME IX VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 15°C AGAINST THERMAL EXPANSION COEFFICIENTS AT 15°C

54C RANGE

where ∆t = t - 15 (˚C)486…918918…954

PAGE X-393 954…1674

54D

ρ15 = density at the base temperature

ρ15 = density at the base temperature

α * 106

15

1215

015

KK

15

1215

015

KK

)]8.01([ 1515 ttEXPVCF )]8.01([ 151515 ttEXPt

15

1215

015

KK

)]8.01([ 1515 ttEXPVCF )]8.01([ 151515 ttEXPt

)]8.01([ 1515 ttEXPVCF

15

1215

015

KK

)]8.01([ 1515 ttEXPVCF

15

1215

015

KK

)]8.01([ 1515 ttEXPVCF

15

1215

015

KK

215

151015

KK 2

1515

BA

)]8.01([ 1515 ttEXPVCF

215

151015

KK 2

1515

BA

GENERALIZED CRUDE OILS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60°F

RANGE

˚F0…3000…2500…200

RANGE˚F

0…3000…2500…200

GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60°F AGAINST API GRAVITY AT 60°F

RANGE˚F

0…3000…2500…200

RANGE˚F

0…3000…2500…200

RANGE

˚F

0…3000…250

GENERALIZED PRODUCTS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60°F

GENERALIZED PRODUCTS CORRECTION OFVOLUME TO 60°F AGAINST API GRAVITY AT 60°F


0…200GENERALIZED CRUDE OILS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60 / 60°F

RANGEREL.DENSITY ˚F0,8255…1,076 0…300

0,78…0,825 0…2500,611…0,7795 0…200


0,78…0,825 0…2500,6535…0,7795 0…200

GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60°F AGAINST RELATIVE DENSITY 60 / 60°F


0,78…0,825 0…250

0,611…0,7795 0…200


0,78…0,825 0…250

0,6535…0,7795 0…200

RANGE

˚F

0…3000…2500…200

GENERALIZED CRUDE OILS CORRECTION OF OBSERVED DENSITY TO DENSITY AT 15°C

RANGE

GENERALIZED PRODUCTS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60/60°F

F AGAINST RELATIVE DENSITY 60/60°F


DENSITY ˚C610,5…778,5 -18…95

779…824 -18…125824,5…1075 -18…150

GENERALIZED PRODUCTS CORRECTION OF OBSERVED DENSITY TO DENSITY AT 15°C

RANGEDENSITY ˚C

653…778,5 -18…90779…824 -18…125

824,5…1075 -18…150

GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 15°C AGAINST DENSITY AT 15°C

RANGEDENSITY ˚C

610,5…778,5 -18…95779…824 -18…125

824,5…1075 -18…150

GENERALIZED PRODUCTS CORRECTION OF VOLUME TO 15°C AGAINST DENSITY AT 15°C

RANGEDENSITY ˚C653…778 -18…95

778,5…824 -18…125824,5…1075 -18…150

VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 15°C AGAINST THERMAL EXPANSION COEFFICIENTS AT 15°C

RANGE

˚C-18…150-18…125-18…95

CONSTANTS

1. CRUDE OILS

TABLE RANGE:

5A,6A 341.0957 0 0…100˚ API

23A,24A 341.0957 0 0,6110…1,0760 RELATIVE DENSITY

53A, 54A 613.9723 0

2.PRODUCTS

TABLE RANGE:

5B,6B

103.872 0.2701 0…37˚ API

330.301 0 37,1…47,9 API48…52 API

192.4571 0.2438 52,1…85 API

23B, 24B

103.872 0.2701 0,839…1,076 RELATIVE DENSITY

330.301 0 0,789…0,8395 RELATIVE DENSITY0,771…0,7885 RELATIVE DENSITY

192.4571 0.2438 0,6535…0,7705 RELATIVE DENSITY

53B, 54B

186.9696 0.4862

594.5418 0

346.4228 0.4388

54D 0 0.6278 AllASTM Tables ver 1,1 © HENRY

K0 K1

610,5…1075,0 KG/M3

K0 K1

839…1075 DENSITY, KG/M3

788…838,5 DENSITY, KG/M3

770,5…787,5 DENSITY, KG/M3

653…770 DENSITY, KG/M3

REMARKS

REMARKS

FUEL OIL

JET GROUPA=-0,0018684; B=1489,067

GASOLINES

FUEL OIL

JET GROUPA=-0,0018684; B=1489,067

GASOLINES

FUEL OIL

JET GROUP

A=-0,00336312; B=2680,3206

GASOLINES

Lub.Oils

(KG/M3)2/˚F

(KG/M3)2/˚F

(KG/M3)2/˚C

(KG/M3)2/˚F

(KG/M3)2/˚F

(KG/M3)2/˚F

(KG/M3)2/˚F

(KG/M3)2/˚F

(KG/M3)2/˚F

(KG/M3)2/˚C

(KG/M3)2/˚C

(KG/M3)2/˚C

(KG/M3)2/˚C

Examples

5A CRUDE OILS 5B OIL PRODUCTSAPI GRAVITY AT OBSERVED TEMPERATURE API GRAVITY AT OBSERVED TEMPERATURE

35 35.5 36 36.5 37 37.5 5 5.5 4.6 6.5 7 7.5TEMP ˚F CORRESPONDING API GRAVITY AT 60˚F TEMP ˚F CORRESPONDING API GRAVITY AT 60˚F

195 25.7 26.1 26.5 26.9 27.3 27.8 90 3.6 4.1 4.6 5.1 5.6 6195.5 25.6 26.1 26.5 26.9 27.3 27.7 90.5 3.6 4.1 4.6 5 5.5 6196 25.6 26 26.4 26.9 27.3 27.7 91 3.6 4 4.5 5 5.5 6

196.5 25.6 26 26.4 26.8 27.2 27.7 91.5 3.5 4 4.5 5 5.5 6197 25.5 26 26.4 26.8 27.2 27.6 92 3.5 4 4.5 5 5.5 5.9

197.5 25.5 25.9 26.3 26.8 27.2 27.6 92.5 3.5 4 4.5 4.9 5.4 5.9

6A CRUDE OILS 6B OIL PRODUCTSAPI GRAVITY AT 60˚F API GRAVITY AT 60˚F

50 50.5 51 51.5 52 52.5 35 35.5 36 36.5 37 37.5TEMP ˚F FACTOR FOR CORRECTING VOLUME TO 60˚F TEMP ˚F FACTOR FOR CORRECTING VOLUME TO 60˚F

75 0.9915 0.9915 0.9915 0.9914 0.9914 0.9913 105 0.9791 0.979 0.9789 0.9788 0.9787 0.978675.5 0.9913 0.9912 0.9912 0.9911 0.9911 0.991 105.5 0.988 0.9788 0.9787 0.9786 0.9785 0.978476 0.991 0.9909 0.9909 0.9908 0.9908 0.9907 106 0.9786 0.9785 0.9784 0.9784 0.9783 0.9781

76.5 0.9907 0.9906 0.9906 0.9905 0.9905 0.9904 106.5 0.9784 0.9783 0.9782 0.9781 0.978 0.977977 0.9904 0.9904 0.9903 0.9903 0.9902 0.9901 107 0.9781 0.9781 0.978 0.9779 0.9778 0.9777

77.5 0.9901 0.9901 0.99 0.99 0.9899 0.9899 107.5 0.9779 0.9788 0.9777 0.9776 0.9776 0.9774

23A CRUDE OILS 23B OIL PRODUCTSRELATIVE DENSITY AT OBSERVED TEMPERATURE RELATIVE DENSITY AT OBSERVED TEMPERATURE

0.827 0.829 0.831 0.833 0.835 0.837 0.941 0.943 0.945 0.947 0.949 0.951TEMP ˚F CORRESPONDING RELATIVE DENSITY 60/60˚F TEMP ˚F CORRESPONDING RELATIVE DENSITY 60/60˚F

90 0.8389 0.8409 0.8429 0.8449 0.8468 0.8488 195 0.9906 0.9926 0.9946 0.9965 0.9985 1.000590.5 0.8391 0.8411 0.8431 0.8451 0.847 0.849 195.5 0.9908 0.9928 0.9948 0.9967 0.9987 1.000791 0.8393 0.8413 0.8433 0.8453 0.8472 0.8492 196 0.991 0.993 0.995 0.9969 0.9989 1.0008

91.5 0.8395 0.8415 0.8435 0.8455 0.8474 0.8494 196.5 0.9912 0.9932 0.9951 0.9971 0.9991 1.00192 0.8397 0.8417 0.8437 0.8456 0.8476 0.8496 197 0.9914 0.9933 0.9953 0.9973 0.9992 1.0012

92.5 0.8399 0.8419 0.8439 0.8458 0.8478 0.8498 197.5 0.9916 0.0035 0.9955 0.9975 0.9994 1.0014

24A CRUDE OILS 24B OIL PRODUCTSRELATIVE DENSITY 60/60˚F RELATIVE DENSITY 60/60˚F

0.612 0.614 0.616 0.618 0.62 0.622 0.89 0.892 0.894 0.896 0.898 0.9TEMP ˚F CORRESPONDING RELATIVE DENSITY 60/60˚F TEMP ˚F FACTOR FOR CORRECTING VOLUME TO 60˚F

75 0.9863 0.9863 0.9864 0.9865 0.9866 0.9867 135 0.9671 0.9672 0.9673 0.9674 0.9675 0.967575.5 0.9858 0.9859 0.986 0.9861 0.9862 0.9863 135.5 0.9668 0.9669 0.967 0.9671 0.9672 0.967376 0.9853 0.9854 0.9855 0.9856 0.9857 0.9858 136 0.9666 0.9667 0.9668 0.9669 0.967 0.9671

76.5 0.9849 0.985 0.9851 0.9852 0.9853 0.9854 136.5 0.9664 0.9665 0.9666 0.9667 0.9668 0.966977 0.9844 0.9845 0.9846 0.9847 0.9848 0.9849 137 0.9662 0.9663 0.9664 0.9665 0.9666 0.9667

77.5 0.984 0.9841 0.9842 0.9843 0.9844 0.9845 137.5 0.966 0.9661 0.9662 0.9663 0.9664 0.9665

53A CRUDE OILS 53B OIL PRODUCTSDENSITY AT OBSERVED TEMPERATURE DENSITY AT OBSERVED TEMPERATURE950.0 952.0 954.0 956.0 958.0 960.0 997 999.0 1001.0 1003.0 1005.0 1007.0

TEMP ˚C CORRESPONDING DENSITY AT 15˚C TEMP ˚C CORRESPONDING DENSITY AT 15˚C-18 929.1 931.1 933.1 935.2 937.3 939.3 -0.5 986.9 988.9 990.9 992.9 994.9 996.9

-17.75 929.2 931.3 933.3 935.4 937.4 939.5 -0.25 987.1 989.1 991.1 993.1 995.1 997.1-17.5 929.4 931.4 933.5 935.5 937.6 939.6 0 987.2 989.2 991.2 993.3 995.3 997.3

-17.25 929.5 931.6 933.6 935.7 937.7 939.8 0.25 987.4 989.4 991.4 993.4 995.4 997.4-17 929.7 931.7 933.8 935.8 937.9 939.9 0.5 987.6 989.6 991.6 993.6 995.6 997.6

-16.75 929.9 931.9 934 936 938 940.1 0.75 987.7 989.7 991.7 993.7 995.8 997.8

54A CRUDE OILS 54B OIL PRODUCTSDENSITY AT 15 ˚C DENSITY AT 15 ˚C

990 992.0 994.0 996.0 998.0 1000.0 730 732.0 734.0 736.0 738.0 740.0TEMP ˚C FACTOR FOR CORRECTING VOLUME TO 15 ˚C TEMP ˚C CORRESPONDING DENSITY AT 15˚C

14 1.0006 1.0006 1.0006 1.0006 1.0006 1.0006 40 0.9684 0.9686 0.9687 0.9688 0.969 0.969114.25 1.0005 1.0005 1.0005 1.0005 1.0005 1.0005 40.25 0.9681 0.9683 0.9684 0.9685 0.9687 0.968814.5 1.0003 1.0003 1.0003 1.0003 1.0003 1.0003 40.5 0.9678 0.9679 0.9681 0.9682 0.9683 0.9685

14.75 1.0002 1.0002 1.0002 1.0002 1.0002 1.0002 40.75 0.9675 0.9676 0.9678 0.9679 0.968 0.968215 1 1 1 1 1 1 41 0.9672 0.9673 0.9674 0.9676 0.9677 0.9679

15.25 0.9998 0.9998 0.9998 0.9998 0.9998 0.9998 41.25 0.9669 0.967 0.9671 0.9673 0.9674 0.9675

54D OIL PRODUCTSDENSITY AT 15 ˚C

730 732.0 734.0 736.0 738.0 740.0TEMP ˚C CORRESPONDING DENSITY AT 15˚C

40 0.9684 0.9686 0.9687 0.9688 0.969 0.969140.25 0.9681 0.9683 0.9684 0.9685 0.9687 0.968840.5 0.9678 0.9679 0.9681 0.9682 0.9683 0.9685

40.75 0.9675 0.9676 0.9678 0.9679 0.968 0.968241 0.9672 0.9673 0.9674 0.9676 0.9677 0.9679

41.25 0.9669 0.967 0.9671 0.9673 0.9674 0.9675

6C OIL PRODUCTSCOEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F)

530 532 534 536 538 540TEMP ˚F FACTOR FOR CORRECTING VOLUME TO 60˚F

75 0.992 0.992 0.992 0.9919 0.9919 0.991975.5 0.9918 0.9917 0.9917 0.9917 0.9916 0.991676 0.9915 0.9915 0.9914 0.9914 0.9914 0.9913

76.5 0.9912 0.9912 0.9912 0.9911 0.9911 0.991177 0.991 0.9909 0.9909 0.9909 0.9908 0.9908

77.5 0.9907 0.9907 0.9906 0.9906 0.9906 0.9905


490 492 494 496 498 500TEMP ˚F FACTOR FOR CORRECTING VOLUME TO 60˚F

105 0.9778 0.9777 0.9776 0.9775 0.9774 0.9774105.5 0.9776 0.9775 0.9774 0.9773 0.9772 0.9771106 0.9773 0.9772 0.9771 0.977 0.9769 0.9768

106.5 0.9771 0.977 0.9769 0.9768 0.9767 0.9766107 0.9768 0.9767 0.9766 0.9765 0.9764 0.9763

107.5 0.9766 0.9765 0.9764 0.9763 0.9762 0.9761


800 804 808 812 816 820TEMP ˚C FACTOR FOR CORRECTING VOLUME TO 15˚C

62.5 0.9616 0.9614 0.9612 0.961 0.9608 0.960662.75 0.9614 0.9612 0.961 0.9608 0.9606 0.9604

63 0.9612 0.961 0.9608 0.9606 0.9604 0.960263.25 0.961 0.9608 0.9606 0.9604 0.9602 0.9663.5 0.9608 0.9606 0.9604 0.9602 0.96 0.9598

63.75 0.9606 0.9604 0.9602 0.96 0.9598 0.9596

VCF

VCF calculationDensity @ 15/vac= 0.8668 Density @ Corresponding Mass 5983.445

Actual temp= 39.50 actual temp dcc (approximate) VolumeVCF Table 54A= 0.9799 0.8494 0.00071 7044.51

Table 54B= 0.9800 0.8495 0.00071 7043.79Table 54D= 0.9822 0.8514 0.00063 7028.01

User infoDensity @ 15/vac= 866.8 General formula:

Actual temp= 39.5 VCF=exp(b) and : a=(K0+K1xDensity @ 15/vac)/(Density @ 15/vac^2)diff temp= 24.5 b=-a x diff temp x (1+0,8 x a x diff temp)

diff temp=actual temp-15Formula for Table 54B and 770 <= Dens @ 15/vac < 778:VCF=exp(d) and : c=-0,0033612+2680,32/(Density @ 15/vac^2)

d=-c x diff temp x (1+ 0,8 x c x diff temp)

Table 54AK0= 613.97226 a= 0.000817 VCF= 0.9799K1= 0.00000 b= -0.02034

Table 54DK0= 0.00000 a= 0.000724 VCF= 0.9822K1= 0.62780 b= -0.018

Table 54BDens @ 15/vac < 770K0= 346.42278 a= 0.000967 VCF= 0.9761K1= 0.43884 b= -0.02415

770 <= Dens @ 15/vac < 778c= 0.000206 VCF= 0.9949d= -0.00507

778 <= Dens @ 15/vac < 839K0= 594.54180 a= 0.000791 VCF= 0.9805K1= 0.00000 b= -0.01969

0.00079131Dens @ 15/vac >= 839

K0= 186.96960 a= 0.00081 VCF= 0.9800K1= 0.48618 b= -0.02015

VCF

a=(K0+K1xDensity @ 15/vac)/(Density @ 15/vac^2)b=-a x diff temp x (1+0,8 x a x diff temp)

Formula for Table 54B and 770 <= Dens @ 15/vac < 778:c=-0,0033612+2680,32/(Density @ 15/vac^2)d=-c x diff temp x (1+ 0,8 x c x diff temp)

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