ASTM Tables

ASTM 5A CRUDE OILSAPI GRAVITY 8.5 AT 210 ˚FAPI GRAVITY 2.28 AT 60 ˚F

ASTM 5B OIL PRODUCTSAPI GRAVITY 10.5 AT 135 ˚F http://www.bgicrew.com/API GRAVITY 6.74 AT 60 ˚F САНКТ-ПЕТЕРБУРГ

ASTM 6A CRUDE OILS Тел.: +7 812 346 80 08API GRAVITY 93.5 AT 60 ˚F Факс: +7 812 346 73 32

VCF TO 60˚F 0.97213 AT 92 ˚F

ASTM 6B OIL PRODUCTS ЗДЕСЬ МОГЛА БЫТЬ ВАША РЕКЛАМАAPI GRAVITY 63 AT 60 ˚F PLACE FOR YOUR ADVERTISEMENT

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 60 ˚FREL. DENSITY 0.65000 AT 60 ˚F

ASTM 23B OIL PRODUCTSREL. DENSITY 1.0430 AT 0 ˚FREL. DENSITY 1.02160 AT 60 ˚F

FUEL OILASTM 24A CRUDE OILS Volume: 500REL. DENSITY 1.076 AT 60 ˚F à 475.3269VCF TO 60˚F 0.95065 AT 225 ˚F 0.511452 M.T.

-0.011408 M.T.

ASTM 24B OIL PRODUCTS Volume: 500REL. DENSITY 0.67 AT 60 ˚F à 444.8734VCF TO 60˚F 0.88975 AT 195.5 ˚F 0.298065 M.T.

GASOLINE -0.191296 M.T.

ASTM 24C OIL PRODUCTS Volume: 500TEC 650 AT 60 ˚F à 509.6906

VCF 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

FUEL OIL

E-mail : [email protected]

M3

Volume at 15oC: M3

Weight in Vac.at 15oC:Weight in Air at 15oC:

M3

Volume at 15oC: M3

Weight in Vac.at 15oC:Weight in Air at 15oC:

M3

Volume at 15oC: M3

ASTM 54A CRUDE OILS Volume: 500DENSITY 1050 AT 15 ˚C à 488.7912

VCF TO 15˚C 0.97758 AT 55 ˚C 513.2308 M.T.512.6931 M.T.

ASTM 54B OIL PRODUCTS Volume: 500DENSITY 1062 AT 15 ˚C à 508.5287

VCF TO 15˚C 1.01706 AT -12.5 ˚C 540.0575 M.T.FUEL OIL 539.4981 M.T.

ASTM 54C OIL PRODUCTS Volume: 500TEC 1644 AT 15 ˚C à 526.6338

VCF TO 15˚C 1.0533 AT -18 ˚C

ASTM 54D LUBE OILS Volume: 500Density in vac.: 875 AT 15 ˚C à 496.405

VCF TO 15˚C 0.9928 AT 25 ˚C 434.3544 M.T.433.8083 M.T.

ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail: [email protected]

M3

Volume at 15oC: M3

Weight in Vac.at 15oC:Weight in Air at 15oC:

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

Weight in Vac.at 15oC:Weight in Air at 15oC:

http://oleg352.mail333.su/

ЗДЕСЬ МОГЛА БЫТЬ ВАША РЕКЛАМАPLACE FOR YOUR ADVERTISEMENT

E-mail : [email protected]

ASTM SG TO API ASTMSG 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 15Real temp: 15.4VCF: 0.9996

ASTM 54B OIL PRODUCTS Volume:Density in vac.: 0.8546 at temp 15Real temp: 33VCF: 0.9851

ASTM 54C Volume:Temp.Exp.Coef. 640 at temp 15

Real temp: 115VCF: 0.9349

ASTM 54D LUBE OILS Volume:Density in vac.: 0.875 at temp 15Real temp: 25VCF: 0.9928

Расчет поправок к плотности груза по таблицам ASTM c точностью бумажных таблиц1 ASTM 54D СМАЗОЧНЫЕ МАСЛА

ASTM 54D LUBE OILSDensity in vac.: 0.873 at temp 15 TEMP1 24.5Real temp: 24.6 24.6VCF: 0.9931 TEMP2 24.75

ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail: [email protected]

Dens 600F

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

Weight in Air at 15oC:

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

Weight in Air at 15oC:

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

Weight in Air at 15oC:

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

Weight in Air at 15oC:

0C0C

http://oleg352.mail333.su/

API TO SGAPI - American Petroleum Institute

945.636455 VCF - Volume Correction Factor

500499.79

427.120534426.570765

http://www.bgicrew.com/500 САНКТ-ПЕТЕРБУРГ

492.543645 Владимирский пр., д. 23, лит. А,

420.927799 “Регент холл”, 5-й этаж,

420.386001 г. Санкт-Петербург 191002 Россия

500 Тел.: +7 812 346 80 08

467.468188 Факс: +7 812 346 73 32

??

500 ЗДЕСЬ МОГЛА БЫТЬ ВАША РЕКЛАМА496.405

434.354375433.808329

Density at 15 ˚CDen1 Den2

0.872 0.873 0.8740.9931 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

E-mail : [email protected]

Скорость налива в танк для электростатических жидкостейДиам.трубы= 300 мм

1 м/с 7 м/сСкорость налива в пределах: 254.5 1781.3

Максимальная скорость налива в танк по времени реагирования 1 мин.20001960

Скорость налива: 2400

Определение максимальной высоты подъема жидкости насосомДавление насоса 800000Плотность жидк. 1000 вода: 1000макс.высота 81.632653 м

V100%= m3

V98%= m3

м3/час

9,8 m/s2

кг/м3

Определение поправки к объему груза за нагрев1. Для смазочных масел - таблица 54 D

Volume before 1000 ###Dens. In Vac 0.875 at 15Temp. before 25 1 tempTemp. after: 50 ###Difference: 18.57 ###Volume after 1018.57 2 temp

ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail: [email protected]

m3

oCoCoC

m3

m3

http://oleg352.mail333.su/ Weight in Air at 15oC:

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

5A341.0957 PAGE X-800.0 PAGE X-80

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

API = observed API gravity

PAGE X-65B VOLUME II

5B CONVERT API GRAVITY TO DENSITY:

API = observed API gravity

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)

PAGE X-916B VOLUME II

6BWHERE ∆t = t - 60 (˚F)

PAGE X-1126C VOLUME III

6CWHERE ∆t = t - 60 (˚F)

PAGE X-135

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

ρt = density at temperature t

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

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

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

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

VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 60

α60 = coefficient of thermal expansion

VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]

α 60=K0ρ602 +

K1ρ60

ρt=141 .5∗999.012131 .5+API

ρt=141 .5∗999.012131 .5+API

α 60=K0ρ602 +

K1ρ60

VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]

ρt= ρ60EXP [−α 60 Δt (1+0. 8α 60 Δt ) ]

ρt= ρ60EXP [−α 60 Δt (1+0. 8α 60 Δt ) ]

VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]

α 60=K0ρ602 +

K1ρ60

ρ60=141.5∗999 .012131.5+API 60

VCF=EXP [−α60 Δt (1+0 . 8α60 Δt )]

α 60=K0ρ602 +

K1ρ60

ρ60=141.5∗999 .012131.5+API 60

VCF=EXP [−α60 Δt (1+0 . 8α60 Δt )]

α 60=K0+K1 ρ60

ρ602 α 60=A+

Bρ602

23A VOLUME IV GENERALIZED CRUDE OILS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60 / 60°F

23A

WHERE ∆t = t - 60 (˚F) PAGE X-151

23B VOLUME V

23B

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)

WHERE PAGE X-223

24B VOLUME V

24BWHERE ∆t = t - 60 (˚F)

OR

WHEREPAGE X-243

24C VOLUME VI

24CWHERE ∆t = t - 60 (˚F)

PAGE X-266

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

53A

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

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*999,012999,012 = density of water at 60˚F, Kg/m3

VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 60

α60 = coefficient of thermal expansion

α 60=K0ρ602 +

K1ρ60

VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]ρt= ρ60EXP [−α 60 Δt (1+0.8α60 Δt ) ]

α 60=K0ρ602 +

K1ρ60

VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]ρt= ρ60EXP [−α 60 Δt (1+0.8α 60 Δt ) ]

VCF=EXP [−α60 Δt (1+0 . 8α60 Δt )]

α 60=K0ρ602 +

K1ρ60

VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]

α 60=K0ρ602 +

K1ρ60

VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]

α 15=K0ρ152 +

K1ρ15

α 60=K0+K1 ρ60

ρ602

α 60=A+Bρ602

where∆t = t - 15 (˚C) PAGE X-283

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

53B

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

54Awhere ∆t = t - 15 (˚C)

PAGE X-351

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

54Bwhere ∆t = t - 15 (˚C)

PAGE X-371

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

54Cwhere ∆t = t - 15 (˚C)

PAGE X-393

54D

ρ15 = density at the base temperature

ρ15 = density at the base temperature

α 15=K0ρ152 +

K1ρ15

VCF=EXP [−α15 Δt (1+0 .8α15 Δt )]ρt= ρ15EXP [−α 15Δt (1+0 .8α 15 Δt ) ]

α 15=K0ρ152 +

K1ρ15

VCF=EXP [−α15 Δt (1+0 .8α15 Δt )]ρt= ρ15EXP [−α 15Δt (1+0 .8α 15 Δt ) ]

VCF=EXP [−α15 Δt (1+0 .8α15 Δt )]

α 15=K0ρ152 +

K1ρ15

VCF=EXP [−α15 Δt (1+0 .8α15 Δt )]

α 15=K0ρ152 +

K1ρ15

VCF=EXP [−α15 Δt (1+0 .8α15 Δt )]

α 15=K0ρ152 +

K1ρ15

α 15=K0+K 1 ρ15

ρ152

α 15=A+Bρ152

VCF=EXP [−α15 Δt (1+0 .8α15 Δt )]

15

1215

015

KK α 15=

K0+K 1 ρ15ρ152

α 15=A+Bρ152

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

RANGE˚API ˚F

0…40 0…30040…50 0…25050…100 0…200

RANGE˚API ˚F

0…40 0…30040…50 0…25050…85 0…200

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

RANGE˚API ˚F

0…40 0…30040…50 0…25050…100 0…200

RANGE˚API ˚F

0…40 0…30040…50 0…25050…85 0…200

RANGE˚F

270…510 0…300510…530 0…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

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

α * 106

α 60=A+Bρ602

530…930 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

RANGEREL.DENSITY ˚F0,8255…1,076 0…300

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

RANGEREL.DENSITY ˚F0,8255…1,076 0…300

0,78…0,825 0…250

0,611…0,7795 0…200

RANGEREL.DENSITY ˚F0,8255…1,076 0…300

0,78…0,825 0…250

0,6535…0,7795 0…200

RANGE˚F

270…510 0…300510…530 0…250530…930 0…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

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

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

α * 106

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

486…918 -18…150918…954 -18…125954…1674-18…95

α * 106

F AGAINST THERMAL EXPANSION COEFFICIENTS AT 60°F

F AGAINST THERMAL EXPANSION COEFFICIENTS AT 60°F

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

CONSTANTS

1. CRUDE OILS

TABLE RANGE:

5A,6A 341.0957 0 0…100˚ API23A,24A 341.0957 0 0,6110…1,0760 RELATIVE DENSITY53A, 54A 613.9723 0

2.PRODUCTS

TABLE RANGE:

5B,6B

103.872 0.2701 0…37˚ API330.301 0 37,1…47,9 API

48…52 API192.4571 0.2438 52,1…85 API

23B, 24B

103.872 0.2701 0,839…1,076 RELATIVE DENSITY330.301 0 0,789…0,8395 RELATIVE DENSITY

0,771…0,7885 RELATIVE DENSITY192.4571 0.2438 0,6535…0,7705 RELATIVE DENSITY

53B, 54B

186.9696 0.4862594.5418 0

346.4228 0.438854D 0 0.6278 All

ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail: [email protected]://oleg352.mail333.su/

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 OILJET GROUPA=-0,0018684; B=1489,067GASOLINESFUEL OILJET GROUPA=-0,0018684; B=1489,067GASOLINESFUEL OILJET GROUPA=-0,00336312; B=2680,3206GASOLINESLub.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

24C OIL PRODUCTSCOEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F)

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

54C OIL PRODUCTSCOEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F)

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

Page 24

VCF calculationDensity @ 15/vac= 0.8668 Density @ Corresponding Mass 5983.45

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= 0.00082 VCF= 0.9799K1= 0.00000 b= -0.02034

Table 54DK0= 0.00000 a= 0.00072 VCF= 0.9822K1= 0.62780 b= -0.018

Table 54 Dens @ 15/vac < 770K0= 346.42278 a= 0.00097 VCF= 0.9761K1= 0.43884 b= -0.02415

770 <= Dens @ 15/vac < 778c= 0.00021 VCF= 0.9949d= -0.00507

778 <= Dens @ 15/vac < 839K0= 594.54180 a= 0.00079 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

Page 25

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)