• Author / Uploaded
• Henry Maeda

• Categories
• Química
• Masa
• Física Aplicada e Interdisciplinaria
• Cantidad
• Industria petrolera

Citation preview

AABAAABBAABN ASTM API GRAVITY API GRAVITY ASTM

5A 8.5 -1.00 5B

AT AT

CRUDE OILS 300 ˚C 60 ˚F

OIL PRODUCTS

API GRAVITY

10.5

AT

135

˚F

API GRAVITY

6.74

AT

60

˚F

ASTM API GRAVITY

6A 93.5

AT

CRUDE OILS 60 ˚F

VCF TO 60˚F

0.97213

AT

92

ASTM API GRAVITY VCF TO 60˚F

6B 63 0.9895

OIL PRODUCTS AT 60 ˚F AT 75 ˚F

ASTM TEC VCF TO 60˚F

6C 910 1.0271

OIL PRODUCTS AT 60 ˚F AT 30 ˚F

ASTM REL. DENSITY REL. DENSITY

23A 0.6500 0.65000

AT AT

ASTM REL. DENSITY REL. DENSITY

23B 1.0430 1.02160 FUEL OIL 24A 1.076 0.95065

ASTM REL. DENSITY VCF TO 60˚F

˚F

www.wma.go.tz [email protected] Cell 0713792395

E-mail : [email protected]

CRUDE OILS 15 ˚C 15 ˚C

OIL PRODUCTS AT 0 ˚C AT 60 ˚C CRUDE OILS AT 60 ˚F AT 225 ˚F

Volume:  Volume at 15oC: o

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

ASTM REL. DENSITY VCF TO 60˚F

24B 870 1.00000 FUEL OIL

OIL PRODUCTS AT 15 ˚C AT 27.5 ˚C

ASTM TEC VCF TO 60˚F

24C 650 1.0194

OIL PRODUCTS AT 60 ˚F AT 30 ˚F

ASTM DENSITY DENSITY

53A 779.0 786.65

AT AT

ASTM DENSITY DENSITY

53B 1008.0 1001.19 FUEL OIL

Volume:  Volume at 15oC: o

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

CRUDE OILS 25 ˚C 15 ˚C

OIL PRODUCTS AT 4.5 ˚C AT 15 ˚C

Volume: o  Volume at 15 C:

500 475.3269 0.511452 -0.01141

M3

500 499.9981 434.9983 434.4483

M3

M3 M.T. M.T.

M3 M.T. M.T.

3 500 M 3 509.6906 M

ASTM DENSITY VCF TO 15˚C

54A 1050 1.00722

CRUDE OILS AT 15 ˚C AT 2 ˚C

Volume: o  Volume at 15 C: o

Weight in Vac.at 15 C: o

Weight in Air at 15 C:

ASTM DENSITY VCF TO 15˚C

Volume: o  Volume at 20 C:

500 503.6118 528.7924 528.2384

M3

500 497.1747 432.542 431.9951

M3

3

M M.T. M.T.

54B 870 0.99435 FUEL OIL

OIL PRODUCTS AT 20 ˚C AT 27 ˚C

ASTM TEC VCF TO 15˚C

54C 1644 1.0533

OIL PRODUCTS AT 15 ˚C AT -18 ˚C

Volume: o  Volume at 15 C:

3 500 M 3 526.6338 M

ASTM Density in vac.: VCF TO 15˚C

54D 875 0.9928

LUBE OILS AT 15 ˚C AT 25 ˚C

Volume:  Volume at 15oC:

1000 992.81 868.7088 867.6167

o

Weight in Vac.at 20 C: o

Weight in Air at 20 C:

o

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

ASTM Tables ver 1,1 © HENRY

http://oleg352.mail333.su/

3

M M.T. M.T.

3

M

M3 M.T. M.T.

[email protected]

ASTM SG

SG TO API 0 Dens 60 F API (60/60F) 0.9465 17.99815108 945.564858

ASTM Density in vac.: Real temp: VCF:

54A 0.8546 15.4 0.9996

ASTM Density in vac.: Real temp: VCF:

54B 0.8546 28.5 0.9888

ASTM Temp.Exp.Coef.

54C 640

Real temp: VCF:

115 0.9349

ASTM Density in vac.: Real temp: VCF:

54D 0.875 43 0.9834

ASTM API (60/60F) SG 18 0.946488 CRUDE OIL 0 C 15

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

OIL PRODUCTS 0 C at temp 15 0 C

Volume: o Volume at 15 C: o Weight in Vac.at 15 C: o Weight in Air at 15 C:

at temp 0 C

at temp

15

0

C

0

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

C

at temp 0 C

Volume: o Volume at 15 C:

LUBE OILS 0 C 20

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

1 ASTM 54D ASTM Density in vac.: Real temp: VCF:

54D 0.873 24.6 0.9931

ASTM Tables ver 1,1 © HENRY

at temp C

LUBE OILS 0 C 15

TEMP1

0

TEMP2

24.5 24.6 24.75

o

SG -Specific gravity = RD - Relative Density (60/60 F) API - American Petroleum Institute VCF - Volume Correction Factor

API TO SG 0 Dens 15 C 945.63645 500 499.79 427.12053 426.57077 500 494.4136 422.52586 421.982 500 467.46819 ? ? 500 491.71 430.24625 429.70537

Density at Den1 0.872 0.9931 0.99306 0.9930

15

˚C Den2 0.873 0.874 0.99315 0.9932 0.99309 0.99312 0.993 0.9930

0

300 мм 1 м/с 254.5

V100%= V98%=

7 м/с 1781.3

3 2000 m 3 1960 m

2400

800000 1000 81.632653

9,8 m/s2 : 1000

Volume before Dens. In Vac Temp. before Temp. after: Difference: Volume after ASTM Tables ver 1,1 © HENRY

1000 0.875 at o 25 C o 50 C

m3 15

18.57 1018.57

m 3 m

3

o

C

5A

VOLUME I

5A

VCF  EXP[ 60 t (1  0.8 60 t )]

 60  WHERE

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

K0

 602



K1

 60

K0=

341.0957

PAGE X-80

K1=

0.0

PAGE X-80

∆t = t - 60 (˚F) CONVERT API GRAVITY TO DENSITY: ρt = density at temperature t 141.5 * 999.012 t  API = observed API gravity 131.5  API 3 999,012 = density of water at 60˚F, Kg/m

 t   60 EXP [  60 t (1  0.8 60 t )]

PAGE X-6 GENERALIZED PRODUCTS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60°

5B

VOLUME II

5B

CONVERT API GRAVITY TO DENSITY: 141.5 * 999.012 ρt = density at temperature t t  API = observed API gravity 131.5  API 999,012 = density of water at 60˚F, Kg/m3

 60 

K0 K1  2  60  60

VCF  EXP[ 60 t (1  0.8 60 t )]

 t   60 EXP [  60 t (1  0.8 60 t )] VOLUME I

PAGE X-36 GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60°F AGAINST API GRAVITY AT 60°F

6A

VCF  EXP[ 60 t (1  0.8 60 t )]

WHERE

∆t = t - 60

(˚F)

6A

K0 K1  2  60  60

 60   60 6B

6B WHERE

141 . 5 * 999 . 012  131 . 5  API 60

VOLUME II

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

PAGE X-91 GENERALIZED PRODUCTS CORRECTION OFVOLUME TO 60°F AGAINST API GRAVITY AT 60°F

VCF  EXP[ 60 t (1  0.8 60 t )]

∆t = t - 60

(˚F)

 60 

K0 K1  2  60  60

 60 

 60 

141 . 5 * 999 . 012 131 . 5  API 60

K 0  K 1  60



2 60



60

 A 

B  602

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

PAGE X-112 VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME COR

6C

VOLUME III

6C

VCF  EXP[ 60 t (1  0.8 60 t )]

WHERE

∆t = t - 60 (˚F) α60 = coefficient of thermal expansion

PAGE X-135

23A

23A

VOLUME IV GENERALIZED CRUDE OILS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE D DENSITY ρt at temperature t: 3

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

ρt=relative density*999,012

K0 K1  2  60  60

 60 

VCF  EXP[ 60 t (1  0.8 60 t )] WHERE 23B

23B

 t   60 EXP [  60 t (1  0.8 60 t )] ∆t = t - 60

(˚F)

PAGE X-151

GENERALIZED PRODUCTS CORRECTION OF OBSERVED RELATIVE DENSITY TO RELATIVE DE VOLUME V DENSITY ρt at temperature t: 3

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

ρt=relative density*999,012

 60 

K0 K1  2  60  60

VCF  EXP[ 60 t (1  0.8 60 t )]  t   60 EXP [  60 t (1  0.8 60 t )] WHERE

∆t = t - 60

(˚F)

24A

VOLUME IV

GENERALIZED CRUDE OILS CORRECTION OF VOLUME TO 60°F AGAINST RELATIVE DENSITY 6

24A

VCF  EXP[ 60 t (1  0.8 60 t )]

WHERE

∆t = t - 60

 60

PAGE X-184

(˚F)

K K1  20   60  60

WHERE

ρ60=relative density60/60˚F*999,012

24B

VOLUME V

24B

VCF  EXP[ 60 t (1  0.8 60 t )]

WHERE

∆t = t - 60

 60  WHERE

PAGE X-223

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

K0 K1   602  60

K 0  K 1  60  602 B  A  2

 60 

(˚F) OR

ρ60=relative density60/60˚F*999,012



60 3

999,012 = density of water at 60˚F, Kg/m VOLUME VI

24C

VCF  EXP[ 60 t (1  0.8 60 t )]

WHERE

∆t = t - 60 (˚F) α60 = coefficient of thermal expansion

53A

VOLUME VII

 15 

PAGE X-243

VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME COR

24C

53A

 60

PAGE X-266

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

K0 K1  2  15  15

VCF  EXP [  15  t (1  0 .8 15  t )]  t  15 EXP [  15  t (1  0 .8 15  t )]

 t  15 EXP [  15  t (1  0 .8 15  t )] where

53B

53B

ρ15 = density at the base temperature ∆t = t - 15 (˚C) VOLUME VIII

 15 

PAGE X-283

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

K0 K1  2  15  15

VCF  EXP [  15  t (1  0 .8 15  t )]  t  15 EXP [  15  t (1  0 .8 15  t )] where

ρ15 = density at the base temperature ∆t = t - 15 (˚C)

PAGE X-311

54A

VOLUME VII

54A

VCF  EXP [  15  t (1  0 .8 15  t )]

where

54B

54B where

∆t = t - 15

(˚C)

 15 

K0 K1  2  15  15

VOLUME VIII

PAGE X-351

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

VCF  EXP [  15  t (1  0 .8 15  t )] ∆t = t - 15

 15  54C

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

(˚C)

K0 K1   152  15

 15 

K 0  K 1  15 

 152

15

 A 

B  152

PAGE X-371

VOLUME IX

VOLUME CORRECTION FACTORS FOR INDIVIDUAL AND SPECIAL APPLICATIONS VOLUME COR

54C

VCF  EXP [  15  t (1  0 .8 15  t )]

where

∆t = t - 15

(˚C)

 15 54D

K0 K1    152  15

PAGE X-393

VCF  EXP [  15  t (1  0 .8 15  t )]

 15 

K0 K1   152  15

 15 

K 0  K 1  15 

 152

15

 A 

B

 152

BSERVED API GRAVITY TO API GRAVITY AT 60°F RANGE ˚API 0…40 40…50 50…100

˚F 0…300 0…250 0…200

BSERVED API GRAVITY TO API GRAVITY AT 60°F RANGE ˚API ˚F 0…40 0…300 40…50 0…250 50…85 0…200

OLUME TO 60°F AGAINST API GRAVITY AT 60°F RANGE ˚API ˚F 0…40 0…300 40…50 0…250 50…100 0…200

LUME TO 60°F AGAINST API GRAVITY AT 60°F

 A 

B  602

RANGE ˚API ˚F 0…40 0…300 40…50 0…250 50…85 0…200

°

°

UAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 60 F AGAINST THERMAL EXPANSION COEFFICIENTS AT 60 F RANGE 6 α * 10 ˚F 270…510 0…300 510…530 0…250 530…930 0…200

BSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60 / 60°F RANGE REL.DENSITY ˚F 0,8255…1,076 0…300 0,78…0,825 0…250 0,611…0,7795 0…200

°

BSERVED RELATIVE DENSITY TO RELATIVE DENSITY 60/60 F RANGE REL.DENSITY ˚F 0,8255…1,076 0…300 0,78…0,825 0…250 0,6535…0,7795 0…200

OLUME TO 60°F AGAINST RELATIVE DENSITY 60 / 60°F RANGE REL.DENSITY ˚F 0,8255…1,076 0…300 0,78…0,825 0…250 0,611…0,7795 0…200

OLUME TO 60°F AGAINST RELATIVE DENSITY 60/60°F RANGE REL.DENSITY ˚F 0,8255…1,076 0…300 0,78…0,825 0…250 0,6535…0,7795 0…200

°

°

UAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 60 F AGAINST THERMAL EXPANSION COEFFICIENTS AT 60 F

RANGE 6 α * 10 ˚F 270…510 0…300 510…530 0…250 530…930 0…200 BSERVED DENSITY TO DENSITY AT 15°C RANGE DENSITY ˚C 610,5…778,5 -18…95 779…824 -18…125

824,5…1075

-18…150

BSERVED DENSITY TO DENSITY AT 15°C RANGE DENSITY ˚C 653…778,5 -18…90 779…824 -18…125 824,5…1075 -18…150

OLUME TO 15°C AGAINST DENSITY AT 15°C RANGE DENSITY ˚C 610,5…778,5 -18…95 779…824 -18…125 824,5…1075 -18…150

OLUME TO 15°C AGAINST DENSITY AT 15°C RANGE DENSITY ˚C 653…778 -18…95 778,5…824 -18…125 824,5…1075 -18…150

UAL AND SPECIAL APPLICATIONS VOLUME CORRECTION TO 15°C AGAINST THERMAL EXPANSION COEFFICIENTS AT 15°C RANGE α * 106 ˚C 486…918 -18…150 918…954 -18…125 954…1674 -18…95

°

SION COEFFICIENTS AT 60 F

°

SION COEFFICIENTS AT 60 F

SION COEFFICIENTS AT 15°C

CONSTANTS 1. CRUDE OILS TABLE

K0

K1

5A,6A 23A,24A 53A, 54A

341.0957 341.0957 613.9723

0 0 0

RANGE: 0…100˚ API 0,6110…1,0760 RELATIVE DENSITY 3 610,5…1075,0 KG/M

2.PRODUCTS TABLE

5B,6B

23B, 24B

53B, 54B

K0

K1

103.872 330.301

0.2701 0

192.4571 103.872 330.301

0.2438 0.2701 0

192.4571 186.9696 594.5418

0.2438 0.4862 0

346.4228 0.4388 54D 0 0.6278 ASTM Tables ver 1,1 © HENRY

RANGE: 0…37˚ API 37,1…47,9 API 48…52 API 52,1…85 API 0,839…1,076 RELATIVE DENSITY 0,789…0,8395 RELATIVE DENSITY 0,771…0,7885 RELATIVE DENSITY 0,6535…0,7705 RELATIVE DENSITY 839…1075 DENSITY, KG/M3 788…838,5 DENSITY, KG/M3 770,5…787,5 DENSITY, KG/M3 653…770 DENSITY, KG/M3 All

REMARKS (KG/M3)2/˚F (KG/M3)2/˚F 3 2 (KG/M ) /˚C

REMARKS FUEL OIL JET GROUP A=-0,0018684; B=1489,067 GASOLINES FUEL OIL JET GROUP A=-0,0018684; B=1489,067 GASOLINES FUEL OIL JET GROUP A=-0,00336312; B=2680,3206 GASOLINES Lub.Oils

3 2

(KG/M ) /˚F 3 2 (KG/M ) /˚F (KG/M3)2/˚F 3 2

(KG/M ) /˚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 TEMP ˚F 195 195.5 196 196.5 197 197.5

6A TEMP ˚F 75 75.5 76 76.5 77 77.5

23A

CRUDE OILS API GRAVITY AT OBSERVED TEMPERATURE 35 35.5 36 36.5 37 37.5 CORRESPONDING API GRAVITY AT 60˚F 25.7 26.1 26.5 26.9 27.3 27.8 25.6 26.1 26.5 26.9 27.3 27.7 25.6 26 26.4 26.9 27.3 27.7 25.6 26 26.4 26.8 27.2 27.7 25.5 26 26.4 26.8 27.2 27.6 25.5 25.9 26.3 26.8 27.2 27.6 CRUDE OILS API GRAVITY AT 60˚F 50 50.5 51 51.5 52 52.5 FACTOR FOR CORRECTING VOLUME TO 60˚F 0.9915 0.9915 0.9915 0.9914 0.9914 0.9913 0.9913 0.9912 0.9912 0.9911 0.9911 0.991 0.991 0.9909 0.9909 0.9908 0.9908 0.9907 0.9907 0.9906 0.9906 0.9905 0.9905 0.9904 0.9904 0.9904 0.9903 0.9903 0.9902 0.9901 0.9901 0.9901 0.99 0.99 0.9899 0.9899 CRUDE OILS

RELATIVE DENSITY AT OBSERVED TEMPERATURE 0.827 0.829 0.831 0.833 0.835 0.837 TEMP ˚F CORRESPONDING RELATIVE DENSITY 60/60˚F 90 0.8389 0.8409 0.8429 0.8449 0.8468 0.8488 90.5 0.8391 0.8411 0.8431 0.8451 0.847 0.849 91 0.8393 0.8413 0.8433 0.8453 0.8472 0.8492 91.5 0.8395 0.8415 0.8435 0.8455 0.8474 0.8494 92 0.8397 0.8417 0.8437 0.8456 0.8476 0.8496 92.5 0.8399 0.8419 0.8439 0.8458 0.8478 0.8498

5B TEMP ˚F 90 90.5 91 91.5 92 92.5

6B TEMP ˚F 105 105.5 106 106.5 107 107.5

23B

OIL PRODUCTS API GRAVITY AT OBSERVED TEMPERATURE 5 5.5 4.6 6.5 7 7.5 CORRESPONDING API GRAVITY AT 60˚F 3.6 4.1 4.6 5.1 5.6 6 3.6 4.1 4.6 5 5.5 6 3.6 4 4.5 5 5.5 6 3.5 4 4.5 5 5.5 6 3.5 4 4.5 5 5.5 5.9 3.5 4 4.5 4.9 5.4 5.9 OIL PRODUCTS API GRAVITY AT 60˚F 35 35.5 36 36.5 37 37.5 FACTOR FOR CORRECTING VOLUME TO 60˚F 0.9791 0.979 0.9789 0.9788 0.9787 0.9786 0.988 0.9788 0.9787 0.9786 0.9785 0.9784 0.9786 0.9785 0.9784 0.9784 0.9783 0.9781 0.9784 0.9783 0.9782 0.9781 0.978 0.9779 0.9781 0.9781 0.978 0.9779 0.9778 0.9777 0.9779 0.9788 0.9777 0.9776 0.9776 0.9774 OIL PRODUCTS

RELATIVE DENSITY AT OBSERVED TEMPERATURE 0.941 0.943 0.945 0.947 0.949 0.951 TEMP ˚F CORRESPONDING RELATIVE DENSITY 60/60˚F 195 0.9906 0.9926 0.9946 0.9965 0.9985 1.0005 195.5 0.9908 0.9928 0.9948 0.9967 0.9987 1.0007 196 0.991 0.993 0.995 0.9969 0.9989 1.0008 196.5 0.9912 0.9932 0.9951 0.9971 0.9991 1.001 197 0.9914 0.9933 0.9953 0.9973 0.9992 1.0012 197.5 0.9916 0.0035 0.9955 0.9975 0.9994 1.0014

24A TEMP ˚F 75 75.5 76 76.5 77 77.5

53A TEMP ˚C -18 -17.75 -17.5 -17.25 -17 -16.75

54A TEMP ˚C 14 14.25 14.5 14.75 15 15.25

24B

CRUDE OILS RELATIVE DENSITY 60/60˚F 0.612 0.614 0.616 0.618 0.62 0.622 CORRESPONDING RELATIVE DENSITY 60/60˚F 0.9863 0.9863 0.9864 0.9865 0.9866 0.9867 0.9858 0.9859 0.986 0.9861 0.9862 0.9863 0.9853 0.9854 0.9855 0.9856 0.9857 0.9858 0.9849 0.985 0.9851 0.9852 0.9853 0.9854 0.9844 0.9845 0.9846 0.9847 0.9848 0.9849 0.984 0.9841 0.9842 0.9843 0.9844 0.9845

RELATIVE DENSITY 60/60˚F 0.89 0.892 0.894 0.896 0.898 0.9 FACTOR FOR CORRECTING VOLUME TO 60˚F 0.9671 0.9672 0.9673 0.9674 0.9675 0.9675 0.9668 0.9669 0.967 0.9671 0.9672 0.9673 0.9666 0.9667 0.9668 0.9669 0.967 0.9671 0.9664 0.9665 0.9666 0.9667 0.9668 0.9669 0.9662 0.9663 0.9664 0.9665 0.9666 0.9667 0.966 0.9661 0.9662 0.9663 0.9664 0.9665

53B

CRUDE OILS DENSITY AT OBSERVED TEMPERATURE 950.0 952.0 954.0 956.0 958.0 CORRESPONDING DENSITY AT 15˚C 929.1 931.1 933.1 935.2 937.3 929.2 931.3 933.3 935.4 937.4 929.4 931.4 933.5 935.5 937.6 929.5 931.6 933.6 935.7 937.7 929.7 931.7 933.8 935.8 937.9 929.9 931.9 934 936 938

TEMP ˚F 135 135.5 136 136.5 137 137.5

OIL PRODUCTS

960.0 939.3 939.5 939.6 939.8 939.9 940.1

CRUDE OILS DENSITY AT 15 ˚C 990 992.0 994.0 996.0 998.0 1000.0 FACTOR FOR CORRECTING VOLUME TO 15 ˚C 1.0006 1.0006 1.0006 1.0006 1.0006 1.0006 1.0005 1.0005 1.0005 1.0005 1.0005 1.0005 1.0003 1.0003 1.0003 1.0003 1.0003 1.0003 1.0002 1.0002 1.0002 1.0002 1.0002 1.0002 1 1 1 1 1 1 0.9998 0.9998 0.9998 0.9998 0.9998 0.9998

TEMP ˚C -0.5 -0.25 0 0.25 0.5 0.75

OIL PRODUCTS DENSITY AT OBSERVED TEMPERATURE 997 999.0 1001.0 1003.0 1005.0 1007.0 CORRESPONDING DENSITY AT 15˚C 986.9 988.9 990.9 992.9 994.9 996.9 987.1 989.1 991.1 993.1 995.1 997.1 987.2 989.2 991.2 993.3 995.3 997.3 987.4 989.4 991.4 993.4 995.4 997.4 987.6 989.6 991.6 993.6 995.6 997.6 987.7 989.7 991.7 993.7 995.8 997.8

54B

OIL PRODUCTS DENSITY AT 15 ˚C 732.0 734.0 736.0 738.0 740.0 CORRESPONDING DENSITY AT 15˚C 0.9684 0.9686 0.9687 0.9688 0.969 0.9691 0.9681 0.9683 0.9684 0.9685 0.9687 0.9688 0.9678 0.9679 0.9681 0.9682 0.9683 0.9685 0.9675 0.9676 0.9678 0.9679 0.968 0.9682 0.9672 0.9673 0.9674 0.9676 0.9677 0.9679 0.9669 0.967 0.9671 0.9673 0.9674 0.9675 730

TEMP ˚C 40 40.25 40.5 40.75 41 41.25

54D

OIL PRODUCTS DENSITY AT 15 ˚C 732.0 734.0 736.0 738.0 740.0 CORRESPONDING DENSITY AT 15˚C 0.9684 0.9686 0.9687 0.9688 0.969 0.9691 0.9681 0.9683 0.9684 0.9685 0.9687 0.9688 0.9678 0.9679 0.9681 0.9682 0.9683 0.9685 0.9675 0.9676 0.9678 0.9679 0.968 0.9682 0.9672 0.9673 0.9674 0.9676 0.9677 0.9679 0.9669 0.967 0.9671 0.9673 0.9674 0.9675 730

TEMP ˚C 40 40.25 40.5 40.75 41 41.25

6C

OIL PRODUCTS

COEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F) 530 532 534 536 538 540 TEMP ˚F FACTOR FOR CORRECTING VOLUME TO 60˚F 75 0.992 0.992 0.992 0.9919 0.9919 0.9919 75.5 0.9918 0.9917 0.9917 0.9917 0.9916 0.9916 76 0.9915 0.9915 0.9914 0.9914 0.9914 0.9913 76.5 0.9912 0.9912 0.9912 0.9911 0.9911 0.9911 77 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 PRODUCTS

COEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F) 490 492 494 496 498 500 TEMP ˚F FACTOR FOR CORRECTING VOLUME TO 60˚F 105 0.9778 0.9777 0.9776 0.9775 0.9774 0.9774 105.5 0.9776 0.9775 0.9774 0.9773 0.9772 0.9771 106 0.9773 0.9772 0.9771 0.977 0.9769 0.9768 106.5 0.9771 0.977 0.9769 0.9768 0.9767 0.9766 107 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 PRODUCTS

COEFFICIENT OF THERMAL EXPANSION * 1000000 (1/DEG F) 800 804 808 812 816 820 TEMP ˚C FACTOR FOR CORRECTING VOLUME TO 15˚C 62.5 0.9616 0.9614 0.9612 0.961 0.9608 0.9606 62.75 0.9614 0.9612 0.961 0.9608 0.9606 0.9604 63 0.9612 0.961 0.9608 0.9606 0.9604 0.9602 63.25 0.961 0.9608 0.9606 0.9604 0.9602 0.96 63.5 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 calculation Density @ 15/vac= Actual temp= VCF Table 54A= Table 54B= Table 54D=

0.8668 39.50 0.9799 0.9800 0.9822

Density @ actual temp 0.8494 0.8495 0.8514

Corresponding dcc (approximate) 0.00071 0.00071 0.00063

Mass 5983.45 Volume 7044.51 7043.79 7028.01

User info Density @ 15/vac= Actual temp= diff temp=

866.8 39.5 24.5

General formula: VCF=exp(b) and : a=(K0+K1xDensity @ 15/vac)/(Density @ 15/vac^2) b=-a x diff temp x (1+0,8 x a x diff temp) diff temp=actual temp-15 Formula for Table 54B and 770