March 13, 2017 | Author: Putra Pradana | Category: N/A
ASTM API GRAVITY API GRAVITY
5A 8.5 2.28
AT AT
ASTM API GRAVITY API GRAVITY
5B 10.5 6.74
OIL PRODUCTS AT 135 ˚F 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
CRUDE OILS 210 ˚F 60 ˚F
˚F
http://www.bgicrew.com/ САНКТ-ПЕТЕРБУРГ Тел.: +7 812 346 80 08 Факс: +7 812 346 73 32
E-mail :
[email protected] ЗДЕСЬ МОГЛА БЫТЬ ВАША РЕКЛАМА PLACE FOR YOUR ADVERTISEMENT
CRUDE OILS 60 ˚F 60 ˚F
OIL PRODUCTS AT 0 ˚F AT 60 ˚F 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 0.67 0.88975 GASOLINE
OIL PRODUCTS AT 60 ˚F AT 195.5 ˚F
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 54A
ASTM
Volume: Volume at 15oC: o
Weight in Vac.at 15 C: Weight in Air at 15oC:
Volume: o Volume at 15 C:
3
500 475.3269 0.511452 -0.01141
M
500 444.8734 0.298065 -0.1913
M3
M3 M.T. M.T.
M3 M.T. M.T.
3 500 M 3 509.6906 M
CRUDE OILS 25 ˚C 15 ˚C
OIL PRODUCTS AT 4.5 ˚C AT 15 ˚C CRUDE OILS
Volume:
3
500 M
DENSITY VCF TO 15˚C
1050 0.97758
AT AT
15 55
˚C ˚C
3
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 15 C:
488.7912 M 513.2308 M.T. 512.6931 M.T.
OIL PRODUCTS AT 15 ˚C AT -12.5 ˚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: o Volume at 15 C:
500 496.405 434.3544 433.8083
o
Weight in Vac.at 15 C: o
Weight in Air at 15 C:
o
Weight in Vac.at 15 C: o
Weight in Air at 15 C:
ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail:
[email protected]
http://oleg352.mail333.su/
500 508.5287 540.0575 539.4981
M3
54B 1062 1.01706 FUEL OIL
3
M M.T. M.T.
3
M
3
M M.T. M.T.
[email protected]
ЫТЬ ВАША РЕКЛАМА R ADVERTISEMENT
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 33 0.9851
ASTM Temp.Exp.Coef.
54C 640
Real temp: VCF:
115 0.9349
ASTM Density in vac.: Real temp: VCF:
54D 0.875 25 0.9928
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 15
Volume: Volume at 15oC: Weight in Vac.at 15oC: Weight in Air at 15oC:
Расчет поправок к плотности груза по таблицам ASTM c точностью бумажных таблиц 1 ASTM 54D СМАЗОЧНЫЕ МАСЛА ASTM Density in vac.: Real temp: VCF:
54D 0.873 24.6 0.9931
at temp C
LUBE OILS 0 C 15
TEMP1
0
ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail:
[email protected]
http://oleg352.mail333.su/
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
http://www.bgicrew.com/ 500 492.54365 420.9278 420.386
САНКТ-ПЕТЕРБУРГ
500 467.46819
Тел.: +7 812 346 80 08
Владимирский пр., д. 23, лит. А, “Регент холл”, 5-й этаж, г. Санкт-Петербург 191002 Россия
Факс: +7 812 346 73 32
E-mail :
[email protected]
? ? 500 496.405 434.35438 433.80833
Density at Den1 0.872 0.9931 0.99306 0.9930
ЗДЕСЬ МОГЛА БЫТЬ ВАША РЕКЛАМА
15
˚C Den2 0.873 0.874 0.99315 0.9932 0.99309 0.99312 0.993 0.9930
Скорость налива в танк для электростатических жидкостей Диам.трубы= 300 мм 1 м/с 7 м/с Скорость налива в пределах: 254.5 1781.3 Максимальная скорость налива в танк по времени реагирования 1 мин. 3 V100%= 2000 m 3 V98%= 1960 m Скорость налива:
3 2400 м /час
Определение максимальной высоты подъема жидкости насосом 9,8 m/s2 Давление насоса 800000 3 Плотность жидк. 1000 кг/м вода: 1000 макс.высота 81.632653 м
Определение поправки к объему груза за нагрев 1. Для смазочных масел - таблица 54 D Volume before Dens. In Vac Temp. before Temp. after: Difference: Volume after
1000 0.875 at o 25 C o 50 C
m3 15
18.57 1018.57
m 3 m
o
C
3
ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail:
[email protected]
http://oleg352.mail333.su/
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
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
346.4228 0.4388 54D 0 0.6278 All ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail:
[email protected] http://oleg352.mail333.su/
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
