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 08
API 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 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 0.67 AT 60 ˚F à 444.8734
VCF TO 60˚F 0.88975 AT 195.5 ˚F 0.298065 M.T.
GASOLINE -0.191296 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
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
FUEL OIL
ASTM 54A CRUDE OILS Volume: 500
DENSITY 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: 500
DENSITY 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: 500
TEC 1644 AT 15 ˚C à 526.6338VCF TO 15˚C 1.0533 AT -18 ˚C
ASTM 54D LUBE OILS Volume: 500
Density 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 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:
Density in vac.: 0.73 at temp 15
Real temp: 40
VCF: 0.9684
ASTM 54C Volume:
Temp.Exp.Coef. 640 at temp 15
Real temp: 115
VCF: 0.9349
ASTM 54D LUBE OILS Volume:
Density in vac.: 0.875 at temp 15
Real temp: 25
VCF: 0.9928
Расчет поправок к плотности груза по таблицам ASTM c точностью бумажных таблиц1 ASTM 54D СМАЗОЧНЫЕ МАСЛА
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
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 SG
API - American Petroleum Institute945.636455 VCF - Volume Correction Factor
500
499.79
427.120534
426.570765http://www.bgicrew.com/
500 САНКТ-ПЕТЕРБУРГ
484.223326 Владимирский пр., д. 23, лит. А,
353.483028 “Регент холл”, 5-й этаж,
352.950383 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 РЕКЛАМА
496.405
434.354375
433.808329
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
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.
2000
1960
Скорость налива: 2400
Определение максимальной высоты подъема жидкости насосом
Давление насоса 800000
Плотность 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 12000 0.83 28
Dens. In Vac 0.83 at 28 25
Temp. before 25 1 temp 1.0023
Temp. after: 20 0.83 28
Difference: -44.968 20
Volume after 11955.032 2 temp 1.0060
ASTM Tables ver 1,1 © Oleg Boriskin 2009 e-mail: [email protected]
m3
oCoCoC
m3
m3
http://oleg352.mail333.su/
Volume: 12000
12027.24
9982.6092
9969.379236
Volume: 11955.031609
12027.24
9982.6092
9969.379236
Volume at 15oC:
Weight in Vac.at 15oC:
Weight in Air at 15oC:
Volume at 15oC:
Weight in Vac.at 15oC:
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-80
0.0 PAGE X-80
WHERE ∆t = t - 60 (˚F)CONVERT API GRAVITY TO DENSITY:
API = observed API gravity
PAGE X-6
5B 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-91
6B VOLUME II
6BWHERE ∆t = t - 60 (˚F)
PAGE X-112
6C 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+
B
ρ602
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
WHERE
PAGE 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*999,012
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
α 60=K0ρ602
+K1ρ60
VCF=EXP [−α60 Δt (1+0 .8α60 Δt )]ρt=ρ60EXP [−α 60 Δt(1+0 .8α 60 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=K 0ρ152
+K1ρ15
α 60=K0+K1 ρ60
ρ602
α 60=A+B
ρ602
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=K 0ρ152
+K1ρ15
VCF=EXP [−α15 Δt (1+0 .8α15 Δt ) ]ρt= ρ15EXP [−α15 Δt (1+0 .8α 15Δt ) ]
α 15=K 0ρ152
+K1ρ15
VCF=EXP [−α15 Δt (1+0 .8α15 Δt ) ]ρt= ρ15EXP [−α15 Δt (1+0 .8α 15Δt ) ]
VCF=EXP [−α15 Δt (1+0 .8α15 Δt ) ]
α 15=K 0ρ152
+K1ρ15
VCF=EXP [−α15 Δt (1+0 .8α15 Δt ) ]
α 15=K 0ρ152
+K1ρ15
VCF=EXP [−α15 Δt (1+0 .8α15 Δt ) ]
α 15=K 0ρ152
+K1ρ15
α 15=K0+K1 ρ15
ρ152
α 15=A+B
ρ152
VCF=EXP [−α15 Δt (1+0 .8α15 Δt ) ]
15
1215
015
KK α 15=
K0+K1 ρ15ρ152
α 15=A+B
ρ152
GENERALIZED CRUDE OILS CORRECTION OF OBSERVED API GRAVITY TO API GRAVITY AT 60°F
RANGE
˚API ˚F0…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+B
ρ602
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
˚C486…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˚ 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 © 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 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
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 25
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 26
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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