Q2): 1200 BPD of 32. were obtained in the Volu Perc Gasoline 26.8 Naphtha 5.63 Kerosene 19.8 Gas oil 10.6 Reduced 36.9 crude Crude 100 Steam Check the gas oil p respectively and the Given: 1 BPD = 42

Structural Analysis
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Chapter2: Loads On Structures
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Q2): 1200 BPD of 32 ° API crude oil is fed to an atmospheric distillation unit, the following products
were obtained in the presence of 567 lb/hr steam. Assume vaporization temperature = 576 °F
Volume,
°API
Mw
T
Latent heat
CP,
CPL
Percent
(Btu/Lb)
(Btu/Lb °F)
(Btu/Lb °F)
(°F)
Gasoline
26.8
62.8
286
110
0.615
120
0.59
Naphtha
5.63
52.8
113
155
335
0.604
0.58
420
Kerosene
19.8
45.6
185
100
0.60
0.604
Gas oil
510
10.6
39.4
240
0.615
90
0.63
510
Reduced
36.97
0.74
31.2
crude
576
Crude
100.00
0.5
535
Steam
Check the gas oil plate temperature if the dew point and bubble point of gas oil are 600 ° F and 580 ° F
respectively and the pressure at the withdrawn plate is 990 mm Hg.
Given: 1 BPD = 42gal, pwater 8.324 lb/gal
Transcribed Image Text:Q2): 1200 BPD of 32 ° API crude oil is fed to an atmospheric distillation unit, the following products were obtained in the presence of 567 lb/hr steam. Assume vaporization temperature = 576 °F Volume, °API Mw T Latent heat CP, CPL Percent (Btu/Lb) (Btu/Lb °F) (Btu/Lb °F) (°F) Gasoline 26.8 62.8 286 110 0.615 120 0.59 Naphtha 5.63 52.8 113 155 335 0.604 0.58 420 Kerosene 19.8 45.6 185 100 0.60 0.604 Gas oil 510 10.6 39.4 240 0.615 90 0.63 510 Reduced 36.97 0.74 31.2 crude 576 Crude 100.00 0.5 535 Steam Check the gas oil plate temperature if the dew point and bubble point of gas oil are 600 ° F and 580 ° F respectively and the pressure at the withdrawn plate is 990 mm Hg. Given: 1 BPD = 42gal, pwater 8.324 lb/gal
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