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Q2): 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 Percent 26.8 5.63 Latent heat (Btu/Lb) 120 113 CPL CP, (Btu/Lb "F) (Btu/Lb "F)CF. Gasoline Naphtha Kerosene Gas oil 62.8 52.8 110 155 0.615 0,604 0.59 0.58 286 335 19.8 45.6 185 100 0.604 0.60 420 10.6 39.4 240 0.615 0.74 90 0.63 510 Reduced crude |36.97 Crude Steam 31.2 510 100,00 576 0.5 535 Check the Naphtha plate temperature if hot reflux is used, the dew point and bubble point of gas oil are 380 °F and 360 ° F respectively and the pressure at the withdrawn plate is 810 mm Hg. Given: 1 BPD - 42gal, Pra 8.324 Ib/gal

Q2): 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 Percent 26.8 5.63 Latent heat (Btu/Lb) 120 113 CPL CP, (Btu/Lb "F) (Btu/Lb "F)CF. Gasoline Naphtha Kerosene Gas oil 62.8 52.8 110 155 0.615 0,604 0.59 0.58 286 335 19.8 45.6 185 100 0.604 0.60 420 10.6 39.4 240 0.615 0.74 90 0.63 510 Reduced crude |36.97 Crude Steam 31.2 510 100,00 576 0.5 535 Check the Naphtha plate temperature if hot reflux is used, the dew point and bubble point of gas oil are 380 °F and 360 ° F respectively and the pressure at the withdrawn plate is 810 mm Hg. Given: 1 BPD - 42gal, Pra 8.324 Ib/gal

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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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 Latent heat CPL CP, Percent (Btu/Lb) (Btu/Lb "F) (Btu/Lb "F) (F) Gasoline 26.8 62.8 110 120 0.615 0.59 286 52.8 0.604 Naphtha Kerosene 5.63 155 113 0.58 335 19.8 45.6 185 100 0.604 0.60 420 Gas oil 10.6 39.4 240 90 0.615 0.63 510 Reduced crude 36.97 31.2 0.74 510 Crude 100.00 576 | Steam 0.5 535 Check the Naphtha plate temperature if hot reflux is used, the dew point and bubble point of gas oil are 380 ° F and 360 ° F respectively and the pressure at the withdrawn plate is 810 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 Latent heat CPL CP, Percent (Btu/Lb) (Btu/Lb "F) (Btu/Lb "F) (F) Gasoline 26.8 62.8 110 120 0.615 0.59 286 52.8 0.604 Naphtha Kerosene 5.63 155 113 0.58 335 19.8 45.6 185 100 0.604 0.60 420 Gas oil 10.6 39.4 240 90 0.615 0.63 510 Reduced crude 36.97 31.2 0.74 510 Crude 100.00 576 | Steam 0.5 535 Check the Naphtha plate temperature if hot reflux is used, the dew point and bubble point of gas oil are 380 ° F and 360 ° F respectively and the pressure at the withdrawn plate is 810 mm Hg. Given: 1 BPD = 42gal, pwater= 8.324 lb/gal
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