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...


Q2): 1200 BPD of 32 ° API crude oil is fed to an atmospheric distillation unit, the following products were<br>obtained in the presence of 567 lb/hr steam. Assume vaporization temperature = 576 °F<br>Volume,<br>

Extracted 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reflux is used, the dew point and bubble point of gas oil are 380 ° F and 360 ° F respectively and the pressure at the withdrawn plate is 810 mm Hg.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

Jun 09, 2022
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