spnene lowing products in the presence of 567 lb/hr steam. Assume vaporization temperature = 576 °F Volume, Percent Latent heat (Btu/Lb) 120 CP (Btu/Lb "F) "API Mw CP, (Btu/Lb "F) 0.59 0.58 T "F) Gasoline 26.8 62.8 110 0.615 286 Naphtha Kerosene 5.63 52.8 155 113 0.604 335 0.60 0.63 19.8 45.6 185 100 0.604 420 Gas oil Reduced crude 10.6 36.97 39.4 240 90 0.615 0.74 510 510 31.2 Crude Steam 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hot reflux is used, the dew point and bubble point of gas oil are 380 F and 360 F respectively and the pressure at the withdrawn plate is 810 mm Hg.
spnene lowing products in the presence of 567 lb/hr steam. Assume vaporization temperature = 576 °F Volume, Percent Latent heat (Btu/Lb) 120 CP (Btu/Lb "F) "API Mw CP, (Btu/Lb "F) 0.59 0.58 T "F) Gasoline 26.8 62.8 110 0.615 286 Naphtha Kerosene 5.63 52.8 155 113 0.604 335 0.60 0.63 19.8 45.6 185 100 0.604 420 Gas oil Reduced crude 10.6 36.97 39.4 240 90 0.615 0.74 510 510 31.2 Crude Steam 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hot reflux is used, the dew point and bubble point of gas oil are 380 F and 360 F respectively and the pressure at the withdrawn plate is 810 mm Hg.
Chemistry
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ISBN:9781305957404
Author:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Publisher:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Chapter1: Chemical Foundations
Section: Chapter Questions
Problem 1RQ: Define and explain the differences between the following terms. a. law and theory b. theory and...
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