HW5.3: 120000 Lb/hr of 340API crude oil at 6500F is fed to an atmospheric distillation unit. Steam at a rate of 600 Ib/hr and 8500F is used. The fraction obtained were 34000 Ib/hr gasoline (MW=110, 2=120) at 310 0F; 12000 Ib/hr kerosene (MW=185, A=108) at 420 ’ F; 30000 Ib/hr gas oil (MW=270, 1=95) at 510 OFA o o The residue is withdrawn at 510 F. Assume C = 0.7, C = 0.6 Btw/lb. F and the vaporizion PL PV 0 temperature=576 F o a) Check the top tower temperature if the dew point of gasoline is 296 F and the pressure at the top plate is 780 mm Hg. . b) Calculate the diameter of the tower if K=735 and p =42.7 Ib/ft . L H.W 5.3:120000 Lb/hr of 34 API crude oil at 650 F is fed to an atmospheric distillation unit. Steam at arate of 600 lb/hr and 850 F is used. The fraction obtained were 34000 lb/hr gasoline (MW=110,1=120) at 310 F; 12000 lb/hr kerosene (MW=185, 2=108) at 420F; 30000 lb/hr gas oil(MW=270, A=95) at 510 F.The residue is withdrawn at 510 F. Assume C = 0.7, C= 0.6 Btu/lb. F and the vaporizionPLPVtemperature=576 Fa) Check the top tower temperature if the dew point of gasoline is 296 Fand the pressure at thetop plate is 780 mm Hg.3b) Calculate the diameter of the tower if K=735 and p = 42.7 lb/ft.L

a) Crude oil = 120000 lb/hr at T = 650 0F, steam = 600 lb/hr at T = 850 0F. They are fed to the…

Answered: H.W 5.3: 120000 Lb/hr of 34 API crude…

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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Problem 1.1P

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HW5.3: 120000 Lb/hr of 340API crude oil at 6500F is fed to an atmospheric distillation unit. Steam at a rate of 600 Ib/hr and 8500F is used. The fraction obtained were 34000 Ib/hr gasoline (MW=110, 2=120) at 310 0F; 12000 Ib/hr kerosene (MW=185, A=108) at 420 ’ F; 30000 Ib/hr gas oil (MW=270, 1=95) at 510 OFA o o The residue is withdrawn at 510 F. Assume C = 0.7, C = 0.6 Btw/lb. F and the vaporizion PL PV 0 temperature=576 F o a) Check the top tower temperature if the dew point of gasoline is 296 F and the pressure at the top plate is 780 mm Hg. . b) Calculate the diameter of the tower if K=735 and p =42.7 Ib/ft . L

H.W 5.3:
120000 Lb/hr of 34 API crude oil at 650 F is fed to an atmospheric distillation unit. Steam at a
rate of 600 lb/hr and 850 F is used. The fraction obtained were 34000 lb/hr gasoline (MW=110,
1=120) at 310 F; 12000 lb/hr kerosene (MW=185, 2=108) at 420
F; 30000 lb/hr gas oil
(MW=270, A=95) at 510 F.
The residue is withdrawn at 510 F. Assume C = 0.7, C
= 0.6 Btu/lb. F and the vaporizion
PL
PV
temperature=576 F
a) Check the top tower temperature if the dew point of gasoline is 296 Fand the pressure at the
top plate is 780 mm Hg.
3
b) Calculate the diameter of the tower if K=735 and p = 42.7 lb/ft.
L

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