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✓ Given that the conversion of C2H6 in the reactor is 13% and the A. 312 product stream contains 11 mol C₂H5CI/mol C₂H4Cl2, calculate the mole ratio of C₂H6 to Cl2₂ in the inlet stream to the reactor. Hint: Do an elemental balance around the reactor. Make a basis of 100 mol/h C2H5Cl in the reactor effluent. ✓ If 3 mol of the recycle stream is mixed with every 1 mol of fresh feed gas fed into the process, and the stream entering the reactor is 17 mole % N2, calculate the molar flow rate of the purge stream with a basis of 100 mol/h C2H5CI leaving the reactor. B.288 C. 448 D. 6.33 E. 7.10 F. 4.95

✓ Given that the conversion of C2H6 in the reactor is 13% and the A. 312 product stream contains 11 mol C₂H5CI/mol C₂H4Cl2, calculate the mole ratio of C₂H6 to Cl2₂ in the inlet stream to the reactor. Hint: Do an elemental balance around the reactor. Make a basis of 100 mol/h C2H5Cl in the reactor effluent. ✓ If 3 mol of the recycle stream is mixed with every 1 mol of fresh feed gas fed into the process, and the stream entering the reactor is 17 mole % N2, calculate the molar flow rate of the purge stream with a basis of 100 mol/h C2H5CI leaving the reactor. B.288 C. 448 D. 6.33 E. 7.10 F. 4.95

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
Section: Chapter Questions
Problem 1.1P
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M0n0chl0r0ethane (C2H5Cl) is pr0duced by the chl0rinati0n 0f ethane acc0rding t0 the reacti0n bel0w. An undersired side reacti0n can 0ccur where the m0n0chl0r0ethane is further chlr0inated f0rming dichl0r0ethane (C2H4Cl2). Sh0w s0lution. Ch0ices are F0und at the rightside

Given that the conversion of C2H6 in the reactor is 13% and the A. 312 product stream contains 11 mol C2H5CI / mol C2H4CI2, calculate the mole ratio of C2H6 to Cl2 in the inlet stream to the В. 288 reactor. С. 448 Hint: Do an elemental balance around the reactor. Make a basis of 100 mol/h C2H5CI in the reactor effluent. D. 6.33 Е. 7.10 v If 3 mol of the recycle stream is mixed with every 1 mol of fresh feed gas fed into the process, and the stream entering the reactor is 17 mole % N2, calculate the molar flow rate of the purge stream with a basis of 100 mol/h C2H5CI leaving the F. 4.95 reactor.
Transcribed Image Text:Given that the conversion of C2H6 in the reactor is 13% and the A. 312 product stream contains 11 mol C2H5CI / mol C2H4CI2, calculate the mole ratio of C2H6 to Cl2 in the inlet stream to the В. 288 reactor. С. 448 Hint: Do an elemental balance around the reactor. Make a basis of 100 mol/h C2H5CI in the reactor effluent. D. 6.33 Е. 7.10 v If 3 mol of the recycle stream is mixed with every 1 mol of fresh feed gas fed into the process, and the stream entering the reactor is 17 mole % N2, calculate the molar flow rate of the purge stream with a basis of 100 mol/h C2H5CI leaving the F. 4.95 reactor.
C,H,+Cl,¬C,H¸CI+ HCI C,H,CI+Cl,¬C,H,Cl,+HCI The process below is fed with a mixture of ethane, chlorine gas and nitrogen gas. A recycle stream is mixed with the feed gas stream before being fed into a reactor. The reactor effluent stream is fed into a separator where all the C2H5CI, C2H5CI2, and HCl are separated from the other gases. The separated gas stream is purged before it is recycled to combine with the fresh feed. Recycle Purge Separated Gas Fresh Feed Reactor Separator Separated Liquid
Transcribed Image Text:C,H,+Cl,¬C,H¸CI+ HCI C,H,CI+Cl,¬C,H,Cl,+HCI The process below is fed with a mixture of ethane, chlorine gas and nitrogen gas. A recycle stream is mixed with the feed gas stream before being fed into a reactor. The reactor effluent stream is fed into a separator where all the C2H5CI, C2H5CI2, and HCl are separated from the other gases. The separated gas stream is purged before it is recycled to combine with the fresh feed. Recycle Purge Separated Gas Fresh Feed Reactor Separator Separated Liquid
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