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6. It is desired to lower the n-hexane content of a nitrogen- n-hexane mixture at 45°C (the partial pressure of n-hexane =310 mmHg) and a total pressure of 757 mmHg to a mixture containing 15% mole n-hexane. This could be achieved by passing a portion of the gas mixture through a chiller which condenses out some of the n-hexane and leaves the gas saturated at 10°C (the partial pressure of n-hexane =64 mmHg) and a total pressure of 750 mmHg. The bypassed gas mixes with the gas from the chiller to form 15% mole n-hexane. Three hundred cubic meters per minute of the original gas mixture is to be treated. Wolaby 11 Solve o 2a) kmoles/min of the final mixture containing 15% mole n-hexaneou enidmon b) kmoles/min of the n-hexane condenses in the chiller of blupil joc) kmoles/min of the gas that bypasses the chiller.

6. It is desired to lower the n-hexane content of a nitrogen- n-hexane mixture at 45°C (the partial pressure of n-hexane =310 mmHg) and a total pressure of 757 mmHg to a mixture containing 15% mole n-hexane. This could be achieved by passing a portion of the gas mixture through a chiller which condenses out some of the n-hexane and leaves the gas saturated at 10°C (the partial pressure of n-hexane =64 mmHg) and a total pressure of 750 mmHg. The bypassed gas mixes with the gas from the chiller to form 15% mole n-hexane. Three hundred cubic meters per minute of the original gas mixture is to be treated. Wolaby 11 Solve o 2a) kmoles/min of the final mixture containing 15% mole n-hexaneou enidmon b) kmoles/min of the n-hexane condenses in the chiller of blupil joc) kmoles/min of the gas that bypasses the chiller.

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
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roda out sdi otropod po SS a doinw 6. It is desired to lower the n-hexane content of a nitrogen- n-hexane mixture at 45°C (the partial pressure of n-hexane =310 mmHg) and a total pressure of 757 mmHg to a mixture containing 15% mole n-hexane. This could be achieved by passing a portion of the gas mixture through a chiller which condenses out some of the n-hexane and leaves the gas saturated at 10°C (the partial pressure of n-hexane =64 mmHg) and a total pressure of 750 mmHg. The bypassed gas mixes with the gas from the chiller to form 15% mole n-hexane. Three hundred cubic meters per minute of the original gas mixture is to be treated. Solve p a) kmoles/min of the final mixture containing 15% mole n-hexane washidm it b) kmoles/min of the n-hexane condenses in the chiller el bupil joc) kmoles/min of the gas that bypasses the chiller. Feat brip
Transcribed Image Text:roda out sdi otropod po SS a doinw 6. It is desired to lower the n-hexane content of a nitrogen- n-hexane mixture at 45°C (the partial pressure of n-hexane =310 mmHg) and a total pressure of 757 mmHg to a mixture containing 15% mole n-hexane. This could be achieved by passing a portion of the gas mixture through a chiller which condenses out some of the n-hexane and leaves the gas saturated at 10°C (the partial pressure of n-hexane =64 mmHg) and a total pressure of 750 mmHg. The bypassed gas mixes with the gas from the chiller to form 15% mole n-hexane. Three hundred cubic meters per minute of the original gas mixture is to be treated. Solve p a) kmoles/min of the final mixture containing 15% mole n-hexane washidm it b) kmoles/min of the n-hexane condenses in the chiller el bupil joc) kmoles/min of the gas that bypasses the chiller. Feat brip
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