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(b) Figure Q1(b) shows a flowchart of a combustion-condensation process. Each stream contains two components (A and B) in different proportions. Three streams whose flow rates and/or compositions are not known are labeled a, b and c. (Gambarajah Q1fb) menunjukkan carta ahir proses pembakaran-pemehewapan. Setiap saluran mempunyai dua komponen (A dan B) dalam pecahan berbeza. Tigu saluran yang tidak diketahui kadar alir dan atau pecahannya di label sebagai a, b dan c.) (1) (ii) 100 kg/h 0.500 kg A/kg 0.500 kg B/kg 60 kg/h 0.700 kg A/kg 0.300 kg B/kg Unit L b 50 kg/h 0.600 kg A/kg 0.400 kg B/kg Unit 2 50 kg/h 0.500 kg A/kg 0.500 kg B/kg Figure Q1(b) Flowchart of a combustion-condensation process. (Rajah Q1(b) Carta alir proses pembakaran-pemeluwapan. J Identify degree of freedom analysis for overall system and Unit 1. [Tentukan analisa darjah kebebasan untuk Unit I dan keseluruhan sistem. Calculate the unknown flow rates and compositions of stream a, b and c.

(b) Figure Q1(b) shows a flowchart of a combustion-condensation process. Each stream contains two components (A and B) in different proportions. Three streams whose flow rates and/or compositions are not known are labeled a, b and c. (Gambarajah Q1fb) menunjukkan carta ahir proses pembakaran-pemehewapan. Setiap saluran mempunyai dua komponen (A dan B) dalam pecahan berbeza. Tigu saluran yang tidak diketahui kadar alir dan atau pecahannya di label sebagai a, b dan c.) (1) (ii) 100 kg/h 0.500 kg A/kg 0.500 kg B/kg 60 kg/h 0.700 kg A/kg 0.300 kg B/kg Unit L b 50 kg/h 0.600 kg A/kg 0.400 kg B/kg Unit 2 50 kg/h 0.500 kg A/kg 0.500 kg B/kg Figure Q1(b) Flowchart of a combustion-condensation process. (Rajah Q1(b) Carta alir proses pembakaran-pemeluwapan. J Identify degree of freedom analysis for overall system and Unit 1. [Tentukan analisa darjah kebebasan untuk Unit I dan keseluruhan sistem. Calculate the unknown flow rates and compositions of stream a, b and c.

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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(b) Figure Q1(b) shows a flowchart of a combustion-condensation process. Each stream contains two components (A and B) in different proportions. Three streams whose flow rates and/or compositions are not known are labeled a, b and c. (Gambarajah Q1fb) menunjukkan carta alir proses pembakaran-pemehewapaun. Setiap saluran mempunyai dua komponen (A dan B) dalam pecahan berbeza. Tigu saluran yang tidak diketahui kadar alir dan atau pecahannya di label sebagai a, b dan c./ E 100 kg/h 0.500 kg A/kg 0.500 kg B/kg 60 kg/h 0.700 kg A/kg 0.300 kg B/kg Unit L b 50 kg/h 0.600 kg A/kg 0.400 kg B/kg Unit 2 50 kg/h 0.500 kg A/kg 0.500 kg B/kg Figure Q1(b) Flowchart of a combustion-condensation process. (Rajah Q1(b) Carta alir proses pembakaran-pemeluwapan.] Identify degree of freedom analysis for overall system and Unit 1. [Tentukan analisa darjah kebebasan untuk Unit I dan keseluruhan sistem. Calculate the unknown flow rates and compositions of stream a, b and c.
Transcribed Image Text:(b) Figure Q1(b) shows a flowchart of a combustion-condensation process. Each stream contains two components (A and B) in different proportions. Three streams whose flow rates and/or compositions are not known are labeled a, b and c. (Gambarajah Q1fb) menunjukkan carta alir proses pembakaran-pemehewapaun. Setiap saluran mempunyai dua komponen (A dan B) dalam pecahan berbeza. Tigu saluran yang tidak diketahui kadar alir dan atau pecahannya di label sebagai a, b dan c./ E 100 kg/h 0.500 kg A/kg 0.500 kg B/kg 60 kg/h 0.700 kg A/kg 0.300 kg B/kg Unit L b 50 kg/h 0.600 kg A/kg 0.400 kg B/kg Unit 2 50 kg/h 0.500 kg A/kg 0.500 kg B/kg Figure Q1(b) Flowchart of a combustion-condensation process. (Rajah Q1(b) Carta alir proses pembakaran-pemeluwapan.] Identify degree of freedom analysis for overall system and Unit 1. [Tentukan analisa darjah kebebasan untuk Unit I dan keseluruhan sistem. Calculate the unknown flow rates and compositions of stream a, b and c.
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