The gas phase reaction, A+ 3B-C, has a rate that is 1/2 order in A and 1/2 order in B. Thisreaction is to be carried out isothermally at 55°C ad isobariclly at 506.625 Pa in a plug flowreactor. The gas stream entering the reactor has three components: A, B and I (an inertcompound). The flew rates of A and B into the reactor are 0,01 mol A/s and 0.03 mol B/s.Additional information for this reactor is given below:Total molar flowrateVolen tarieTotal flowrate into the reactor. VRate constant, KAUniversal Clas Law ConstantcomABCIFA3 FA0Oa) Construct a stoichiometric table for the above process.Irbis chany RemingFAX3 FAXFADF-0.3716 mol/sVo =0.002 m/s-mmol Akgcats mol BR-8.314 Pa m³/(mol K)-0.001-F₁ (1-x)f^(₂x)-FAU0-5| ² (0·001) = 0·031€-$₂S =Y P0.33 *RT 8314+=0.365LADb) Estimate the volume of reactor required to achieve xA=0.75 assuming that the reactantsare dilute.

A gas phaser reaction is carried out isothermally in a plug flow reactor.

430 The gas phase reaction, A+ 3B-C, has a rate that is 1/2 order in A and 1/2 order in B. This reaction is to be carried out isothermally at 55°C ad isobariclly at 506.625 Pa in a plug flow reactor. The gas stream entering the reactor has three components: A, B and I (an inert compound). The flow rates of A and B into the reactor are 0.01 mol A/s and 0.03 mol B/s. Additional information for this reactor is given below: A com Rate constant, KA Universal Clas Law Constant a) Construct a stoichiometric table for the above process. Imbas chang Reming FA. C Total molar flowrate Volen torre Total flowrate into the reactor, V₂. B I C 3 FA O O Fr -0.3716 mol/s V-0.002 m/s -0.001, 3 FAX -FA₂ m mol A kgcats mol B R-8.314 Pa m³/mol K) FA (1-x) F^ (@8 - x) -FA0 O 0.5 1²- (0·001) = 0·03 €-$₂S = Y P 0.33* K RT 8.314 =0.365 b) Estimate the volume of reactor required to achieve XA=0.75 assuming that the reactants are dilute.

430 The gas phase reaction, A+ 3B-C, has a rate that is 1/2 order in A and 1/2 order in B. This reaction is to be carried out isothermally at 55°C ad isobariclly at 506.625 Pa in a plug flow reactor. The gas stream entering the reactor has three components: A, B and I (an inert compound). The flow rates of A and B into the reactor are 0.01 mol A/s and 0.03 mol B/s. Additional information for this reactor is given below: A com Rate constant, KA Universal Clas Law Constant a) Construct a stoichiometric table for the above process. Imbas chang Reming FA. C Total molar flowrate Volen torre Total flowrate into the reactor, V₂. B I C 3 FA O O Fr -0.3716 mol/s V-0.002 m/s -0.001, 3 FAX -FA₂ m mol A kgcats mol B R-8.314 Pa m³/mol K) FA (1-x) F^ (@8 - x) -FA0 O 0.5 1²- (0·001) = 0·03 €-$₂S = Y P 0.33* K RT 8.314 =0.365 b) Estimate the volume of reactor required to achieve XA=0.75 assuming that the reactants are dilute.

Chemistry

10th Edition

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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