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3.1, The rate of a heterogeneous reaction was measured in a rotating basket reactor. The volume of the basket was 100 mL and it was filled with 240 g of catalytic particles whose specific surface area was 9.5 m/g of Sbcript I indicates simple problems that require application of equations provided in the teAL 2 ndicates problems whose solutions require some more in-depth analysis and modificauon pen equations. Subscript 3 indicates problems whose solutions require more comprenenoshe and involve application of several concepts. Subscript 4 indicates problems that requine ee da mathematical software or the writing of a computer code to obtain numerical solutions.

3.1, The rate of a heterogeneous reaction was measured in a rotating basket reactor. The volume of the basket was 100 mL and it was filled with 240 g of catalytic particles whose specific surface area was 9.5 m/g of Sbcript I indicates simple problems that require application of equations provided in the teAL 2 ndicates problems whose solutions require some more in-depth analysis and modificauon pen equations. Subscript 3 indicates problems whose solutions require more comprenenoshe and involve application of several concepts. Subscript 4 indicates problems that requine ee da mathematical software or the writing of a computer code to obtain numerical solutions.

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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d pen equations. Subscript 3 indicates problems whose solutions require more comprehensive wwof a mathematical software or the writing of a computer code to obtain numerical solutions. ays and involve application of several concepts. Subscript 4 indicates problems that require the PROBLEMS* 3.1 The rate of a heterogeneous reaction was measured in a rotating basket reactor. The volume of the basket was 100 mL and it was filled with 240 g of catalytic particles whose specific surface area was 9.5 m/g of Scipt I indicates simple problems that require application of equations provided in the text. enpt 2 mdicates problems whose solutions require some more in-depth analysis and modincaton
Transcribed Image Text:d pen equations. Subscript 3 indicates problems whose solutions require more comprehensive wwof a mathematical software or the writing of a computer code to obtain numerical solutions. ays and involve application of several concepts. Subscript 4 indicates problems that require the PROBLEMS* 3.1 The rate of a heterogeneous reaction was measured in a rotating basket reactor. The volume of the basket was 100 mL and it was filled with 240 g of catalytic particles whose specific surface area was 9.5 m/g of Scipt I indicates simple problems that require application of equations provided in the text. enpt 2 mdicates problems whose solutions require some more in-depth analysis and modincaton
98 CHEMICAL KINETICS catalyst. At 100°C, the measured volume-based reaction rate constant was 2.5 s. Determine: a. The order of the reaction, based on the units of the reaction rate constant b. The mass-based rate constant c. The surface-based rate constant
Transcribed Image Text:98 CHEMICAL KINETICS catalyst. At 100°C, the measured volume-based reaction rate constant was 2.5 s. Determine: a. The order of the reaction, based on the units of the reaction rate constant b. The mass-based rate constant c. The surface-based rate constant
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