CHE 611 Advanced Chemical Reaction Engineering

Similar documents
CHE 611 Advanced Chemical Reaction Engineering

CHE 611 Advanced Chemical Reaction Engineering

CHE 611 Advanced Chemical Reaction Engineering

NPTEL. Chemical Reaction Engineering II - Video course. Chemical Engineering. COURSE OUTLINE

ChE 140B Chemical Reaction Engineering

Fundamentals of Heat Transfer Muhammad Rashid Usman

NPTEL. Chemical Reaction Engineering 2 (Heterogeneous Reactors) - Video course. Chemical Engineering.

Fundamentals of Heat Transfer Muhammad Rashid Usman

Class Schedule: Class will meet on TU/TH 11:30 AM - 12:45PM (Physics 107).

NPTEL. Chemical Reaction Engineering 1 (Homogeneous Reactors) - Video course. Chemical Engineering.

1. Usman, M.R Comprehensive Dictionary of Chemical Engineering. Lulu Publishing.

CHE 611 Advanced Chemical Reaction Engineering

A Shrinking Core Model for Steam Hydration of CaO-Based Sorbents Cycled for CO2 Capture: Supplementary Information

Thermodynamics and Rate Processes. D.Kunzru Dept. of Chemical Engineering I.I.T.Kanpur

Introduction to the course ``Theory and Development of Reactive Systems'' (Chemical Reaction Engineering - I)

16:375:527 Spring Semeter Physicochemical Process Dynamics in Environmental Systems

CHE 717, Chemical Reaction Engineering, Fall 2016 COURSE SYLLABUS

Research Article Dehydrogenation of Methylcyclohexane: Parametric Sensitivity of the Power Law Kinetics

Mass Transfer with Chemical Reactions in Porous Catalysts: A Discussion on the Criteria for the Internal and External Diffusion Limitations

Chemical Reaction Engineering (CRE) Education: From the Era of Slide Rule to the Digital Age

University School of Chemical Technology

ERQ - Chemical Reaction Engineering

AUTOMOTIVE EXHAUST AFTERTREATMENT

CHEMICAL ENGINEEERING AND CHEMICAL PROCESS TECHNOLOGY Vol. III - Ideal Models Of Reactors - A. Burghardt

Review Paper Modeling and Simulation Study of the CSTR for Complex Reaction by Using Polymath

Department of Chemical Engineering. Year 3 Module Synopses

BIRLA INSTITUTE OF TECHNOLOGY AND SCIENCE, Pilani Pilani Campus

Review for Final Exam. 1ChE Reactive Process Engineering

Modeling of the Unsteady State Methanol Synthesis at the Level of Catalyst Pellet

240EQ021 - Catalysis and Advanced Reactor Design

Examination paper for TKP 4155 / KP 8903 REACTION KINETICS AND CATALYSIS

Module 1: Mole Balances, Conversion & Reactor Sizing (Chapters 1 and 2, Fogler)

COPYRIGHTED MATERIAL OVERVIEW OF CHEMICAL REACTION ENGINEERING*

Chemical Reactor flnolysis

Evaluation of diffusional resistances in the process of glucose isomerization to fructose by immobilized glucose isomerase

Introduction to Catalysis (CME 425) & Heterogeneous Catalysis & Surface Reaction (CME522)

Novel Jet-loop Reactor for Kinetic Measurements of Gas-Solid Heterogeneous Catalyzed Reactions Involving Commercial-Scale Particles

Document Version Publisher s PDF, also known as Version of Record (includes final page, issue and volume numbers)

University School of Chemical Technology

Synthesis of Ethylene Glycol Evaluation of Standard Process and Possible Alternatives

Chemical Reaction Engineering. Lecture 2

Minimization of Exergy Destruction Costs for the Production of Hydrogen from Methane Cracking

A First Course on Kinetics and Reaction Engineering Unit 2. Reaction Thermochemistry

Effects of Different Processing Parameters on Divinylbenzene (DVB) Production Rate

Appendix A Course Syllabi Appendix A: Syllabi. Engineering Physics. Bachelor of Science in Engineering Physics. Self-Study Report

Title of the Dissertation

Fundamentals of Heat Transfer Muhammad Rashid Usman

Kinetics of the Fischer-Tropsch Reaction over a Ru- Promoted Co/Al 2 o 3 Catalyst

Engineering and. Tapio Salmi Abo Akademi Abo-Turku, Finland. Jyri-Pekka Mikkola. Umea University, Umea, Sweden. Johan Warna.

Name of Course: B.Tech. (Chemical Technology/Leather Technology)

Review of Chemical Equilibrium Introduction

The Catalytic Pellet: A Very Useful Environment for Engineering Scaling

The Title of an Article

The Title of an Article

Review of Chemical Equilibrium Introduction

Notes on reaction-diffusion cases with effectiveness factors greater than one! Richard K. Herz,

Chemical Reaction Engineering

The Title of an Article

PHEN 612 SPRING 2008 WEEK 1 LAURENT SIMON

INTRODUCTION TO CATALYTIC COMBUSTION

CHEMICAL REACTION ENGINEERING

SRI VENKATESWARA COLLEGE OF ENGINEERING. Department of Chemical Engineering

CBE 400 and 459 RESERVE BOOKS

Use of Differential Equations In Modeling and Simulation of CSTR

Development and Validation of a multi-site kinetic model for NH 3 -SCR over Cu-SSZ-13. Rohil Daya Isuzu Technical Center of America

Elsevier Preprint Document

Chemical Reaction Engineering, 2nd Edition By Octave Levenspiel READ ONLINE

Modeling of Fischer-Tropsch Product Distribution over Fe-based Catalyst

ERQQ - Chemical Reaction Engineering

Sample Journal of Economic Theory. Document

Bimetallic ruthenium-copper nanoparticles embedded in. mesoporous carbon as an effective hydrogenation catalyst

Analysis and Characterization of Fischer-Tropsch Products through Thermodynamic Equilibrium using Global Optimization Techniques

Solvent-Free Iridium-Catalyzed. Kinetic Modeling

Chemical Reactions and Chemical Reactors

Adsorption and Catalysis. Radha V Jayaram Institute of Chemical Technology, Mumbai

Introductory Chemical Engineering Thermodynamics 2nd Edition Elliot Solutions Manual

Fuel Cells in Energy Technology. Tutorial 5 / SS solutions. Prof. W. Schindler, Jassen Brumbarov / Celine Rüdiger

Chemical Sl.No Subject Code Name of the Subject

American Economic Review (Similar)

Unit 12: Chemical Kinetics

Fluid Flow Analysis Penn State Chemical Engineering

Ramasamy Kandasamy Department of Mathematics, Institute of Road and Transport Technology Erode , India kandan

Chemical Reaction Engineering - Part 7 Richard K. Herz,

Lecture 5. Solid surface: Adsorption and Catalysis

REFERENCE TEXTBOOKS MATERIAL AND ENERGY BALANCE: THERMODYNAMICS: TRANSPORT: KINETICS AND REACTOR DESIGN:

Studies on flow through and around a porous permeable sphere: II. Heat Transfer

PHYS100 General Physics - Mechanics and Thermodynamics Fall

The Seeding of Methane Oxidation

Kinetic modeling of pure hydrogen production from decalin

CHAPTER 80 NUMERICAL METHODS FOR FIRST-ORDER DIFFERENTIAL EQUATIONS

SAMPLE CHAPTERS UNESCO EOLSS ENVIRONMENTAL GEOCHEMISTRY. Peggy A. O Day Arizona State University, Tempe, AZ, USA

A Compact Reactor-Pump-Cell-Injection System for In-Situ / On- Line Spectroscopic Studies

Role of Re and Ru in Re Ru/C Bimetallic Catalysts for the

The material in this ebook also appears in the print version of this title: X.

Fluid mechanics MFKGT710005

MODELING AND SIMULATION OF REFORMER AUTO- THERMAL REACTOR IN AMMONIA UNIT

Nanoscale Materials and Their Properties Teacher Guide Unit 2: Metallic and Ionic Nanoparticle

Teaching Nanoscale Transport Phenomena

University School of Chemical Technology

What is "In" and What is "Out" in Engineering Problem Solving

Transcription:

CHE 611 Advanced Chemical Reaction Engineering Dr. Muhammad Rashid Usman Institute of Chemical Engineering and Technology University of the Punjab, Lahore 54590 mrusman.icet@pu.edu.pk 1

Development of kinetic rate equation based on LHHW dual-site surface reaction for the dehydrogenation of methylcyclohexane 2

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 3

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 4

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 5

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 6

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 7

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 8

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 9

Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 10

Homework problems For the simple mechanisms given previously in Part 7 (slide 16), work out the rate equations by considering adsorption, surface reaction, and desorption as the rate controlling step. For the Eley-Rideal mechanism, workout the rate equation for the surface reaction. 11

Homework problems Modify the mechanism given in slide 2, develop a kinetic rate equation based on LHHW kinetics when the rate controlling step is: Adsorption of methylcyclohexane Single-site surface reaction for the loss of first hydrogen Single-site surface reaction for the loss of second hydrogen Single-site surface reaction for the loss of third hydrogen Desorption of toluene Consult Chapter 10 of Fogler [2]. See also Chapter 2 of Froment et al. [1]. 12

Homework problems Modify the mechanism given in slide 2 for single-site surface reaction while neglecting hydrogen adsorption-desorption step. Develop kinetic rate equation based on LHHW kinetics when the rate controlling step is: Adsorption of methylcyclohexane Single-site surface reaction for the loss of first hydrogen Single-site surface reaction for the loss of second hydrogen Single-site surface reaction for the loss of third hydrogen Desorption of toluene Consult Chapter 10 of Fogler [2]. See also Chapter 2 of Froment et 13 al. [1].

Problem: Finding weight of catalyst 14

Problem: Finding weight of catalyst 15

Homework problem Using POLYMATH software find out the weight of the catalyst for the problem described above, however, use the rate equation as described in Usman et al. 2011 [6]. Solve the problem and see the difference for using two different rate equations. What are your comments? Instead of using POLYMATH software, you can prepare an excel spreadsheet using Euler s method or Runge-Kutta method for finding the weight of the catalyst, etc. 16

References [1] Froment, G.F., Bischoff, K.B., and De Wilde, J. 2011. Chemical reactor analysis and design. 3 rd ed. John Wiley & Sons, Inc. [2] Fogler, H.S. 1999. Elements of chemical reaction engineering. 3 rd ed. Prentice-Hall. [3] Levenspiel, O. 1999. Chemical reaction engineering. 3 rd ed. Wiley & Sons, Inc., Singapore. [4] Catalysis looks to the future. 1992. Panel on New Directions in Catalytic Science and Technology, National Research Council, National Academy Press, Washington, D.C. [5] Usman, M.R. 2011. Catalytic Dehydrogenation of Methylcyclohexane over Monometallic Catalysts for On-board Hydrogen Storage, Production, and Utilization. Energy Sources A 33, 2231 2238. [6] Usman, M.R.; Aslam, R.; Alotaibi, F. 2011. Hydrogen storage in a recyclable organic hydride: Kinetic modeling of methylcyclohexane dehyrogenation over 1.0 wt% Pt/θalumina. Energy Sources, Part A 33, 2264 2271. [7] Yaws, C.L. 1999. Chemical properties handbook. McGraw-Hill. [8] Bird, R.B. Stewart, W.E. Lightfoot, E.N. (2002). Transport phenomena. 2 nd ed. John Wiley & Sons, Inc. Singapore. [9] Poling, B.E.; Prausnitz, J.H.; O Connell, J.P. 2000. The properties of gases and liquids. 5 th ed. McGraw-Hill. [10] Missen, R.W., Mims, C.A., and Saville, B.A. 1999. Introduction to chemical reaction engineering and kinetics. John Wiley & Sons, Inc., New York. [11] Satterfield, C.N.1970. Mass transfer in heterogeneous catalysis. MIT Press. 17