CHE 611 Advanced Chemical Reaction Engineering
|
|
|
- Anastasia Scott
- 5 years ago
- Views:
Transcription
1 CHE 611 Advanced Chemical Reaction Engineering Dr. Muhammad Rashid Usman Institute of Chemical Engineering and Technology University of the Punjab, Lahore
2 Development of kinetic rate equation based on LHHW dual-site surface reaction for the dehydrogenation of methylcyclohexane 2
3 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 3
4 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 4
5 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 5
6 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 6
7 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 7
8 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 8
9 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 9
10 Development of kinetic rate equation based on dual-site surface reaction for the dehydrogenation of methylcyclohexane 10
11 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
12 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
13 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].
14 Problem: Finding weight of catalyst 14
15 Problem: Finding weight of catalyst 15
16 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 [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
17 References [1] Froment, G.F., Bischoff, K.B., and De Wilde, J Chemical reactor analysis and design. 3 rd ed. John Wiley & Sons, Inc. [2] Fogler, H.S Elements of chemical reaction engineering. 3 rd ed. Prentice-Hall. [3] Levenspiel, O Chemical reaction engineering. 3 rd ed. Wiley & Sons, Inc., Singapore. [4] Catalysis looks to the future Panel on New Directions in Catalytic Science and Technology, National Research Council, National Academy Press, Washington, D.C. [5] Usman, M.R Catalytic Dehydrogenation of Methylcyclohexane over Monometallic Catalysts for On-board Hydrogen Storage, Production, and Utilization. Energy Sources A 33, [6] Usman, M.R.; Aslam, R.; Alotaibi, F Hydrogen storage in a recyclable organic hydride: Kinetic modeling of methylcyclohexane dehyrogenation over 1.0 wt% Pt/θalumina. Energy Sources, Part A 33, [7] Yaws, C.L 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 The properties of gases and liquids. 5 th ed. McGraw-Hill. [10] Missen, R.W., Mims, C.A., and Saville, B.A Introduction to chemical reaction engineering and kinetics. John Wiley & Sons, Inc., New York. [11] Satterfield, C.N Mass transfer in heterogeneous catalysis. MIT Press. 17
CHE 611 Advanced Chemical Reaction Engineering
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 Diffusion and reaction
CHE 611 Advanced Chemical Reaction Engineering
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 Course contents
CHE 611 Advanced Chemical Reaction Engineering
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 Advanced Chemical
NPTEL. Chemical Reaction Engineering II - Video course. Chemical Engineering. COURSE OUTLINE
NPTEL Syllabus Chemical Reaction Engineering II - Video course COURSE OUTLINE This is a typical second course in the subject of chemical reaction engineering with an emphasis on heterogeneous reaction
ChE 140B Chemical Reaction Engineering
http://www.chemengr.ucsb.edu/~ceweb/courses/che140b/index.html Enrollment code: 05173 Meeting Time: Tuesdays, Thursdays 9:30 10:45 a.m. Engineering 2, Room 1519 Instructor: Professor Brad Chmelka Office:
Fundamentals of Heat Transfer Muhammad Rashid Usman
Fundamentals of Heat Transfer Muhammad Rashid Usman Institute of Chemical Engineering and Technology University of the Punjab, Lahore. Figure taken from: http://heatexchanger-design.com/2011/10/06/heat-exchangers-6/
NPTEL. Chemical Reaction Engineering 2 (Heterogeneous Reactors) - Video course. Chemical Engineering.
NPTEL Syllabus Chemical Reaction Engineering 2 (Heterogeneous Reactors) - Video course COURSE OUTLINE In simple terms, Chemical Engineering deals with the production of a variety of chemicals on large
Fundamentals of Heat Transfer Muhammad Rashid Usman
Fundamentals of Heat Transfer Muhammad Rashid Usman Institute of Chemical Engineering and Technology University of the Punjab, Lahore. Figure taken from: http://heatexchanger-design.com/2011/10/06/heat-exchangers-6/
Class Schedule: Class will meet on TU/TH 11:30 AM - 12:45PM (Physics 107).
ENCH 640 Advanced Chemical Reaction Kinetics Instructor: Dr. Peng Xu (pengxu@umbc.edu) Assistant Professor, Chemical, Biochemical and Environmental Engineering, Office: Engineering 323 Phone: 410-455-2474
NPTEL. Chemical Reaction Engineering 1 (Homogeneous Reactors) - Video course. Chemical Engineering.
NPTEL Syllabus Chemical Reaction Engineering 1 (Homogeneous Reactors) - Video course COURSE OUTLINE In simple terms, Chemical Engineering deals with the production of a variety of chemicals on large scale.
1. Usman, M.R Comprehensive Dictionary of Chemical Engineering. Lulu Publishing.
Muhammad Rashid Usman, PhD Associate Professor Institute of Chemical Engineering and Technology University of the Punjab, New Campus, Lahore-54590, Pakistan. Phone: +92 (0) 42 99234062, Fax: +92 (0) 42
CHE 611 Advanced Chemical Reaction Engineering
CHE 611 Advanced Chemical Reaction Engineering Muhammad Rashid Usman, PhD Feb, 2016 Institute of Chemical Engineering and Technology University of the Punjab, Lahore 54590 mrusman.icet@pu.edu.pk 1 Course
A Shrinking Core Model for Steam Hydration of CaO-Based Sorbents Cycled for CO2 Capture: Supplementary Information
A Shrinking Core Model for Steam Hydration of CaO-Based Sorbents Cycled for CO2 Capture: Supplementary Information John Blamey 1, Ming Zhao 2, Vasilije Manovic 3, Edward J. Anthony 3, Denis R. Dugwell
Thermodynamics and Rate Processes. D.Kunzru Dept. of Chemical Engineering I.I.T.Kanpur
Thermodynamics and Rate Processes D.Kunzru Dept. of Chemical Engineering I.I.T.Kanpur Importance of Chemical Reaction Engineering chemical reactor is usually the heart of any process traditional applications:
Introduction to the course ``Theory and Development of Reactive Systems'' (Chemical Reaction Engineering - I)
Introduction to the course ``Theory and Development of Reactive Systems'' (Chemical Reaction Engineering - I) Prof. Gabriele Pannocchia Department of Civil and Industrial Engineering (DICI) University
16:375:527 Spring Semeter Physicochemical Process Dynamics in Environmental Systems
16:375:527 Spring Semeter Physicochemical Process Dynamics in Environmental Systems Instructor: Professor Weilin Huang whuang@envsci.rutgers.edu Description: This course covers fundamentals of process
CHE 717, Chemical Reaction Engineering, Fall 2016 COURSE SYLLABUS
Page 1 of 5 CHE 717, Chemical Reaction Engineering, Fall 2016 COURSE SYLLABUS engineeringonline.ncsu.edu/onlinecourses/coursehomepages/fall-2016/che717.html Instructor: Prof. Jason Haugh 3100 Partners
Research Article Dehydrogenation of Methylcyclohexane: Parametric Sensitivity of the Power Law Kinetics
ISRN Chemical Engineering Volume 2013, Article ID 152893, 8 pages http://dx.doi.org/10.1155/2013/152893 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
Defect and Diffusion Forum Online: 03-0-3 ISSN: 66-9507, Vols. 334-335, pp 79-83 doi:0.408/www.scientific.net/ddf.334-335.79 03 Trans Tech Publications, Switzerland Mass Transfer with Chemical Reactions
Chemical Reaction Engineering (CRE) Education: From the Era of Slide Rule to the Digital Age
Chemical Reaction Engineering (CRE) Education: From the Era of Slide Rule to the Digital Age H. Scott Fogler, University of Michigan Michael B. Cutlip, University of Connecticut Abstract The complexity
University School of Chemical Technology
University School of Chemical Technology Guru Gobind Singh Indraprastha University Syllabus of Examination B.Tech/M.Tech Dual Degree (Chemical Engineering) (6 th Semester) (w.e.f. August 2004 Batch) Page
ERQ - Chemical Reaction Engineering
Coordinating unit: 205 - ESEIAAT - Terrassa School of Industrial, Aerospace and Audiovisual Engineering Teaching unit: 713 - EQ - Department of Chemical Engineering Academic year: Degree: 2017 BACHELOR'S
AUTOMOTIVE EXHAUST AFTERTREATMENT
AUTOMOTIVE EXHAUST AFTERTREATMENT CATALYST FUNDAMENTLS Catalyst in its simplest term is a material that increase the rate (molecules converted by unit time) of a chemical reaction while itself not undergoing
CHEMICAL ENGINEEERING AND CHEMICAL PROCESS TECHNOLOGY Vol. III - Ideal Models Of Reactors - A. Burghardt
IDEAL MODELS OF REACTORS A. Institute of Chemical Engineering, Polish Academy of Sciences, Poland Keywords: Thermodynamic state, conversion degree, extent of reaction, classification of chemical reactors,
Review Paper Modeling and Simulation Study of the CSTR for Complex Reaction by Using Polymath
Research Journal of Chemical Sciences ISSN 2231-606X. Review Paper Modeling and Simulation Study of the CSTR for Complex Reaction by Using Polymath Abstract Kanse Nitin G. 1, Dhanke P.B. 1 and Thombare
Department of Chemical Engineering. Year 3 Module Synopses
Department of Chemical Engineering Year 3 Module Synopses CENG301P Process Plant Design Project (1.0cu) CENG302P Process Dynamics & Control CENG303P Chemical Reaction Engineering CENG304P Transport Phenomena
BIRLA INSTITUTE OF TECHNOLOGY AND SCIENCE, Pilani Pilani Campus
First Semester 2017-2018 Instruction Division Course Handout (Part II) Date: 02/08/2017 In addition to Part I (General Handout for all courses appended to the Time Table), this portion gives further specific
Review for Final Exam. 1ChE Reactive Process Engineering
Review for Final Exam 1ChE 400 - Reactive Process Engineering 2ChE 400 - Reactive Process Engineering Stoichiometry Coefficients Numbers Multiple reactions Reaction rate definitions Rate laws, reaction
Modeling of the Unsteady State Methanol Synthesis at the Level of Catalyst Pellet
Modeling of the Unsteady State Methanol Synthesis at the Level of Catalyst Pellet IONUT BANU, IOANA STOICA, GHEORGHE BUMBAC, GRIGORE BOZGA* University Politehnica of Bucharest, Department of Chemical and
240EQ021 - Catalysis and Advanced Reactor Design
Coordinating unit: Teaching unit: Academic year: Degree: ECTS credits: 2018 295 - EEBE - Barcelona East School of Engineering 713 - EQ - Department of Chemical Engineering MASTER'S DEGREE IN CHEMICAL ENGINEERING
Examination paper for TKP 4155 / KP 8903 REACTION KINETICS AND CATALYSIS
Department of Chemical Engineering Examination paper for TKP 4155 / KP 8903 REACTION KINETICS AND CATALYSIS Academic contact during examination: Professor Magnus Rønning Phone: 918 97 585 Examination date:
Module 1: Mole Balances, Conversion & Reactor Sizing (Chapters 1 and 2, Fogler)
CHE 309: Chemical Reaction Engineering Lecture-2 Module 1: Mole Balances, Conversion & Reactor Sizing (Chapters 1 and 2, Fogler) Module 1: Mole Balances, Conversion & Reactor Sizing Topics to be covered
COPYRIGHTED MATERIAL OVERVIEW OF CHEMICAL REACTION ENGINEERING*
1 OVERVIEW OF CHEMICAL REACTION ENGINEERING* Chemical reaction engineering (CRE) is the branch of engineering that encompasses the selection, design, and operation of chemical reactors. Because of the
Chemical Reactor flnolysis
Introduction to Chemical Reactor flnolysis SECOND EDITION R.E. Hayes J.P. Mmbaga ^ ^ T..,«,,.«M.iirti,im.' TECHNISCHE INFORMATIONSBIBLIOTHEK UNWERSITATSBIBLIOTHEK HANNOVER i ii ii 1 J /0\ CRC Press ycf*
Evaluation of diffusional resistances in the process of glucose isomerization to fructose by immobilized glucose isomerase
Enzyme and Microbial Technology 28 (2001) 246 252 www.elsevier.com/locate/enzmictec 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)
Introduction to Catalysis (CME 425) & Heterogeneous Catalysis & Surface Reaction (CME522) Text book: Julian R.H. Ross, Heterogeneous Catalysis: Fundamentals and Applications, 2011, Elsevier Publications,
Novel Jet-loop Reactor for Kinetic Measurements of Gas-Solid Heterogeneous Catalyzed Reactions Involving Commercial-Scale Particles
Novel Jet-loop Reactor for Kinetic Measurements of Gas-Solid Heterogeneous Catalyzed Reactions Involving Commercial-Scale Particles Anuradha Nagaraj Department of Environmental Engineering Texas A&M University-Kingsville
Document Version Publisher s PDF, also known as Version of Record (includes final page, issue and volume numbers)
On the temperature dependence of the Arrhenius activation energy for hydroisomerization catalyzed by Pt/Mordenite Runstraat, van de, A.; van Grondelle, J.; van Santen, R.A. Published in: Journal of Catalysis
University School of Chemical Technology
University School of Chemical Technology Guru Gobind Singh Indraprastha University Syllabus of Examination B.Tech/M.Tech Dual Degree (Chemical Engineering) (5 th Semester) (w.e.f. August 2004 Batch) Page
Synthesis of Ethylene Glycol Evaluation of Standard Process and Possible Alternatives
Synthesis of Ethylene Glycol Evaluation of Standard Process and Possible Alternatives Miles Beamguard September 4, 2001 Ethylene glycol, a clear, colorless, odorless liquid, is typically synthesized through
Chemical Reaction Engineering. Lecture 2
hemical Reaction Engineering Lecture 2 General algorithm of hemical Reaction Engineering Mole balance Rate laws Stoichiometry Energy balance ombine and Solve lassification of reactions Phases involved:
Minimization of Exergy Destruction Costs for the Production of Hydrogen from Methane Cracking
Minimization of Exergy Destruction Costs for the Production of Hydrogen from Methane Cracking Federico Gutiérrez, Federico Méndez. Abstract In the present work, the conservation principles (energy and
A First Course on Kinetics and Reaction Engineering Unit 2. Reaction Thermochemistry
Unit 2. Reaction Thermochemistry Overview This course is divided into four parts, I through IV. Part I reviews some topics related to chemical reactions that most students will have encountered in previous
Effects of Different Processing Parameters on Divinylbenzene (DVB) Production Rate
1 Effects of Different Processing Parameters on Divinylbenzene (DVB) Production Rate ME Zeynali Petrochemical Synthesis Group, Petrochemical Faculty, Iran Polymer and Petrochemical Institute (IPPI), P.O.
Appendix A Course Syllabi Appendix A: Syllabi. Engineering Physics. Bachelor of Science in Engineering Physics. Self-Study Report
Appendix A Course Syllabi Appendix A: Syllabi Engineering Physics Bachelor of Science in Engineering Physics Self-Study Report New Mexico State University 159 Chemical Engineering Courses Chemical Engineering
Title of the Dissertation
NORTHWESTERN UNIVERSITY Title of the Dissertation A DISSERTATION SUBMITTED TO THE GRADUATE SCHOOL IN PARTIAL FULFILLMENT OF THE REQUIREMENTS for the degree DOCTOR OF PHILOSOPHY Field of Mathematics By
Fundamentals of Heat Transfer Muhammad Rashid Usman
Fundamentals of Heat Transfer Muammad Rasid Usman Institute of Cemical Engineering and Tecnology University of te Punjab, Laore. Figure taken from: ttp://eatexcanger-design.com/20/0/06/eat-excangers-6/
Kinetics of the Fischer-Tropsch Reaction over a Ru- Promoted Co/Al 2 o 3 Catalyst
Kinetics of the Fischer-Tropsch Reaction over a Ru- Promoted Co/Al o 3 Catalyst Tejas Bhatelia 1, Wenping Ma, Burtron Davis, Gary Jacobs and Dragomir Bukur 1* 1 Department of Chemical Engineering, Texas
Engineering and. Tapio Salmi Abo Akademi Abo-Turku, Finland. Jyri-Pekka Mikkola. Umea University, Umea, Sweden. Johan Warna.
Chemical Reaction Engineering and Reactor Technology Tapio Salmi Abo Akademi Abo-Turku, Finland Jyri-Pekka Mikkola Umea University, Umea, Sweden Johan Warna Abo Akademi Abo-Turku, Finland CRC Press is
Name of Course: B.Tech. (Chemical Technology/Leather Technology)
Name of : B.Tech. (Chemical Technology/Leather Technology) Harcourt Butler Technological Institute, Kanpur Study and [Effective from the Session 201-1] B. Tech. (Chemical Technology/Leather Technology)
Review of Chemical Equilibrium Introduction
Review of Chemical Equilibrium Introduction Copyright c 2015 by Nob Hill Publishing, LLC This chapter is a review of the equilibrium state of a system that can undergo chemical reaction Operating reactors
The Catalytic Pellet: A Very Useful Environment for Engineering Scaling
The Catalytic Pellet: Very Useful Environment for Engineering Scaling Stephen Whitaker 1, Pedro E. rce bstract This contribution focuses on the scaling aspects in the learning of catalytic reactions in
The Title of an Article
The Title of an Article Dr. Author Jones University of Somewhere Abstract This article illustrates many features of a mathematics article, but we do not explain the spurious appearance of the formula (
The Title of an Article
The Title of an Article Dr. Author Jones 1 At this Address City, State 12345-6789 1 Sample Mathematics and Text This short sample document illustrates the typeset appearance of in-line and displayed mathematics
Review of Chemical Equilibrium Introduction
Review of Chemical Equilibrium Introduction Copyright c 2015 by Nob Hill Publishing, LLC This chapter is a review of the equilibrium state of a system that can undergo chemical reaction Operating reactors
Notes on reaction-diffusion cases with effectiveness factors greater than one! Richard K. Herz,
Notes on reaction-diffusion cases with effectiveness factors greater than one! Richard K. Herz, rherz@ucsd.edu For isothermal n-th order reactions where n >= 0, the catalyst effectiveness factor value
Chemical Reaction Engineering
Chemical Reaction Engineering Dr. Yahia Alhamed Chemical and Materials Engineering Department College of Engineering King Abdulaziz University General Mole Balance Batch Reactor Mole Balance Constantly
The Title of an Article
The Title of an Article Dr. Author Jones At this Address May 2, 2006 Abstract This article illustrates many features of a mathematics article, but we do not explain the spurious appearance of the formula
PHEN 612 SPRING 2008 WEEK 1 LAURENT SIMON
PHEN 612 SPRING 2008 WEEK 1 LAURENT SIMON Chapter 1 * 1.1 Rate of reactions r A A+B->C Species A, B, and C We are interested in the rate of disappearance of A The rate of reaction, ra, is the number of
INTRODUCTION TO CATALYTIC COMBUSTION
INTRODUCTION TO CATALYTIC COMBUSTION R.E. Hayes Professor of Chemical Engineering Department of Chemical and Materials Engineering University of Alberta, Canada and S.T. Kolaczkowski Professor of Chemical
CHEMICAL REACTION ENGINEERING
CHEMICL RECTION ENGINEERING Unit 5 nalysis of reactor DT Collection and analysis of rate data Batch reactor for homogenous and heterogeneous reactions measurement during the unsteady-state operation Differential
SRI VENKATESWARA COLLEGE OF ENGINEERING. Department of Chemical Engineering
COURSE DELIVERY PLAN - THEORY Page 1 of 6 Department of Chemical Engineering B.Tech : Chemical Engineering Regulation: R - 2013 Sub. Code / Sub. Name : CH6403 Chemical Process Calculations Unit : I LP:
CBE 400 and 459 RESERVE BOOKS
RESERVE BOOKS Process and Product Design Seider, W. D., J. D. Seader, D. R. Lewin, and S. Widagdo, Product and Process Design Principles: Synthesis, Analysis, and Evaluation, Third Edition, Wiley, 2009.
Use of Differential Equations In Modeling and Simulation of CSTR
Use of Differential Equations In Modeling and Simulation of CSTR JIRI VOJTESEK, PETR DOSTAL Department of Process Control, Faculty of Applied Informatics Tomas Bata University in Zlin nám. T. G. Masaryka
Development and Validation of a multi-site kinetic model for NH 3 -SCR over Cu-SSZ-13. Rohil Daya Isuzu Technical Center of America
Development and Validation of a multi-site kinetic model for NH 3 -SCR over Cu-SSZ-13 Rohil Daya Isuzu Technical Center of America Introduction, Objective and Purpose Cu-CHA small pore SCR catalysts utilized
Elsevier Preprint Document
Elsevier Preprint Document A. U. Thor Institute of Far Away Places Additional Author Institute of Still Farther Away Places Abstract This article illustrates many features of a mathematics article, but
Chemical Reaction Engineering, 2nd Edition By Octave Levenspiel READ ONLINE
Chemical Reaction Engineering, 2nd Edition By Octave Levenspiel READ ONLINE Oct 27, 2016 Chemical Reaction Engineering Levenspiel Solution Reaction Engineering Levenspiel 2nd Edition chemical reaction
Modeling of Fischer-Tropsch Product Distribution over Fe-based Catalyst
793 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 32, 2013 Chief Editors: Sauro Pierucci, Jiří J. Klemeš Copyright 2013, AIDIC Servizi S.r.l., ISBN 978-88-95608-23-5; ISSN 1974-9791 The Italian
ERQQ - Chemical Reaction Engineering
Coordinating unit: Teaching unit: Academic year: Degree: ECTS credits: 2017 295 - EEBE - Barcelona East School of Engineering 713 - EQ - Department of Chemical Engineering BACHELOR'S DEGREE IN CHEMICAL
Sample Journal of Economic Theory. Document
Sample Journal of Economic Theory Document A. U. Thor Institute of Far Away Places Additional Author Institute of Still Farther Away Places Abstract We study the e ects of warm water on the local penguin
Bimetallic ruthenium-copper nanoparticles embedded in. mesoporous carbon as an effective hydrogenation catalyst
Supporting Information Bimetallic ruthenium-copper nanoparticles embedded in mesoporous carbon as an effective hydrogenation catalyst Jiajia Liu, *a Li Li Zhang, b Jiatao Zhang, a Tao Liu, c and X. S.
Analysis and Characterization of Fischer-Tropsch Products through Thermodynamic Equilibrium using Global Optimization Techniques
1669 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 57, 2017 Guest Editors: Sauro Pierucci, Jiří Jaromír Klemeš, Laura Piazza, Serafim Bakalis Copyright 2017, AIDIC Servizi S.r.l. ISBN 978-88-95608-48-8;
Solvent-Free Iridium-Catalyzed. Kinetic Modeling
Electronic Supplementary Material (ESI) for Catalysis Science & Technology. This journal is The Royal Society of Chemistry 2014 Supplementary Information Solvent-Free Iridium-Catalyzed Hydrosilylation
Chemical Reactions and Chemical Reactors
Chemical Reactions and Chemical Reactors George W. Roberts North Carolina State University Department of Chemical and Biomolecular Engineering WILEY John Wiley & Sons, Inc. x Contents 1. Reactions and
Adsorption and Catalysis. Radha V Jayaram Institute of Chemical Technology, Mumbai
Adsorption and Catalysis Radha V Jayaram Institute of Chemical Technology, Mumbai 1 2 Different solids would adsorb different amounts of the same gas even under similar conditions. Substances like charcoal
Introductory Chemical Engineering Thermodynamics 2nd Edition Elliot Solutions Manual
Introductory Chemical Engineering Thermodynamics 2nd Edition Elliot Solutions Manual Fundamentals of Engineering Thermodynamics Solutions Manual. chemical engineering thermodynamics 7th edition(solution
Fuel Cells in Energy Technology. Tutorial 5 / SS solutions. Prof. W. Schindler, Jassen Brumbarov / Celine Rüdiger
Fuel Cells in Energy Technology Tutorial 5 / SS 2013 - solutions Prof. W. Schindler, Jassen Brumbarov / Celine Rüdiger 05.06.2013 Homework 3: What hydrogen flow rate (g/hour) is required to generate 1
Chemical Sl.No Subject Code Name of the Subject
Chemical Sl.No Subject Code Name of the Subject 1 14PHDCH001 Transport Phenomena 2 14PHDCH002 Process Modeling and Simulation 3 14PHDCH003 Novel Separation Processes 4 14PHDCH004 Environmental Pollution
American Economic Review (Similar)
American Economic Review (Similar) A. U. Thor - Omit from submitted draft The University of Somewhere - Omit from submitted draft Abstract We study the e ects of warm water on the local penguin population.
Unit 12: Chemical Kinetics
Unit 12: Chemical Kinetics Author: S. Michalek Introductory Resources: Zumdahl v. 5 Chapter 12 Main Ideas: Integrated rate laws Half life reactions Reaction Mechanisms Model for chemical kinetics Catalysis
Fluid Flow Analysis Penn State Chemical Engineering
Fluid Flow Analysis Penn State Chemical Engineering Revised Spring 2015 Table of Contents LEARNING OBJECTIVES... 1 EXPERIMENTAL OBJECTIVES AND OVERVIEW... 1 PRE-LAB STUDY... 2 EXPERIMENTS IN THE LAB...
Ramasamy Kandasamy Department of Mathematics, Institute of Road and Transport Technology Erode , India kandan
Journal of Computational and Applied Mechanics, Vol. 6., No. 1., (2005), pp. 27 37 NONLINEAR HYDROMAGNETIC FLOW, HEAT AND MASS TRANSFER OVER AN ACCELERATING VERTICAL SURFACE WITH INTERNAL HEAT GENERATION
Chemical Reaction Engineering - Part 7 Richard K. Herz,
Chemical Reaction Engineering - Part 7 Richard K. Herz, rherz@ucsd.edu, www.reactorlab.net Methods of experimental data analysis So far we have been given rate equations and values of rate coefficients.
Lecture 5. Solid surface: Adsorption and Catalysis
Lecture 5 Solid surface: Adsorption and Catalysis Adsorbtion G = H T S DG ads should be negative (spontaneous process) DS ads is negative (reduced freedom) DH should be negative for adsorption processes
REFERENCE TEXTBOOKS MATERIAL AND ENERGY BALANCE: THERMODYNAMICS: TRANSPORT: KINETICS AND REACTOR DESIGN:
REFERENCE TEXTBOOKS MATERIAL AND ENERGY BALANCE: Elementary Principles of Chemical Processes, 4 th Edition - Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard THERMODYNAMICS: Introduction to Chemical
Studies on flow through and around a porous permeable sphere: II. Heat Transfer
Studies on flow through and around a porous permeable sphere: II. Heat Transfer A. K. Jain and S. Basu 1 Department of Chemical Engineering Indian Institute of Technology Delhi New Delhi 110016, India
PHYS100 General Physics - Mechanics and Thermodynamics Fall
PHYS100 General Physics - Mechanics and Thermodynamics Fall 2014-2015 Assoc. Prof. Dr. O. Özgür Eğilmez Civil Engineering Department Room: A-523 Email: ozgur.egilmez@ieu.edu.tr Phone: (232) 488-8214 Textbook:
The Seeding of Methane Oxidation
The Seeding of Methane Oxidation M. B. DAVIS and L. D. SCHMIDT* Department of Chemical Engineering and Materials Science, University of Minnesota, Minneapolis, MN 55455 USA Mixtures of light alkanes and
Kinetic modeling of pure hydrogen production from decalin
Journal of Catalysis 253 (2008) 229 238 www.elsevier.com/locate/jcat Kinetic modeling of pure hydrogen production from decalin Bo Wang a, D. Wayne Goodman a, Gilbert F. Froment b, a Department of Chemical
CHAPTER 80 NUMERICAL METHODS FOR FIRST-ORDER DIFFERENTIAL EQUATIONS
CHAPTER 8 NUMERICAL METHODS FOR FIRST-ORDER DIFFERENTIAL EQUATIONS EXERCISE 33 Page 834. Use Euler s method to obtain a numerical solution of the differential equation d d 3, with the initial conditions
SAMPLE CHAPTERS UNESCO EOLSS ENVIRONMENTAL GEOCHEMISTRY. Peggy A. O Day Arizona State University, Tempe, AZ, USA
ENVIRONMENTAL GEOCHEMISTRY Peggy A. O Day Arizona State University, Tempe, AZ, USA Keywords: environmental geochemistry, time and space scales, chemical principles, equilibrium thermodynamics. Kinetics
A Compact Reactor-Pump-Cell-Injection System for In-Situ / On- Line Spectroscopic Studies
A Compact Reactor-Pump-Cell-Injection System for In-Situ / On- Line Spectroscopic Studies Feng Gao, Li Chuanzhao and Marc Garland Department of Chemical and Biomolecular Engineering 4 Engineering Drive
Role of Re and Ru in Re Ru/C Bimetallic Catalysts for the
Role of Re and Ru in Re Ru/C Bimetallic Catalysts for the Aqueous Hydrogenation of Succinic Acid Xin Di a, Chuang Li a, Bingsen Zhang b, Ji Qi a, Wenzhen Li c, Dangsheng Su b, Changhai Liang a, * a Laboratory
The material in this ebook also appears in the print version of this title: X.
Copyright 2008, 997, 984, 973, 963, 950, 94, 934 by The McGraw-Hill Companies, Inc. All rights reserved. Manufactured in the United States of America. Except as permitted under the United States Copyright
Fluid mechanics MFKGT710005
Fluid mechanics MFKGT710005 MSc in Petroleum Engineering Full time course SUBJECT-MATTER COMMUNICATIONS DOSSIER UNIVERSITY OF MISKOLC FACULTY OF EARTH SCIENCE AND ENGINEERING INSTITUTE OF PETROLEUM AND
MODELING AND SIMULATION OF REFORMER AUTO- THERMAL REACTOR IN AMMONIA UNIT
Peet trool lleeuum & Cooaal ll IISSN 337-77 Available online at www.vuru.sk/c Petroleum & Coal 9 (), 6-7, 7 MODELING AND SIMULATION OF REFORMER AUTO- THERMAL REACTOR IN AMMONIA UNIT Kayvan Khorsand *,
Nanoscale Materials and Their Properties Teacher Guide Unit 2: Metallic and Ionic Nanoparticle
Nanoscale Materials and Their Properties Teacher Guide Unit 2: Metallic and Ionic Nanoparticles: Extendable Structures Objectives for Metallic and Ionic Nanoparticles: Extendable Structures Lesson Objectives:
Teaching Nanoscale Transport Phenomena
Teaching Nanoscale Transport Phenomena Pamela Norris Professor Department of Mechanical and Aerospace Engineering University of Virginia Charlottesville, VA 22902 VIRGINIA 1 UVa MAE 612 Microscale Heat
University School of Chemical Technology
University School of Chemical Technology Guru Gobind Singh Indraprastha University Syllabus of Examination B.Tech/M.Tech Dual Degree (Chemical Engineering) (7 th Semester) (w.e.f. August 2004 Batch) Page
What is "In" and What is "Out" in Engineering Problem Solving
18 th European Symposium on Computer Aided Process Engineering ESCAPE 18 Bertrand Braunschweig and avier Joulia (Editors) 008 Elsevier B.V./Ltd. All rights reserved. M. Shacham, M. B. Cutlip and N. Brauner,"What