Oxidative Coupling of Methane

Size: px
Start display at page:

Download "Oxidative Coupling of Methane"

Transcription

1 Oxidative Coupling of Methane Objective: Parameter Estimation for Methane to Ethylene reaction In this example, we build a simplified reaction network for the Oxidative Coupling of Methane (OCM) and estimate the kinetic parameters based on data from [1]. We start with a basic model and the model is refined sequentially to improve empirical accuracy. You may download the zip file containing the rex files analyzed next. Features Illustrated Building a Macro-kinetic Reaction Network Manipulation of weighting factors with automated procedures. Reaction Traffic tool used to compare the relative magnitude of reaction paths Reaction Model Oxidative Coupling of Methane is generally accepted as a combination of catalytic and gas-phase reactions. The reaction network for this system as shown in [1] is below: The complete model from [1] includes 50+ elementary reactions. Gas phase reactions include radical species and detailed microkinetics are considered for the reactions on the catalyst surface. While the detailed microkinetic model proposed in [1] can be formulated in REX using the Detailed Catalyst feature as shown here, we focus this example on building an empirical macrokinetic model. This model contains bulk species only: radicals and surface intermediates are not considered. The experimental data from from [1] are used for the kinetic estimation.

2 The reaction network consists of two path types: Formation of C 2 species from methane, indicated in blue in the image below. Oxidation of all species yielding CO x indicated in green: Setting up the first Mass Action Model (OCM-1.rex) In the Units Configuration node, the rate basis is selected to be Catalyst Mass; Partial Pressure is chosen for the concentration term in the rate expression. Other units selected are shown below: In the Compounds node, we define all the species. Optional information for atom counts may also be entered in the Compounds Formula node. All reactions are considered irreversible:

3 The compound orders are defined in node Chemistry Kinetics Parameters node for every reaction. We choose order=1 for all reactants in a reaction. Experimental Data The experiments are carried out in a fixed bed reactor (modeled as a PFR), where pressure and temperature are Interpolated from Data. Those specifications are defined in the Reactor node, where the gas flow is chosen as float so that it can be calculated by REX to match the pressure setpoint:

4 Experimental data retrieved from [1] covers the following effects: Methane and Oxygen conversion and product selectivities vs Space Time T=973K, P=110 kpa, CH 4 /O 2 feed = 3.0 W/F varying from 2 to 12 (kg s / mol) Methane and Oxygen conversion and product selectivities vs CH 4 /O 2 feed ratio T=1013K, P=130 kpa, W/F = 2.0 CH 4 /O 2 feed ratio varying from 2 to 12 Methane and Oxygen conversion vs CH 4 /O 2 feed ratio at different temperatures P=130 kpa, W/F = 2.0 Temperature values: 944K, 973K and 1013K The experimental data is available in the Experiments Measurements SetName nodes of the provided rex files.

5 Setting up the parameter estimation All reactions are selected as Estimate in Estimation node, and bounds are open in Estimation Parameters node for pre-exponential and activation energies. In the Weights node, we select all the compounds to be reconciled, except water. Hybrid weights are generated with the Ignore Zero option enabled. This ensures that the weights are kept at zero for the measurements whose experimental values are zero. When running this model, the total weighted Least Square Error (LSQ) for this model is around In order to have better scaling of the objective function, we increase all weights by a factor of This is done in the Advanced tab of the Weights node. First, we include all checkboxes, so that the change is done for all compounds and sets. A quick way to include all checkboxes in a column is by pointing to the column header, then using the right click mouse button and selecting the Check All option. For example for the CH4 column:

6 The same must be done for the other compound columns to have all checkboxes included. Another option is to include one checkbox, then copy this checkbox ( Ctrl-C works or by right click on the mouse) and paste the include flag to a region of checkboxes (Ctrl-V works). Once the required checkboxes are selected, the Multiply by Custom Weight option is chosen in the Modification Type combo. A factor of 1000 is entered in the Custom Weight box followed by the Apply button as shown below:

7 The OCM-1.rex file already includes this modification. A log with the changes done on the weights can be seen in the History tab on Weights node. Estimation Results After running the estimation model, we obtain the objective function to be 7.06.The parameter values from the solution are shown in the Results Parameters node:

8 You may note that several reactions have very small pre-exponential values with high activation energy. These reactions have negligible traffic and thus can be eliminated without affecting model predictions. We continue analyzing the model predictions by inspecting the parity plots in the Results Model-Data Comparison node:

9 As seen above, C 2 H 4 and C 2 H 6 predictions need to be improved. In OCM-2.rex, we try to see if increasing the C 2 H 4 weights by a factor of 10 (in the Advanced tab of the Weights node) can improve the fit. However, despite running the model with the increased weights, the C 2 H 4 parity plot shows no significant improvement:. Next, we try to optimize the compound orders for the reactions in OCM-3.rex. We initially had all orders fixed to one; now we open them between 0.5 and 2 in the Estimation Parameters node. This gives a better weighted LSQ value of The resulting parameters are below:

10 Some orders have hit their bounds. You may experiment with relaxing the bounds to see if further improvement can be obtained. In the final trial, we fix the orders close to the solution obtained from previous run. The orders are fixed to either 0.5, 1 or 2 by setting them closest to the optimal value. For example, reaction CH4-to- C2H6 will have orders fixed fo 0.5 for CH4 and for O2. We also un-include the reactions that have negligibly small rates: C2H6-to-CO2, C2H6-to-CO and C2H4-to-CO. They can be un-included from either the Chemistry Reactions or Chemistry Kinetics node; the latter is shown below and the corresponding rex file is OCM-4.rex:

11 This simplified model has a weighted LSQ of 3.72 which is slightly higher than the previous model with open bounds on the compound orders. The parameter values and resulting parity charts are shown next:

12 Comparing the previous parity results from OCM-1.rex file, we can see that C 2 H 4 match has improved, while all other compounds predictions remain reasonably good as before. The carbon traffic in Reaction Traffic node allows us to qualitatively compare the relative importance of the reaction paths in the resulting reaction network:

13 Further studies You may start from the mass action model in OCM-1.rex and add Langmuir Hinshelwood kinetics and compare these results with the model from OCM-4.rex. You may also build a first principles model based on the surface reactions by using the Detailed Catalyst model in REX. References 1. Sun, J., Thybaut, J.W., Marin, G.B., (2008) Microkinetics of Methane Oxidative Coupling. Catalysis Today, Vol 137,

Model for Propane Dehydrogenation

Model for Propane Dehydrogenation www.optience.com Model for Propane Dehydrogenation Objective: Develop a kinetic model for Propane Dehydrogenation In this example, we propose a simplified model for the catalytic dehydrogenation of propane

More information

Objective: To Evaluate Predictions of Alternative Models

Objective: To Evaluate Predictions of Alternative Models www.optience.com Methanol Synthesis Objective: To Evaluate Predictions of Alternative Models In this example, we propose and evaluate Mass Action and Langmuir Hinshelwood (LHHW) models for methanol synthesis

More information

Objective: To Estimate Kinetic Parameters for Toluene Reaction with Benzyl Alcohol

Objective: To Estimate Kinetic Parameters for Toluene Reaction with Benzyl Alcohol www.optience.com Toluene Benzylation Objective: To Estimate Kinetic Parameters for Toluene Reaction with Benzyl Alcohol In this example, an LHHW kinetic model for toluene reaction over solid catalyst in

More information

Propylene Hydroformylation

Propylene Hydroformylation www.optience.com Propylene Hydroformylation Objective: Building Fedbatch reactors with Pressure Control In this example, we simulate a multiphase batch reactor for Propylene Hydroformylation and also explain

More information

Polymerization Modeling

Polymerization Modeling www.optience.com Polymerization Modeling Objective: Modeling Condensation Polymerization by using Functional Groups In this example, we develop a kinetic model for condensation polymerization that tracks

More information

Exploring The Fundamentals In Catalytic Partial Oxidation Of Methane: The Interaction Between Diffusion And Reaction In A Packed Bed Reactor

Exploring The Fundamentals In Catalytic Partial Oxidation Of Methane: The Interaction Between Diffusion And Reaction In A Packed Bed Reactor Exploring The Fundamentals In Catalytic Partial Oxidation Of Methane: The Interaction Between Diffusion And Reaction In A Packed Bed Reactor Songjun Liu; Ana Obradović; Joris W. Thybaut; Guy B. Marin Laboratory

More information

(1) This reaction mechanism includes several undesired side reactions that produce toluene and benzene:

(1) This reaction mechanism includes several undesired side reactions that produce toluene and benzene: HYSYS Multiple Reactions - Styrene Prepared by Robert P. Hesketh Spring 005 Styrene Reactor System You have been studying how to use HYSYS using the example of a Styrene reactor system. In this session

More information

Reactors. Reaction Classifications

Reactors. Reaction Classifications Reactors Reactions are usually the heart of the chemical processes in which relatively cheap raw materials are converted to more economically favorable products. In other cases, reactions play essential

More information

Preparations and Starting the program

Preparations and Starting the program Preparations and Starting the program https://oldwww.abo.fi/fakultet/ookforskning 1) Create a working directory on your computer for your Chemkin work, and 2) download kinetic mechanism files AAUmech.inp

More information

Ligand Scout Tutorials

Ligand Scout Tutorials Ligand Scout Tutorials Step : Creating a pharmacophore from a protein-ligand complex. Type ke6 in the upper right area of the screen and press the button Download *+. The protein will be downloaded and

More information

A First Course on Kinetics and Reaction Engineering Example 1.2

A First Course on Kinetics and Reaction Engineering Example 1.2 Example 1.2 Problem Purpose This example shows how to determine when it is permissible to choose a basis for your calculations. It also illustrates how to use reaction progress variables and the initial

More information

Ammonia Synthesis with Aspen Plus V8.0

Ammonia Synthesis with Aspen Plus V8.0 Ammonia Synthesis with Aspen Plus V8.0 Part 1 Open Loop Simulation of Ammonia Synthesis 1. Lesson Objectives Become comfortable and familiar with the Aspen Plus graphical user interface Explore Aspen Plus

More information

WS Prediction of the carbon deposition in steam reforming unit (Equilibrium reaction calculation in Gibbs Reactor)

WS Prediction of the carbon deposition in steam reforming unit (Equilibrium reaction calculation in Gibbs Reactor) WS-4-03 Prediction of the carbon deposition in steam reforming unit (Equilibrium reaction calculation in Gibbs Reactor) Problem Steam reformer is often used in refineries or chemical plants. Design and

More information

= k 2 [CH 3 *][CH 3 CHO] (1.1)

= k 2 [CH 3 *][CH 3 CHO] (1.1) Answers to Exercises Last update: Tuesday 29 th September, 205. Comments and suggestions can be sent to i.a.w.filot@tue.nl Exercise d[ch 4 ] = k 2 [CH 3 *][CH 3 CHO].) The target is to express short-lived

More information

Chemical Reaction Engineering. Dr. Yahia Alhamed

Chemical Reaction Engineering. Dr. Yahia Alhamed Chemical Reaction Engineering Dr. Yahia Alhamed 1 Kinetics and Reaction Rate What is reaction rate? It is the rate at which a species looses its chemical identity per unit volume. The rate of a reaction

More information

CHE 611 Advanced Chemical Reaction Engineering

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

More information

Objective: Building a Bioreactor with intracellular reactions

Objective: Building a Bioreactor with intracellular reactions www.optience.com BioCell Model Objective: Building a Bioreactor with intracellular reactions This example shows a more advanced bioreactor model where both intracellular and extracellular concentrations

More information

Aspen Plus PFR Reactors Tutorial using Styrene with Pressure Drop Considerations By Robert P. Hesketh and Concetta LaMarca Spring 2005

Aspen Plus PFR Reactors Tutorial using Styrene with Pressure Drop Considerations By Robert P. Hesketh and Concetta LaMarca Spring 2005 Aspen Plus PFR Reactors Tutorial using Styrene with Pressure Drop Considerations By Robert P. Hesketh and Concetta LaMarca Spring 2005 In this laboratory we will incorporate pressure-drop calculations

More information

Chemical Reactions and Chemical Reactors

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

More information

Process design decisions and project economics Dr. V. S. Moholkar Department of chemical engineering Indian Institute of Technology, Guwahati

Process design decisions and project economics Dr. V. S. Moholkar Department of chemical engineering Indian Institute of Technology, Guwahati Process design decisions and project economics Dr. V. S. Moholkar Department of chemical engineering Indian Institute of Technology, Guwahati Module - 02 Flowsheet Synthesis (Conceptual Design of a Chemical

More information

Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09)

Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09) Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09) In this session you will learn how to create a stoichiometric reactor model

More information

ChE 344 Chemical Reaction Engineering Winter 1999 Final Exam. Open Book, Notes, CD ROM, Disk, and Web

ChE 344 Chemical Reaction Engineering Winter 1999 Final Exam. Open Book, Notes, CD ROM, Disk, and Web ChE 344 Chemical Reaction Engineering Winter 1999 Final Exam Open Book, Notes, CD ROM, Disk, and Web Name Honor Code 1) /25 pts 2) /15 pts 3) /10 pts 4) / 3 pts 5) / 6 pts 6) / 8 pts 7) / 8 pts 8) / 5

More information

Chapter 12. Answers to Questions. 1. (a) nitrogen dioxide (b) hydrogen sulfide (c) hydrogen chloride

Chapter 12. Answers to Questions. 1. (a) nitrogen dioxide (b) hydrogen sulfide (c) hydrogen chloride Chapter 12 Answers to Questions 1. (a) nitrogen dioxide (b) hydrogen sulfide (c) hydrogen chloride 2. (a) hydrogen cyanide (b) dinitrogen oxide (c) ammonia 3. X = sulfur, Y = oxygen, Z = sulfur dioxide

More information

HSC Chemistry 7.0 User's Guide

HSC Chemistry 7.0 User's Guide HSC Chemistry 7.0 47-1 HSC Chemistry 7.0 User's Guide Sim Flowsheet Module Experimental Mode Pertti Lamberg Outotec Research Oy Information Service P.O. Box 69 FIN - 28101 PORI, FINLAND Fax: +358-20 -

More information

Reaction and Diffusion in a Porous Catalyst Pellet. by Richard K. Herz

Reaction and Diffusion in a Porous Catalyst Pellet. by Richard K. Herz Reaction and Diffusion in a Porous Catalyst Pellet by Richard K. Herz Solid catalysts are often called "heterogeneous catalysts" meaning that they are in a different phase from fluid reactants

More information

TABLE OF CONTENT. Chapter 4 Multiple Reaction Systems 61 Parallel Reactions 61 Quantitative Treatment of Product Distribution 63 Series Reactions 65

TABLE OF CONTENT. Chapter 4 Multiple Reaction Systems 61 Parallel Reactions 61 Quantitative Treatment of Product Distribution 63 Series Reactions 65 TABLE OF CONTENT Chapter 1 Introduction 1 Chemical Reaction 2 Classification of Chemical Reaction 2 Chemical Equation 4 Rate of Chemical Reaction 5 Kinetic Models For Non Elementary Reaction 6 Molecularity

More information

Athena Visual Software, Inc. 1

Athena Visual Software, Inc. 1 Athena Visual Studio Visual Kinetics Tutorial VisualKinetics is an integrated tool within the Athena Visual Studio software environment, which allows scientists and engineers to simulate the dynamic behavior

More information

Virtual Beach Making Nowcast Predictions

Virtual Beach Making Nowcast Predictions Virtual Beach 3.0.6 Making Nowcast Predictions In this module you will learn how to: A. Create a real-time connection to Web data services through EnDDaT B. Download real-time data to make a Nowcast prediction

More information

41. Sim Reactions Example

41. Sim Reactions Example HSC Chemistry 7.0 41-1(6) 41. Sim Reactions Example Figure 1: Sim Reactions Example, Run mode view after calculations. General This example contains instruction how to create a simple model. The example

More information

How to Perform a Site Based Plant Search

How to Perform a Site Based Plant Search PlantSelector Help Use PlantSelector to get detailed information and photos of plants by: Searching for plants that will grow well at your planting site. How do I do this? OR Searching for plants with

More information

Oxidative Coupling of Methane: A Microkinetic Model Accounting for Intraparticle Surface-Intermediates Concentration Profiles

Oxidative Coupling of Methane: A Microkinetic Model Accounting for Intraparticle Surface-Intermediates Concentration Profiles pubs.acs.org/iecr Oxidative Coupling of Methane: A Microkinetic Model Accounting for Intraparticle Surface-Intermediates Concentration Profiles Panagiotis N. Kechagiopoulos, Joris W. Thybaut,* and Guy

More information

Temperature: An increase in temperature increases the rate of reaction.

Temperature: An increase in temperature increases the rate of reaction. 9 Kinetics I Factors affecting the rate of reaction Temperature: An increase in temperature increases the rate of reaction. Concentration: An increase in the concentration of a solution of reactants increases

More information

Umeå University Sara Sjöstedt-de Luna Time series analysis and spatial statistics

Umeå University Sara Sjöstedt-de Luna Time series analysis and spatial statistics Umeå University 01-05-5 Sara Sjöstedt-de Luna Time series analysis and spatial statistics Laboration in ArcGIS Geostatistical Analyst These exercises are aiming at helping you understand ArcGIS Geostatistical

More information

Learning to Use Scigress Wagner, Eugene P. (revised May 15, 2018)

Learning to Use Scigress Wagner, Eugene P. (revised May 15, 2018) Learning to Use Scigress Wagner, Eugene P. (revised May 15, 2018) Abstract Students are introduced to basic features of Scigress by building molecules and performing calculations on them using semi-empirical

More information

M&M Exponentials Exponential Function

M&M Exponentials Exponential Function M&M Exponentials Exponential Function Teacher Guide Activity Overview In M&M Exponentials students will experiment with growth and decay functions. Students will also graph their experimental data and

More information

A First Course on Kinetics and Reaction Engineering Example 38.1

A First Course on Kinetics and Reaction Engineering Example 38.1 Example 38.1 Problem Purpose This example illustrates the calculation of the effectiveness factor and demonstrates its use in the ideal PFR design equations for a first-order reaction with spherical catalyst

More information

Reactions and Reactors

Reactions and Reactors Reactions and Reactors ChE 400 - Reactive Process Engineering If we want to run a chemical process in order to convert some reactants (the reactor feed) to some product (the reactor effluent), we have

More information

M E R C E R W I N WA L K T H R O U G H

M E R C E R W I N WA L K T H R O U G H H E A L T H W E A L T H C A R E E R WA L K T H R O U G H C L I E N T S O L U T I O N S T E A M T A B L E O F C O N T E N T 1. Login to the Tool 2 2. Published reports... 7 3. Select Results Criteria...

More information

ChE 344 Winter 2013 Mid Term Exam I Tuesday, February 26, Closed Book, Web, and Notes. Honor Code

ChE 344 Winter 2013 Mid Term Exam I Tuesday, February 26, Closed Book, Web, and Notes. Honor Code ChE 344 Winter 2013 Mid Term Exam I Tuesday, February 26, 2013 Closed Book, Web, and Notes Name Honor Code (Sign at the end of exam period) 1) / 5 pts 2) / 5 pts 3) / 5 pts 4) / 5 pts 5) / 5 pts 6) / 5

More information

A First Course on Kinetics and Reaction Engineering Example 33.1

A First Course on Kinetics and Reaction Engineering Example 33.1 Example 33.1 Problem Purpose This problem will help you determine whether you have mastered the learning objectives for this unit. It illustrates the analysis of a tubular reactor using the ial dispersion

More information

ICM-Chemist How-To Guide. Version 3.6-1g Last Updated 12/01/2009

ICM-Chemist How-To Guide. Version 3.6-1g Last Updated 12/01/2009 ICM-Chemist How-To Guide Version 3.6-1g Last Updated 12/01/2009 ICM-Chemist HOW TO IMPORT, SKETCH AND EDIT CHEMICALS How to access the ICM Molecular Editor. 1. Click here 2. Start sketching How to sketch

More information

INTRODUCTION TO CHEMICAL PROCESS SIMULATORS

INTRODUCTION TO CHEMICAL PROCESS SIMULATORS INTRODUCTION TO CHEMICAL PROCESS SIMULATORS DWSIM Chemical Process Simulator A. Carrero, N. Quirante, J. Javaloyes October 2016 Introduction to Chemical Process Simulators Contents Monday, October 3 rd

More information

Understanding Chemical Reactions through Computer Modeling. Tyler R. Josephson University of Delaware 4/21/16

Understanding Chemical Reactions through Computer Modeling. Tyler R. Josephson University of Delaware 4/21/16 Understanding Chemical Reactions through Computer Modeling Tyler R. Josephson University of Delaware 4/21/16 A little about me B.S. in Chem E from U of M, 2011 Currently, Ph.D. student at University of

More information

A First Course on Kinetics and Reaction Engineering Example 38.2

A First Course on Kinetics and Reaction Engineering Example 38.2 Example 38.2 Problem Purpose This example illustrates some limitations to the use of the effectiveness factor and shows how to model an isothermal packed bed reactor by writing mole balances separately

More information

Identify the condition that causes a bond in CCl 4 to break in the upper atmosphere. Deduce an equation for the formation of the reactive species.

Identify the condition that causes a bond in CCl 4 to break in the upper atmosphere. Deduce an equation for the formation of the reactive species. Q1.CCl 4 is an effective fire extinguisher but it is no longer used because of its toxicity and its role in the depletion of the ozone layer. In the upper atmosphere, a bond in CCl 4 breaks and reactive

More information

Two-dimensional mathematical modeling of oxidative coupling of methane in a membrane reactor

Two-dimensional mathematical modeling of oxidative coupling of methane in a membrane reactor Conference topics: cr11 TIChE International Conference 11 Two-dimensional mathematical modeling of oxidative coupling of methane in a membrane reactor Salamah Manundawee 1, Suttichai Assabumrungrat 1,

More information

Methane Oxidation Reactions

Methane Oxidation Reactions Methane Oxidation Reactions CH 4 + 2 O -> CO 2 2 + 2 H 2 O Total Oxidation (Combustion) CH 4 + 0.5 O -> CO 2 + 2 H 2 CO + 0.5 O -> CO 2 2 H 2 + 0.5 O -> H 2 2 O CH 4 + H 2 O->CO + 3 H 2 Partial Oxidation

More information

OECD QSAR Toolbox v.4.1. Step-by-step example for predicting skin sensitization accounting for abiotic activation of chemicals

OECD QSAR Toolbox v.4.1. Step-by-step example for predicting skin sensitization accounting for abiotic activation of chemicals OECD QSAR Toolbox v.4.1 Step-by-step example for predicting skin sensitization accounting for abiotic activation of chemicals Background Outlook Objectives The exercise Workflow 2 Background This is a

More information

Introduction to MoLEs Activities Computer Simulations *

Introduction to MoLEs Activities Computer Simulations * Introduction to MoLEs Activities Computer Simulations * Molecular Level Experiments (MoLEs) are chemistry laboratory experiments based on computer simulations. There are two types of simulation programs

More information

CHAPTER 4 Chemical Kinetics: Rate and Mechanistic Models. 4.1 Introduction

CHAPTER 4 Chemical Kinetics: Rate and Mechanistic Models. 4.1 Introduction CHAPE 4 Chemical Kinetics: ate and Mechanistic Models 4. Introduction By listing the plausible reaction stoichiometries, we can calculate the composition of the system in its final state, i.e. at equilibrium,

More information

Non-steady-state approach t o steady-state kinetics: cas e study of H2S oxidation by oxygen

Non-steady-state approach t o steady-state kinetics: cas e study of H2S oxidation by oxygen Boresov Institute of Catalysis From the SelectedWors of Andrey N Zagoruio December, 2003 Non-steady-state approach t o steady-state inetics: cas e study of H2S oxidation by oxygen Andrey N Zagoruio Vladimir

More information

MAGNETITE OXIDATION EXAMPLE

MAGNETITE OXIDATION EXAMPLE HSC Chemistry 7.0 1 MAGNETITE OXIDATION EXAMPLE Pelletized magnetite (Fe 3 O 4 ) ore may be oxidized to hematite (Fe 2 O 3 ) in shaft furnace. Typical magnetite content in ore is some 95%. Oxidation is

More information

CHEMICAL KINETICS. LECTURE Introduction

CHEMICAL KINETICS. LECTURE Introduction LECTURE-2. 2. Introduction CHEMICAL KINETICS 09//03 We have shown in the previous chapter that upon listing of the plausible reaction stoichiometries we can calculate the composition of the system in its

More information

Chemical Reaction Engineering. Lecture 2

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:

More information

Ontario Flow Assessment Tool III

Ontario Flow Assessment Tool III Ontario Flow Assessment Tool III Quick Start Guide Ontario Flow Assessment Tools, version III (OFAT III) is an online, spatially-based application to automate a series of labourintensive technical hydrology

More information

Burning a Hydrocarbon II

Burning a Hydrocarbon II Burning a Hydrocarbon II Name Lab Section Problem Statement: How are the masses of products limited by the amounts of reactants? I. Data Collection: A. Go to http://cheminfo.chem.ou.edu/~mra/home.html

More information

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

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:

More information

Dock Ligands from a 2D Molecule Sketch

Dock Ligands from a 2D Molecule Sketch Dock Ligands from a 2D Molecule Sketch March 31, 2016 Sample to Insight CLC bio, a QIAGEN Company Silkeborgvej 2 Prismet 8000 Aarhus C Denmark Telephone: +45 70 22 32 44 www.clcbio.com support-clcbio@qiagen.com

More information

Building Inflation Tables and CER Libraries

Building Inflation Tables and CER Libraries Building Inflation Tables and CER Libraries January 2007 Presented by James K. Johnson Tecolote Research, Inc. Copyright Tecolote Research, Inc. September 2006 Abstract Building Inflation Tables and CER

More information

Standards-Based Quantification in DTSA-II Part II

Standards-Based Quantification in DTSA-II Part II Standards-Based Quantification in DTSA-II Part II Nicholas W.M. Ritchie National Institute of Standards and Technology, Gaithersburg, MD 20899-8371 nicholas.ritchie@nist.gov Introduction This article is

More information

CHEM Chemical Kinetics

CHEM Chemical Kinetics Chemical Kinetics Catalysts A catalyst is a substance that increases the rate of the reaction but is neither created nor destroyed in the process. Catalysts can be divided into two broad categories. Homogeneous

More information

Esterification in a PFR with Aspen Plus V8.0

Esterification in a PFR with Aspen Plus V8.0 Esterification in a PFR with Aspen Plus V8.0 1. Lesson Objectives Use Aspen Plus to determine whether a given reaction is technically feasible using a plug flow reactor. 2. Prerequisites Aspen Plus V8.0

More information

Topical Workshop MOF Catalysis. Microkinetics in Heterogeneous Catalysis. DFG Priority Program 1362

Topical Workshop MOF Catalysis. Microkinetics in Heterogeneous Catalysis. DFG Priority Program 1362 Topical Workshop MOF Catalysis Microkinetics in Heterogeneous Catalysis DFG Priority Program 1362 Roger Gläser Institut für Technische Chemie Institut für Nichtklassische Chemie e.v. Universität Leipzig

More information

Tutorial: Premixed Flow in a Conical Chamber using the Finite-Rate Chemistry Model

Tutorial: Premixed Flow in a Conical Chamber using the Finite-Rate Chemistry Model Tutorial: Premixed Flow in a Conical Chamber using the Finite-Rate Chemistry Model Introduction The purpose of this tutorial is to provide guidelines and recommendations for setting up and solving the

More information

Engineering. Green Chemical. S. Suresh and S. Sundaramoorthy. and Chemical Processes. An Introduction to Catalysis, Kinetics, CRC Press

Engineering. Green Chemical. S. Suresh and S. Sundaramoorthy. and Chemical Processes. An Introduction to Catalysis, Kinetics, CRC Press I i Green Chemical Engineering An Introduction to Catalysis, Kinetics, and Chemical Processes S. Suresh and S. Sundaramoorthy CRC Press Taylor & Francis Group Boca Raton London New York CRC Press is an

More information

Effects of Ethane Partial Pressure on the Apparent Rate Expressions of Oxidative Couplin... Page 1 of 16

Effects of Ethane Partial Pressure on the Apparent Rate Expressions of Oxidative Couplin... Page 1 of 16 Effects of Ethane Partial Pressure on the Apparent Rate Expressions of Oxidative Couplin... Page 1 of 16 Effects of Ethane Partial Pressure on the Apparent Rate Expressions of Oxidative Coupling of Methane

More information

Chemical Reaction Engineering Prof. Jayant Modak Department of Chemical Engineering Indian Institute of Science, Bangalore

Chemical Reaction Engineering Prof. Jayant Modak Department of Chemical Engineering Indian Institute of Science, Bangalore Chemical Reaction Engineering Prof. Jayant Modak Department of Chemical Engineering Indian Institute of Science, Bangalore Lecture No. #40 Problem solving: Reactor Design Friends, this is our last session

More information

Project: Equilibrium Simulation

Project: Equilibrium Simulation UNIT 02: BCLN CHEMISTRY 12 - Rev. July, 2015 Project: Simulation Potential Credits: /20 Name: Goal: In this project you will explore the concept of reversible reactions and calculating K eq using some

More information

Instructions for Mapping 2011 Census Data

Instructions for Mapping 2011 Census Data Instructions for Mapping 2011 Census Data To map 2011 census data, you must download the census boundary files and the census data separately, then join the two files in ArcMap. In this guide, we will

More information

Be prepared to discuss the quantitative comparison method in the oral exam.

Be prepared to discuss the quantitative comparison method in the oral exam. Subject: Ring Experiment III 8 Shell and Tube Heat Exchanger Control The shell and Tube Heat Exchanger has two control valves: one on the process fluid flowing to the tubes and one on the cooling water

More information

Supplementary information. Catalytic consequences of Ga promotion on Cu for CO 2 hydrogenation to methanol

Supplementary information. Catalytic consequences of Ga promotion on Cu for CO 2 hydrogenation to methanol Electronic Supplementary Material (ESI) for Catalysis Science & Technology. This journal is The Royal Society of Chemistry 2017 Supplementary information Catalytic consequences of Ga promotion on Cu for

More information

Typical kinetics Time. 1. What happens to the concentration of A over time? a. Increases b. Decreases c.

Typical kinetics Time. 1. What happens to the concentration of A over time? a. Increases b. Decreases c. Cheryl Coolidge Guided Inquiry Activity Enzyme Kinetics, Part One Why? Understanding the rate behavior of enzyme catalyzed reactions can help to explain how these biologically important reactions are controlled

More information

Student Exploration: Energy of a Pendulum

Student Exploration: Energy of a Pendulum Name: Date: Student Exploration: Energy of a Pendulum Vocabulary: conservation of energy, gravitational potential energy, kinetic energy, pendulum, potential energy, velocity Prior Knowledge Questions

More information

DESIGN AND CONTROL OF BUTYL ACRYLATE REACTIVE DISTILLATION COLUMN SYSTEM. I-Lung Chien and Kai-Luen Zeng

DESIGN AND CONTROL OF BUTYL ACRYLATE REACTIVE DISTILLATION COLUMN SYSTEM. I-Lung Chien and Kai-Luen Zeng DESIGN AND CONTROL OF BUTYL ACRYLATE REACTIVE DISTILLATION COLUMN SYSTEM I-Lung Chien and Kai-Luen Zeng Department of Chemical Engineering, National Taiwan University of Science and Technology, Taipei

More information

2011 DOE Crosscut Workshop on Lean Emissions Reduction Simulation April 2011 Dearborn, MI

2011 DOE Crosscut Workshop on Lean Emissions Reduction Simulation April 2011 Dearborn, MI Renewable energies Eco-friendly production Innovative transport Eco-efficient processes Sustainable resources 2011 DOE Crosscut Workshop on Lean Emissions Reduction Simulation April 2011 Dearborn, MI Research

More information

Boyle s Law and Charles Law Activity

Boyle s Law and Charles Law Activity Boyle s Law and Charles Law Activity Introduction: This simulation helps you to help you fully understand 2 Gas Laws: Boyle s Law and Charles Law. These laws are very simple to understand, but are also

More information

How sulphur really forms on the catalyst surface

How sulphur really forms on the catalyst surface How sulphur really forms on the catalyst surface The catalytic oxidation of hydrogen sulphide to sulphur plays a major role in the sulphur recovery process. The catalytic stages of a Claus unit produce

More information

SeeSAR 7.1 Beginners Guide. June 2017

SeeSAR 7.1 Beginners Guide. June 2017 SeeSAR 7.1 Beginners Guide June 2017 Part 1: Basics 1 Type a pdb code and press return or Load your own protein or already existing project, or Just load molecules To begin, let s type 2zff and download

More information

Static and Kinetic Friction

Static and Kinetic Friction Experiment Static and Kinetic Friction Prelab Questions 1. Examine the Force vs. time graph and the Position vs. time graph below. The horizontal time scales are the same. In Region I, explain how an object

More information

Consequences of Surface Oxophilicity of Ni, Ni-Co, and Co Clusters on Methane. Activation

Consequences of Surface Oxophilicity of Ni, Ni-Co, and Co Clusters on Methane. Activation Supporting Information for: Consequences of Surface Oxophilicity of Ni, Ni-Co, and Co Clusters on Methane Activation Weifeng Tu, 1 Mireille Ghoussoub, Chandra Veer Singh,,3** and Ya-Huei (Cathy) Chin 1,*

More information

Jaguar DFT Optimizations and Transition State Searches

Jaguar DFT Optimizations and Transition State Searches Jaguar DFT Optimizations and Transition State Searches Density Functional Theory (DFT) is a quantum mechanical (QM) method that gives results superior to Hartree Fock (HF) in less computational time. A

More information

A First Course on Kinetics and Reaction Engineering. Class 9 on Unit 9

A First Course on Kinetics and Reaction Engineering. Class 9 on Unit 9 A First Course on Kinetics and Reaction Engineering Class 9 on Unit 9 Part I - Chemical Reactions Part II - Chemical Reaction Kinetics Where We re Going A. Rate Expressions - 4. Reaction Rates and Temperature

More information

Example 8: CSTR with Multiple Solutions

Example 8: CSTR with Multiple Solutions Example 8: CSTR with Multiple Solutions This model studies the multiple steady-states of exothermic reactions. The example is from Parulekar (27) which in turn was modified from one by Fogler (1999). The

More information

Role of products and intermediates in bioethanol conversion to hydrocarbons on H-ZSM-5: A time-resolved study

Role of products and intermediates in bioethanol conversion to hydrocarbons on H-ZSM-5: A time-resolved study Role of products and intermediates in bioethanol conversion to hydrocarbons on H-ZSM-5: A time-resolved study Rakesh Batchu, Vladimir V. Galvita, Konstantinos Alexopoulos, Kristof Van der Borght, Hilde

More information

Chemical Reaction Engineering

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

More information

Tutorial 23 Back Analysis of Material Properties

Tutorial 23 Back Analysis of Material Properties Tutorial 23 Back Analysis of Material Properties slope with known failure surface sensitivity analysis probabilistic analysis back analysis of material strength Introduction Model This tutorial will demonstrate

More information

8.1 Chemical Properties and Changes. chemical property chemical change dissolving

8.1 Chemical Properties and Changes. chemical property chemical change dissolving 8.1 Chemical Properties and Changes chemical property chemical change dissolving Ability to Change 8.1 Chemical Properties and Changes In a chemical change, the properties that give a substance its identity

More information

Chemical Reaction Engineering - Part 12 - multiple reactions Richard K. Herz,

Chemical Reaction Engineering - Part 12 - multiple reactions Richard K. Herz, Chemical Reaction Engineering - Part 12 - multiple reactions Richard K. Herz, rherz@ucsd.edu, www.reactorlab.net Multiple reactions are usually present So far we have considered reactors in which only

More information

Kinetic Parameters Estimation using Vehicle Data for Exhaust Aftertreatment Devices

Kinetic Parameters Estimation using Vehicle Data for Exhaust Aftertreatment Devices Kinetic Parameters Estimation using Vehicle Data for Exhaust Aftertreatment Devices Karthik Ramanathan India Science Lab General Motors, Global Research and Development Center Bangalore, India Acknowledgments:

More information

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

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

More information

85. Geo Processing Mineral Liberation Data

85. Geo Processing Mineral Liberation Data Research Center, Pori / Pertti Lamberg 14024-ORC-J 1 (23) 85. Geo Processing Mineral Liberation Data 85.1. Introduction The Mineral Liberation Analyzer, MLA, is an automated mineral analysis system that

More information

Reactor Modeling of a Non-Catalytic OCM Process

Reactor Modeling of a Non-Catalytic OCM Process Iranian Journal of Chemical Engineering Vol. 2, No. 2, 2005, IAChE Reactor Modeling of a Non-Catalytic OCM Process M. Kazemeini and A.R. Mohammadi 2. Department of Chemical & Petroleum Engineering, Sharif

More information

Hydrogen addition to the Andrussow process for HCN synthesis

Hydrogen addition to the Andrussow process for HCN synthesis Applied Catalysis A: General 201 (2000) 13 22 Hydrogen addition to the Andrussow process for HCN synthesis A.S. Bodke, D.A. Olschki, L.D. Schmidt Department of Chemical Engineering and Materials Science,

More information

Chemical Reactions. Chapter 17

Chemical Reactions. Chapter 17 Chemical Reactions Chapter 17 Chemical Equations C+O 2 CO 2 C (s) +O 2 (g) CO 2 (g) Reactants on left, products on right Each are balanced because same number of atoms of reactants as products Some equations

More information

Review of Fitting Kinetic Data

Review of Fitting Kinetic Data L6-1 Review of Fitting Kinetic Data True or false: The goal of fitting kinetic data is to find the true rate expression. What are the two general methods used to fit kinetic data? L6-2 Advantages and Drawbacks

More information

HOW TO USE MIKANA. 1. Decompress the zip file MATLAB.zip. This will create the directory MIKANA.

HOW TO USE MIKANA. 1. Decompress the zip file MATLAB.zip. This will create the directory MIKANA. HOW TO USE MIKANA MIKANA (Method to Infer Kinetics And Network Architecture) is a novel computational method to infer reaction mechanisms and estimate the kinetic parameters of biochemical pathways from

More information

RT3D BTEX Degradation with Multiple Electron Acceptors

RT3D BTEX Degradation with Multiple Electron Acceptors GMS TUTRIALS RTD BTEX Degradation with Multiple Electron Acceptors This tutorial illustrates the steps involved in using GMS and RTD to model BTEX degradation using a multiple electron acceptor model.

More information

6/28/11. Avogadro s Number and the Mole. The Mole. The Mole. The Mole (mol)

6/28/11. Avogadro s Number and the Mole. The Mole. The Mole. The Mole (mol) Avogadro s Number and the Mole Molecular weight: The sum of atomic weights of all atoms in a molecule. Formula weight: The sum of atomic weights of all atoms in one formula unit of any compound. Mole:

More information

Lecture 11 Kjemisk reaksjonsteknikk Chemical Reaction Engineering

Lecture 11 Kjemisk reaksjonsteknikk Chemical Reaction Engineering Lecture Kjemisk reaksjonsteknikk Chemical Reaction Engineering Review of previous lectures Kinetic data analysis of heterogeneous reactions. Characterization of t catalysts. Kinetic study, find a kinetic

More information

VCell Tutorial. Building a Rule-Based Model

VCell Tutorial. Building a Rule-Based Model VCell Tutorial Building a Rule-Based Model We will demonstrate how to create a rule-based model of EGFR receptor interaction with two adapter proteins Grb2 and Shc. A Receptor-monomer reversibly binds

More information