Problems Points (Max.) Points Received
|
|
|
- Garry Stafford
- 6 years ago
- Views:
Transcription
1 Chemical Engineering 142 Chemical Kinetics and Reaction Engineering Midterm 1 Tuesday, October 8, :10 am-9:30 am The exam is 100 points total. Please read through the questions very carefully before answering. Make sure to show all your work. Name: Student ID: Problems Points (Max.) Points Received Total: You are allowed one sheet of paper with your notes on it and a calculator for this exam. A list of (possibly) useful integrals and constants is provided on the last page of this exam. 1
2 1. Consider the overall reversible formation of hydrobromic acid from hydrogen and bromine whose mechanism is given below:! Br!!!!! 2Br! Br + H!!!!! H + HBr H + Br!!! HBr + Br Note that all rate constants in the first reaction are given in terms of Br 2. The active intermediates are H and Br. This problem has parts a. through e. (25 points) a. Write rate expressions for the two intermediates. (4 points) b. Write a rate expression for the formation of HBr. (2 points) c. Using a pseudo-steady-state assumption determine the rate expression for the formation of HBr in terms of rate constants and concentrations of non-intermediate species. (10 points) 2
3 d. Repeat part c. using a quasi-equilibrium assumption instead of a pseudo-steady-state assumption. (8 points) e. Do you prefer quasi-equilibrium or pseudo-steady-state? No need to explain. (1 point) 3
4 2. Consider constant ν (m 3 /s) of water flowing through an ideal, isothermal, isobaric and liquid phase CSTR of volume V (m 3 ). Now at time t=0 switch from pure water to an aqueous solution of species A at a concentration C A0 (mol/m 3 ). (25 points) (a) If the species A is inert, please write the general mole balance of species A and derive the outlet concentration of species A C A versus t (t 0) (8 points) 4
5 (b) If a 0 th order reaction A(l) B(l) with rate constant k (mol/(m 3 *s)) is carried out in the CSTR once species A enters the reactor, please derive the outlet reactant concentration C A versus t (t 0) (10 points) (c) Calculate the time to reach 99% of the steady state concentration in the CSTR with and without the 0 th order reaction A(l) B(l). Comment on whether the presence of the reaction doesn t change/shortens/lengthens this time. (4 points) 5
6 (d) Please qualitatively plot C A versus t (t 0) and label the maximum and minimum values clearly on the plot. (3 points) 6
7 3. Consider the following elementary reaction taking place in a steady-state CSTR under isothermal and isobaric conditions: 2 A (g) B(g,l) + C(g) The feed consists of species A and an inert species I in equimolar amounts. The total feed rate is 10 mol/min and the total volumetric flow rate into the reactor is 1 liter/min. The saturation mole fraction of B is 0.2. Assume that the gas phases are all ideal. Use k =1 liter/(mol-min) (25 points) a) Construct a stoichiometric table in terms of the molar feed rates and account for all possible conversion regimes. (5 points) b) At what conversion does condensation begin? Show your calculation. (5 points) 7
8 c) Write down the expression for the reaction rate r A (mol/liter-min) as a function of initial concentrations of A and the conversion of A. Account for all possible conversion regimes. (5 points) 8
9 d) Find out the CSTR volume needed to achieve a conversion X A =0.95. (5 points) e) What is the mole fraction of different components in the gaseous phase at the CSTR outlet for a conversion X A =0.95? (5 points) 9
10 4. (25 points) A 2B, r A =- k C A Consider the elementary liquid-phase reaction above, which is being carried out in the leaking cylindrical batch reactor. This reactor is defective and has a small hole of area a in the base. As a result, reactor contents leak continuously at a volumetric flowrate v = a (2gz) 0.5 where z is the height of liquid in the reactor and g is the acceleration due to gravity. The cross-sectional area of the reactor is A C. The initial concentration is C AO and height of liquid is z o. Assume that density ρ remains constant. Z F A ( mol/s) v (litre/s) C A ( mol/liter) a) Express the volume of the liquid in the reactor explicitly as a function of time t and other constants. (5 points) b) Obtain an equation for dca. Hint: Write the general mole balance equation and simplify it. dt Express your answer in terms of C AO, k and t. (10 points) 10
11 c) Express C A explicitly as a function of t and other known constants. Is your answer going to be same or different for a batch reactor without any leak? Please explain physically why it is different or same? Answers without explanation will receive no credit. (4 points) 11
12 d) Find out the number of moles of A in the reactor, N A (t). (3 points) e) Find out the ratio of number of moles of B obtained in the leaky batch reactor after a time t to the number of moles of B obtained when there is no leakage. Assume that the lost liquid, which has leaked from the reactor, cannot be recovered and has no commercial value. Your final answer should contain time t and known constants only. (3 points) 12
Chemical Kinetics and Reaction Engineering Midterm 1
Page 1 Chemical & Biomolecular Engineering 142 Chemical Kinetics and Reaction Engineering Midterm 1 Tuesday, October 4, 2011 The exam is 100 points total and 20% of the course grade. Please read through
CBE 142: Chemical Kinetics & Reaction Engineering
CBE 142: Chemical Kinetics & Reaction Engineering Midterm #2 November 6 th 2014 This exam is worth 100 points and 20% of your course grade. Please read through the questions carefully before giving your
Chemical Kinetics and Reaction Engineering
Chemical Kinetics and Reaction Engineering MIDTERM EXAMINATION II Friday, April 9, 2010 The exam is 100 points total and 20% of the course grade. Please read through the questions carefully before giving
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
H 0 r = -18,000 K cal/k mole Assume specific heats of all solutions are equal to that of water. [10]
![H 0 r = -18,000 K cal/k mole Assume specific heats of all solutions are equal to that of water. [10]](/thumbs/96/128799678.jpg "H 0 r = -18,000 K cal/k mole Assume specific heats of all solutions are equal to that of water. [10]")
Code No: RR320802 Set No. 1 III B.Tech II Semester Supplementary Examinations, November/December 2005 CHEMICAL REACTION ENGINEERING-I (Chemical Engineering) Time: 3 hours Max Marks: 80 Answer any FIVE
ChE 344 Winter 2011 Mid Term Exam I + Solution. Closed Book, Web, and Notes
ChE 344 Winter 011 Mid Term Exam I + Thursday, February 17, 011 Closed Book, Web, and Notes Name Honor Code (sign at the end of exam) 1) / 5 pts ) / 5 pts 3) / 5 pts 4) / 15 pts 5) / 5 pts 6) / 5 pts 7)
ChE 344 Winter 2011 Final Exam + Solution. Open Book, Notes, and Web
ChE 344 Winter 011 Final Exam + Solution Monday, April 5, 011 Open Book, Notes, and Web Name Honor Code (Please sign in the space provided below) I have neither given nor received unauthorized aid on this
ChE 344 Winter 2013 Mid Term Exam II Tuesday, April 9, 2013
ChE 344 Winter 2013 Mid Term Exam II Tuesday, April 9, 2013 Open Course Textbook Only Closed everything else (i.e., Notes, In-Class Problems and Home Problems Name Honor Code (Please sign in the space
ChE 344 Winter 2011 Final Exam. Open Book, Notes, and Web
ChE 344 Winter 2011 Final Exam Monday, April 25, 2011 Open Book, Notes, and Web Name Honor Code (Please sign in the space provided below) I have neither given nor received unauthorized aid on this examination,
CHEMICAL REACTORS - PROBLEMS OF REACTOR ASSOCIATION 47-60
2011-2012 Course CHEMICL RECTORS - PROBLEMS OF RECTOR SSOCITION 47-60 47.- (exam jan 09) The elementary chemical reaction in liquid phase + B C is carried out in two equal sized CSTR connected in series.
Name. Honor Code: I have neither given nor received unauthorized aid on this examination, nor have I concealed any violations of the Honor Code.
ChE 344 Fall 014 Mid Term Exam II Wednesday, November 19, 014 Open Book Closed Notes (but one 3x5 note card), Closed Computer, Web, Home Problems and In-class Problems Name Honor Code: I have neither given
Exam 1 Chemical Reaction Engineering 26 February 2001 Closed Book and Notes
Exam 1 Chemical Reaction Engineering 26 February 21 Closed Book and Notes (2%) 1. Derive the unsteady-state mole balance for a chemical species A for a packed bed reactor using the following steps: a)
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
Midterm II. ChE 142 April 11, (Closed Book and notes, two 8.5 x11 sheet of notes is allowed) Printed Name
ChE 142 pril 11, 25 Midterm II (Closed Book and notes, two 8.5 x11 sheet of notes is allowed) Printed Name KEY By signing this sheet, you agree to adhere to the U.C. Berkeley Honor Code Signed Name_ KEY
IDEAL REACTORS FOR HOMOGENOUS REACTION AND THEIR PERFORMANCE EQUATIONS
IDEAL REACTORS FOR HOMOGENOUS REACTION AND THEIR PERFORMANCE EQUATIONS At the end of this week s lecture, students should be able to: Differentiate between the three ideal reactors Develop and apply the
ChE 344 Winter 2013 Final Exam + Solution. Open Course Textbook Only Closed everything else (i.e., Notes, In-Class Problems and Home Problems
ChE 344 Winter 03 Final Exam + Solution Thursday, May, 03 Open Course Textbook Only Closed everything else (i.e., Notes, In-Class Problems and Home Problems Name Honor Code (Please sign in the space provided
Chemical Reaction Engineering
CHPTE 7 Chemical eaction Engineering (Gate 00). The conversion for a second order, irreversible reaction (constant volume) () k B, in batch mode is given by k C t o ( kcot) (C) k C t o + (D) kcot (B) k
Chemical Reaction Engineering
Lecture 13 Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. Today s lecture Complex
CHEMICAL and BIOMOLECULAR ENGINEERING 140 Exam 1 Friday, September 28, 2018 Closed Book. Name: Section:
CHEMICAL and BIOMOLECULAR ENGINEERING 140 Exam 1 Friday, September 28, 2018 Closed Book Name: Section: Total score: /100 Problem 1: /30 Problem 2: /35 Problem 3: /35 1. (30 points) Short answer questions:
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:
AP Questions: Kinetics
AP Questions: Kinetics 1972 2 A + 2 B C + D The following data about the reaction above were obtained from three experiments: Rate of Formation of [A] [B] C (mole. liter -1 min -1 ) 1 0.60 0.15 6.3 10-3
Dr. Trent L. Silbaugh, Instructor Chemical Reaction Engineering Final Exam Study Guide
Chapter 1 Mole balances: Know the definitions of the rate of reaction, rate of disappearance and rate of appearance Know what a rate law is Be able to write a general mole balance and know what each term
13 th Aug Chemical Reaction Engineering CH3010. Home work problems
13 th ug 18. Chemical Reaction Engineering CH31. Home work problems 1. Batch reactor, variable volume. Consider a gas phase reaction B, conducted isothermally and at constant pressure in a batch reactor.
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
To increase the concentration of product formed in a PFR, what should we do?
To produce more moles of product per time in a flow reactor system, what can we do? a) Use less catalyst b) Make the reactor bigger c) Make the flow rate through the reactor smaller To increase the concentration
FLOW REACTORS FOR HOMOGENOUS REACTION: PERFORMANCE EQUATIONS AND APPLICATIONS
FLOW REACTORS FOR HOMOGENOUS REACTION: PERFORMANCE EQUATIONS AND APPLICATIONS At the end of this week s lecture, students should be able to: Develop and apply the performance equation for plug flow reactors.
Chemical Reaction Engineering - Part 14 - intro to CSTRs Richard K. Herz,
Chemical Reaction Engineering - Part 4 - intro to CSTRs Richard K. Herz, rherz@ucsd.edu, www.reactorlab.net Continuous Stirred Tank Reactors - CSTRs Here are a couple screenshots from the ReactorLab, Division
Mathematical Modeling Of Chemical Reactors
37 Mathematical Modeling Of Chemical Reactors Keywords: Reactors, lug flow, CSTR, Conversion, Selectivity Chemical reactor calculations are based on the elementary conservation laws of matter and energy.
10.37 Exam 2 25 April, points. = 10 nm. The association rate constant
Problem 1: 35 points 10.37 Exam 2 25 April, 2007 100 points A protein and ligand bind reversibly with = 10 nm. The association rate constant k on = 2x10 4 M 1 s -1. The two species are mixed at an initial
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
A First Course on Kinetics and Reaction Engineering Example 11.5
Example 11.5 Problem Purpose This problem illustrates the use of the age function measured using a step change stimulus to test whether a reactor conforms to the assumptions of the ideal PFR model. Then
Physics 121, Midterm Exam #3 Tuesday April 20, am 9.30 am. Do not turn the pages of the exam until you are instructed to do so.
Exam April, 8. am - 9. am, Midterm Exam # Tuesday April, 8. am 9. am Do not turn the pages of the exam until you are instructed to do so. You are responsible for reading the following rules carefully before
Chem 6 sample exam 1 (100 points total)
Chem 6 sample exam 1 (100 points total) @ This is a closed book exam to which the Honor Principle applies. @ The last page contains several equations which may be useful; you can detach it for easy reference.
MATLAB Ordinary Differential Equation (ODE) solver for a simple example 1. Introduction
MATLAB Ordinary Differential Equation (ODE) solver for a simple example 1. Introduction Differential equations are a convenient way to express mathematically a change of a dependent variable (e.g. concentration
For a recycle reactor the relationship between the volume and other parameters is given by
9 ug 7. CRE Tutorial Problem. or a recycle reactor the relationship between the volume and other parameters is given by V R in R r or simple kinetics such as first order reaction (under isothermal conditions),
No. 6. Reaction Rate Constant in CSTR Reaction. 1. Introduction
No. 6. Reaction Rate Constant in CSTR Reaction 1. Introduction In the majority of industrial chemical processes, the reactor vessel in which the process takes place is the key item of equipment. The design
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
MEEBAL Exam 1 October 2012 Show all work in your blue book. Points will be deducted if steps leading to answers are not shown. No work outside blue books (such as writing on the flow sheets) will be considered.
Chemical Reaction Engineering
Lecture 22 Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. Web Lecture 22 Class Lecture
Lecture 8. Mole balance: calculations of microreactors, membrane reactors and unsteady state in tank reactors
Lecture 8 Mole balance: calculations of microreactors, membrane reactors and unsteady state in tank reactors Mole alance in terms of oncentration and Molar low Rates Working in terms of number of moles
CSTR 1 CSTR 2 X A =?
hemical Engineering HE 33 F Applied Reaction Kinetics Fall 014 Problem Set 3 Due at the dropbox located in the hallway outside of WB 5 by Monday, Nov 3 rd, 014 at 5 pm Problem 1. onsider the following
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
CHE 113 MIDTERM EXAMINATION October 25, 2012
CHE 113 MIDTERM EXAMINATION October 25, 2012 University of Kentucky Department of Chemistry READ THESE DIRECTIONS CAREFULLY BEFORE STARTING THE EXAMINATION! It is extremely important that you fill in the
Chemical Reaction Engineering
Lecture 2 Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. 1 Lecture 2 Review of Lecture
Chemical Reaction Engineering
Lecture 24 Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. Web Lecture 24 Class Lecture
Stoichiometric Reactor Module
Reactor Analysis Types of Reactors Stoichiometric Reactor Module Stoichiometric Reactors (1) Stoichiometric Reactors (2) Stoichiometric Reactors (3) Equilibrium Reactors Gibbs Reactor RGibbs Module Equilibrium
CHEMICAL REACTORS - PROBLEMS OF NON IDEAL REACTORS 61-78
011-01 ourse HEMIL RETORS - PROBLEMS OF NON IDEL RETORS 61-78 61.- ccording to several experiments carried out in a continuous stirred tank reactor we suspect that the behavior of the reactor is not ideal.
S OF MATTER TER. Unit. I. Multiple Choice Questions (Type-I)
Unit 5 STATE TES TE S OF MATTER MA TER I. Multiple Choice Questions (Type-I) 1. A person living in Shimla observed that cooking food without using pressure cooker takes more time. The reason for this observation
Lecture 8. Mole balance: calculations of microreactors, membrane reactors and unsteady state in tank reactors
Lecture 8 Mole balance: calculations of microreactors, membrane reactors and unsteady state in tank reactors Mole alance in terms of Concentration and Molar Flow Rates Working in terms of number of moles
CHE 404 Chemical Reaction Engineering. Chapter 8 Steady-State Nonisothermal Reactor Design
Textbook: Elements of Chemical Reaction Engineering, 4 th Edition 1 CHE 404 Chemical Reaction Engineering Chapter 8 Steady-State Nonisothermal Reactor Design Contents 2 PART 1. Steady-State Energy Balance
September 28, Possibly Useful Information: 1) ( ) ( ) ( ) ( ) ( ) R = L atm / mol K. 2) ( ) ( ) ( ) h = 6.
Name Student ID # CEMISTRY 122 [Tyvoll] EXAM I September 28, 2007 1 2 3 4 5 Possibly Useful Information: 1) ( ) ( ) ( ) ( ) ( ) R = 0.0821 L atm / mol K 2) ( ) ( ) ( ) h = 6.63 x 10-34 J s 3) ( ) ( ) (
Fundamentals of Combustion
Fundamentals of Combustion Lec 3: Chemical Thermodynamics Dr. Zayed Al-Hamamre Content Process Heat Transfer 1-3 Process Heat Transfer 1-4 Process Heat Transfer 1-5 Theoretical and Excess Air Combustion
Chemical Reaction Engineering
Lecture 6 hemical Reaction Engineering (RE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. Lecture 6 Tuesday 1/9/13 Block
A First Course on Kinetics and Reaction Engineering Unit 33. Axial Dispersion Model
Unit 33. Axial Dispersion Model Overview In the plug flow reactor model, concentration only varies in the axial direction, and the sole causes of that variation are convection and reaction. Unit 33 describes
Figure Q3. Boundary conditions for a tubular reactor.
1. Please illustrate or explain the meaning the following questions: (a) (10%) Please proof the five dimensionless numbers in fluid transport by Buckingham method as Eu=f(Re, Fr, We, Ma). (b) (10%) Please
CE 329, Fall 2015 Assignment 16, Practice Exam
CE 39, Fall 15 Assignment 16, Practice Exam You may only use pencils, pens and erasers while taking this exam. You may NO use a calculator. You may not leave the room for any reason if you do, you must
Chemical Reaction Engineering
Lecture 4 hemical Reaction Engineering (RE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. hapter 4 Lecture 4 Block 1
A First Course on Kinetics and Reaction Engineering Example 26.3
Example 26.3 unit. Problem Purpose This problem will help you determine whether you have mastered the learning objectives for this Problem Statement A perfectly insulated tubular reactor with a diameter
Name (Print) Section # or TA name. 1. You may use a calculator and one 8 by 11-1/2 handwritten crib sheet during this
1. You may use a calculator and one 8 by 11-1/2 handwritten crib sheet during this exam. Bring extra pencils, batteries, calculators, if necessary. 2. Please place all books, bags, hats, etc. under the
IV B.Tech. I Semester Supplementary Examinations, February/March PROCESS MODELING AND SIMULATION (Chemical Engineering)
www..com www..com Code No: M0824/R07 Set No. 1 IV B.Tech. I Semester Supplementary Examinations, February/March - 2011 PROCESS MODELING AND SIMULATION (Chemical Engineering) Time: 3 Hours Max Marks: 80
Steady-State Molecular Diffusion
Steady-State Molecular Diffusion This part is an application to the general differential equation of mass transfer. The objective is to solve the differential equation of mass transfer under steady state
1/r plots: a brief reminder
L10-1 1/r plots: a brief reminder 1/r X target X L10-2 1/r plots: a brief reminder 1/r X target X L10-3 1/r plots: a brief reminder 1/r X target X Special Case: utocatalytic Reactions Let s assume a reaction
Chemical Reaction Engineering Lecture 5
Chemical Reaction Engineering g Lecture 5 The Scope The im of the Course: To learn how to describe a system where a (bio)chemical reaction takes place (further called reactor) Reactors Pharmacokinetics
CHEMICAL ENGINEERING LABORATORY CHEG 4137W/4139W. Reaction Kinetics Saponification of Isopropyl Acetate with Sodium Hydroxide
CHEMICAL ENGINEERING LABORATORY CHEG 4137W/4139W Reaction Kinetics Saponification of Isopropyl Acetate with Sodium Hydroxide Objective: The purpose of this experiment is to examine and determine the reaction
Process Classification
Process Classification Before writing a material balance (MB) you must first identify the type of process in question. Batch no material (mass) is transferred into or out of the system over the time period
Queen s University at Kingston. CHEE Winter Process Dynamics and Control. M. Guay. Quiz 1
Queen s University at Kingston CHEE 319 - Winter 2011 Process Dynamics and Control M. Guay Quiz 1 Instructions: 1. This is a 50 minute examination. 2. Please write your student number instead of your name
A First Course on Kinetics and Reaction Engineering. Class 20 on Unit 19
A First Course on Kinetics and Reaction Engineering Class 20 on Unit 19 Part I - Chemical Reactions Part II - Chemical Reaction Kinetics Where We re Going Part III - Chemical Reaction Engineering A. Ideal
6. Multiple Reactions
6. Multiple Reactions o Selectivity and Yield o Reactions in Series - To give maximum selectivity o Algorithm for Multiple Reactions o Applications of Algorithm o Multiple Reactions-Gas Phase 0. Types
Name: Discussion Section:
CBE 141: Chemical Engineering Thermodynamics, Spring 2018, UC Berkeley Midterm 2 March 22, 2018 Time: 80 minutes, closed-book and closed-notes, one-sided 8 ½ x 11 equation sheet allowed Please show all
Pre GATE Pre-GATE 2018
Pre GATE-018 Chemical Engineering CH 1 Pre-GATE 018 Duration : 180 minutes Total Marks : 100 CODE: GATE18-1B Classroom Postal Course Test Series (Add : 61C, Kalusarai Near HauzKhas Metro, Delhi 9990657855)
Design of Ideal Batch Reactors operated under Isothermal Conditions (It is important to have this note set with you during all lecture classes.
CP33 Set # July-October 3 Design of Ideal Batch Reactors operated under Isothermal Conditions It is important to have this note set with you during all lecture classes. A batch reactor is such that a batch
Physics 112 Second Midterm Exam February 22, 2000
Physics 112 Second Midterm Exam February 22, 2000 MIDTERM EXAM INSTRUCTIONS: You have 90 minutes to complete this exam. This is a closed book exam, although you are permitted to consult two sheets of handwritten
N h (6.02x10 )(6.63x10 )
CHEM 5200 - Final Exam - December 13, 2018 INFORMATION PAGES (Use for reference and for scratch paper) Constants and Conversion Factors: R = 8.31 J/mol-K = 8.31 kpa-l/mol-k = 0.00831 kj/mol-k 1 L-atm =
Next, make a stoichiometric table for the flow system (see Table 3-4 in Fogler). This table applies to both a PFR and CSTR reactor.
Cite as: William Green, Jr., and K. Dane Wittrup, course materials for.37 Chemical and Biological Reaction Engineering, Spring 27. MIT OpenCourseWare (http://ocw.mit.edu), Massachusetts Institute of Technology.
Extra Exercises. for. Chemical Reactor Analysis and Design Fundamentals
Extra Exercises for Chemical Reactor Analysis and Design Fundamentals James B. Rawlings Department of Chemical and Biological Engineering University of Wisconsin Madison, Wisconsin John G. Ekerdt Department
MSE410/ECE 340: Electrical Properties of Materials Fall 2016 School of Materials Science and Engineering Boise State University
MSE410/ECE 340: Electrical Properties of Materials Fall 2016 School of Materials Science and Engineering Boise State University Practice Midterm Exam October 2016 Read the questions carefully Label all
Chemical Kinetics. What quantities do we study regarding chemical reactions? 15 Chemical Kinetics
Chemical Kinetics Chemical kinetics: the study of reaction rate, a quantity conditions affecting it, the molecular events during a chemical reaction (mechanism), and presence of other components (catalysis).
KEY. Name. Chem 116 Sample Examination #1
page 1 of 7 KEY Name Last 5 digits of Student Number: XXX X hem 116 Sample Examination #1 This exam consists of seven (7) pages, including this cover page. Be sure your copy is complete before beginning
A First Course on Kinetics and Reaction Engineering Unit 22. Analysis of Steady State CSTRs
Unit 22. Analysis of Steady State CSRs Overview Reaction engineering involves constructing an accurate mathematical model of a real world reactor and then using that model to perform an engineering task
Name. Chem 116 Sample Examination #2
page 1 of 8 Name Last 5 digits of Student Number: XXX X Chem 116 Sample Examination #2 This exam consists of eight (8) pages, including this cover page. Be sure your copy is complete before beginning your
CHAPTER FIVE REACTION ENGINEERING
1 CHAPTER FIVE REACTION ENGINEERING 5.1. Determination of Kinetic Parameters of the Saponification Reaction in a PFR 5.3. Experimental and Numerical Determination of Kinetic Parameters of the Saponification
Physics 2080 Extra Credit Due March 15, 2011
Physics 2080 Extra Credit Due March 15, 2011 This assignment covers chapters 15-19 and is worth 10 points extra credit on the final exam. Print these pages and do all work here. Complete the questions
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
Edexcel Chemistry A-level
Edexcel Chemistry A-level Topic 5 - Formulae, Equations and Amounts of Substance Flashcards What is the symbol for amount of substance? What is the symbol for amount of substance? n What is the unit used
CHEMICAL ENGINEERING KINETICS/REACTOR DESIGN. Tony Feric, Kathir Nalluswami, Manesha Ramanathan, Sejal Vispute, Varun Wadhwa
CHEMICAL ENGINEERING KINETICS/REACTOR DESIGN Tony Feric, Kathir Nalluswami, Manesha Ramanathan, Sejal Vispute, Varun Wadhwa Presentation Overview Kinetics Reactor Design Non- Isothermal Design BASICS OF
Bioinformatics: Network Analysis
Bioinformatics: Network Analysis Reaction Kinetics COMP 572 (BIOS 572 / BIOE 564) - Fall 2013 Luay Nakhleh, Rice University 1 Reaction kinetics is the study of how fast chemical reactions take place, what
Fundamentals of Material Balances
Chapter 4 Fundamentals of Material Balances Material Balance-Part 1 Process Classifications 3 type of chemical processes: - Concept of boundary of the process 1. Batch process Feed is charge to the process
A First Course on Kinetics and Reaction Engineering Example 33.2
Example 33.2 Problem Purpose This problem will help you determine whether you have mastered the learning objectives for this unit. Specifically, it illustrates the use of the ial dispersion model and shows
Investigation of adiabatic batch reactor
Investigation of adiabatic batch reactor Introduction The theory of chemical reactors is summarized in instructions to Investigation of chemical reactors. If a reactor operates adiabatically then no heat
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
ERT 208 REACTION ENGINEERING
ERT 208 REACTION ENGINEERING MOLE BALANCE MISMISURAYA MEOR AHMAD School of bioprocess engineering Unimap Course Outcome No.1: Ability to solve the rate of reaction and their kinetics. objectives DESCRIBE
CHAPTER 6 CHEMICAL EQUILIBRIUM
For updated version, please click on http://ocw.ump.edu.my BSK1133 PHYSICAL CHEMISTRY CHAPTER 6 CHEMICAL EQUILIBRIUM PREPARED BY: DR. YUEN MEI LIAN AND DR. SITI NOOR HIDAYAH MUSTAPHA Faculty of Industrial
A First Course on Kinetics and Reaction Engineering Example 13.3
Example 13.3 Problem Purpose This example illustrates the analysis of CSTR data using linear least squares for a situation where there are two independent variables in the model being fit to the data.
DYNAMIC EQUILIBRIUM STUDY GUIDE multiple choice
DYNAMIC EQUILIBRIUM STUDY GUIDE multiple choice Multiple Choice Section: This study guide is a compilation of questions from provincial exams since April 1994. I urge you to become intimately familiar
Chemical Reaction Engineering
Lecture 19 Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. oday s lecture Gas Phase
A First Course on Kinetics and Reaction Engineering Unit 30.Thermal Back-Mixing in a PFR
Unit 30.Thermal Back-Mixing in a PFR Overview One advantage offered by a CSTR when running an exothermic reaction is that the cool feed gets heated by mixing with the contents of the reactor. As a consequence
ALE 1. Chemical Kinetics: Rates of Chemical Reactions
Name Chem 163 Section: Team Number: ALE 1. Chemical Kinetics: Rates of Chemical Reactions (Reference: Sections 16.1 16.2 + parts of 16.5 16.6 Silberberg 5 th edition) How do the surface area, concentration
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
1. Introductory Material
CHEE 321: Chemical Reaction Engineering 1. Introductory Material 1b. The General Mole Balance Equation (GMBE) and Ideal Reactors (Fogler Chapter 1) Recap: Module 1a System with Rxn: use mole balances Input
Thermodynamics Qualifying Exam Study Material
Thermodynamics Qualifying Exam Study Material The candidate is expected to have a thorough understanding of undergraduate engineering thermodynamics topics. These topics are listed below for clarification.