Block Flow Chart of a Typical Particle Processing System

Size: px
Start display at page:

Download "Block Flow Chart of a Typical Particle Processing System"

Transcription

1

2 Block Flow Chart of a Typical Particle Processing System Raw materials (R) uxiliary materials (H) Balance boundary of material, energy, information and costs flows Raw materials E I E I E I E I E I E I Store (R) Store (H) Raw material processing Material conversion Product Material Product B separation Waste Product formulation Store () Store (B) Store (W) Main product Waste Information (I) Energy (E) Costs (K) I E I E E I I E E I I I I uxiliary material supply E I E I Store (W) E I I uxiliary material processing H E I Recycling process (Reuse) E H I Byproduct Information Energy Proceeds

3 Hierarchic Order of Particle Conversion Processes Macroprocess (in process chamber of apparatus) Process group: Comminution Mixing Chemical reaction Storage Separation Drying gglomer pparatus & machine level dsorption films Subprocess (charact zone of process chamber) Material, energy, momentum transport Particle beds Particle swarms Continuum level Microprocess (smallest material element of process chamber) Material, energy, momentum transport fixed surface area sl, g variable surface area process determ sl, g Diluted in fluids, contact points ss variable contact area, process determin ss Particle level s solid l liquid g gas physicochemical basis of conversion Diffusion (nondirectional random transport) Convection (directional transport) De/gglomeration (creat/distruct of interactions) Moleculare level Fundamentals see: H Schubert, W Fratscher und R Kind, Zur Herausbildung einer einheitlichen Modellierungsstrategie in der Verfahrenstechnik, Chem Technik 35 (1980)

4 c) Element with one input and one output stream feed m pass through m P product d) Element with one input and two output streams feed Basic Elements of Processing Systems a) Element with one input stream feed m b) Element with one output stream source m store store separation sink m P product m P1 m P2 product m with multiple product streams m P1 m separation m P2 m P3 separat stage 1 e) Element with two input streams and one output stream feed m 1 m 2 mixing m P product m P1 separat stage 2 m P2 m P3

5 Basic Structures or Element Combinations of Processing Systems 1 Sequential combinations a) Cocurrent combination element 1 (stage 1) element 2 (stage 2) stage 1 stage 2 b) Countercurrent combination stage 1 stage 2 2 Bypass arrangements a) general element 1 element 2 element 3 b) with cocurrent elements (units) stage 1 stage 2 stage 3 c) with countercurrent elements (units) stage 1 stage 2 stage 3

6 Basic Structures or Element Combinations of Processing Systems 3 Parallel arrangement a) input side b) output side element 2a element 1a element 1 element 2 element 2b element 1b c) input and output side element 2a element 1 (stage 1) element 3 element 2b 4 Feedback arrangement, circuit element 2 feed element 1 product 5 Combination of feedbacks element 4 element 2 feed element 1 element 3 product

7 Combination of Comminution and Classification Units Block flow charts of sequential arrangements: a) Element with one input and one output stream m comminution m Fines m comminution 1 comminution 2 m Fines b) Element with one input and two output streams m m Coarse or m F1 m Fines or m F2 or with multiple product streams (fractions i) m m Coarse or m F1 m Fines1 or m F2 m Fines2 or m F F1 F2 F3 F4

8 Combination of Classification Units number of variants: N = (2 n)! n! (n+1)! n machines or classifiers n + 1 product fractions F n+1 1) n N e g 5 structur variants of 3 classifiers to produce n+1 = 4 fractions F 1 F 4 Sequential or cascade arrangements of 3 units: F1 F2 F3 F4 2) F1 F2 F4 F3 F1 F2 3) F3 F4 4) F1 F2 F4 F3 5) Parallel arrangement of n 1 = 2 units: F1 F2 F3 F4

9 Sequential Combination of Comminution and Classification Units Block flow charts: a) Preclassification + Coarse comminution Fines 1 Fines 2 b) Precomminution + comminution Coarse Fines c) Pre and subsequent comminution comminution 1 Coarse + comminution 2 Fines 1 Fines 2 d) Parallel arrangement of subsequent and comminution Coarse + comminution 1 1 Fines comminution 2 2 Fines 1 Fines 2 Fines 3 Technical flow charts (PIflow charts): crushers mills F F F F a) simple pass through without b) pass through with 1 precrusher (jaw crusher); 2 machine 3 recrusher (flat cone crusher) a) simple pass through b) pass through with classifier 1 multichamber mill; 2 premill (singlechamber mill); 3 finish mill for fines (doublechamber mill); 4 classifier with circulating air

10 Combination of Comminution and Classification Units Block flow charts of feedback arrangements and circuits: a) Feedback of coarse feedback of coarse m Coarse bzw m Feedback + comminution m m F Fines b) Feedback of fines Feedback of fines Coarse + comminution Fines 1 c) Preclassification unit preclassification 1 + Coarse feedback of coarse comminution 2 Fines 1 + Fines 2 d) Precomminution unit feedback of coarse precomminution comminution 2 comminution 1 Fines + Fines

11 Evaluation of Residence Time Distribution of Processes page 1 1 Batch process a) Cummulative residence time distribution F( τ) b) Frequency distribution f(τ) 1 F( 0 R f 0 R 2 Continuous processes with ideal residence time distribution Block flow chart: tracer 1 0 tracer a) ideal plug flow channel (piston flow, ideal replacement) 0 b) ideal continuous mixer c) cascade of ideal continuous mixers 3 1 st and 2 nd moment of residence time distribution a) mean residence time (complete initial moment) b) variance of residence time distribution (2 nd central moment)

12 Evaluation of Residence Time Distribution of Processes page 2 4 Normalized frequency distribution of residence time m f( / m ) for cascades of ideal mixers with various stage numbers n at constant total mean residence time m = n m,n = const m f ( m) 1,5 1,0 0,5 n n= with mean residence time of one stage (unit): 0 0,5 1,0 1,5 2,0 2,5 5 Cummulative residence time distribution F ( / m ) for cascades of ideal mixers with various stage numbers n 1 0,8 m F( / m ) 0,6 0,4 0,2 n= m n = 1 ideal mixer ideal replacement 6 Flow channel (pipe) with axial redispersion Bodenstein number of particles v' v axial dispersion (diffusion) coefficient of particles x ideal mixer ideal replacement

13

14

PRINCIPLES AND MODERN APPLICATIONS OF MASS TRANSFER OPERATIONS

PRINCIPLES AND MODERN APPLICATIONS OF MASS TRANSFER OPERATIONS PRINCIPLES AND MODERN APPLICATIONS OF MASS TRANSFER OPERATIONS Jaime Benitez iwiley- INTERSCIENCE A JOHN WILEY & SONS, INC., PUBLICATION Preface Nomenclature xiii xv 1. FUNDAMENTALS OF MASS TRANSFER 1

More information

Nirma University Institute of Technology Chemical Engineering Department, Handouts -RRP- CRE-II. Handouts

Nirma University Institute of Technology Chemical Engineering Department, Handouts -RRP- CRE-II. Handouts Handouts Handout 1: Practical reactor performance deviates from that of ideal reactor s : Packed bed reactor Channeling CSTR & Batch Dead Zones, Bypass PFR deviation from plug flow dispersion Deviation

More information

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

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)

More information

BAE 820 Physical Principles of Environmental Systems

BAE 820 Physical Principles of Environmental Systems BAE 820 Physical Principles of Environmental Systems Type of reactors Dr. Zifei Liu Ideal reactors A reactor is an apparatus in which chemical, biological, and physical processes (reactions) proceed intentionally,

More information

BASIC DESIGN EQUATIONS FOR MULTIPHASE REACTORS

BASIC DESIGN EQUATIONS FOR MULTIPHASE REACTORS BASIC DESIGN EQUATIONS FOR MULTIPHASE REACTORS Starting Reference 1. P. A. Ramachandran and R. V. Chaudhari, Three-Phase Catalytic Reactors, Gordon and Breach Publishers, New York, (1983). 2. Nigam, K.D.P.

More information

Chemical Reaction Engineering

Chemical Reaction Engineering Lecture 32! 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 32 Thursday

More information

Technical Paper. Spray Granulation Gives Solid Materials Customized. The properties of spray-granulated products can be as varied as their appearance

Technical Paper. Spray Granulation Gives Solid Materials Customized. The properties of spray-granulated products can be as varied as their appearance 03/17/15 page 1 of 7 Weimar, March / 17 / 2015 Flowability, dustlessness and easy dosing - these are some of the plus points of granulates produced by fluidized or spouted bed technology. The product design

More information

RADIOTRACER RESIDENCE TIME DISTRIBUTION METHOD IN DIAGNOSING INDUSTRIAL PROCESSING UNITS: CASE STUDIES

RADIOTRACER RESIDENCE TIME DISTRIBUTION METHOD IN DIAGNOSING INDUSTRIAL PROCESSING UNITS: CASE STUDIES RADIOTRACER RESIDENCE TIME DISTRIBUTION METHOD IN DIAGNOSING INDUSTRIAL PROCESSING UNITS: CASE STUDIES J. Thereska*, E. Plasari** * Institute of Applied Nuclear Physics, Tirana, Albania ** Ecole Nationale

More information

AIRLIFT BIOREACTORS. contents

AIRLIFT BIOREACTORS. contents AIRLIFT BIOREACTORS contents Introduction Fluid Dynamics Mass Transfer Airlift Reactor Selection and Design 1 INTRODUCTION airlift reactor (ALR) covers a wide range of gas liquid or gas liquid solid pneumatic

More information

GUJARAT TECHNOLOGICAL UNIVERSITY, AHMEDABAD, GUJARAT. Course Curriculum. MECHANICAL OPERATIONS (Code: ) Chemical Engineering

GUJARAT TECHNOLOGICAL UNIVERSITY, AHMEDABAD, GUJARAT. Course Curriculum. MECHANICAL OPERATIONS (Code: ) Chemical Engineering GUJARAT TECHNOLOGICAL UNIVERSITY, AHMEDABAD, GUJARAT Course Curriculum MECHANICAL OPERATIONS (Code: 3330502) Diploma Programme in which this course is offered Chemical Engineering Semester in which offered

More information

Residence time distribution and dispersion of gas phase in a wet gas scrubbing system

Residence time distribution and dispersion of gas phase in a wet gas scrubbing system Korean J. Chem. Eng., 24(5), 892-896 (2007) SHORT COMMUNICATION Residence time distribution and dispersion of gas phase in a wet gas scrubbing system Uk Yeong Kim, Sung Mo Son, Suk Hwan Kang, Yong Kang

More information

USING THE SMC TEST TO PREDICT COMMINUTION CIRCUIT PERFORMANCE

USING THE SMC TEST TO PREDICT COMMINUTION CIRCUIT PERFORMANCE USING THE SMC TEST TO PREDICT COMMINUTION CIRCUIT PERFORMANCE INTRODUCTION As the SMC Test produces the JK parameter values A and b as well as estimates the JK parameter ta and crusher model energy matrices,

More information

ATOMISATION TECHNOLOGY TO MINIMIZE THE EFFECTS OF NOZZLE WEAR ON THE DROPLET SIZE

ATOMISATION TECHNOLOGY TO MINIMIZE THE EFFECTS OF NOZZLE WEAR ON THE DROPLET SIZE ILASS-Europe Darmstadt 11-13 September ATOMISATION TECHNOLOGY TO MINIMIZE THE EFFECTS OF NOZZLE WEAR ON THE DROPLET SIZE J. Kohlmann*, M. Schmidt*, G. Slowik** and M.Bürgermeister*** * Fachhochschule für

More information

HEAT TRANSFER. PHI Learning PfcO too1. Principles and Applications BINAY K. DUTTA. Delhi Kolkata. West Bengal Pollution Control Board

HEAT TRANSFER. PHI Learning PfcO too1. Principles and Applications BINAY K. DUTTA. Delhi Kolkata. West Bengal Pollution Control Board HEAT TRANSFER Principles and Applications BINAY K. DUTTA West Bengal Pollution Control Board Kolkata PHI Learning PfcO too1 Delhi-110092 2014 Contents Preface Notations ix xiii 1. Introduction 1-8 1.1

More information

Attention is drawn to the following places, which may be of interest for search:

Attention is drawn to the following places, which may be of interest for search: B03C MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS (filters making use of electricity or magnetism B01D 35/06; separating

More information

Contents. Preface... xvii

Contents. Preface... xvii Contents Preface... xvii CHAPTER 1 Idealized Flow Machines...1 1.1 Conservation Equations... 1 1.1.1 Conservation of mass... 2 1.1.2 Conservation of momentum... 3 1.1.3 Conservation of energy... 3 1.2

More information

Types of Chemical Reactors. Nasir Hussain Production and Operations Engineer PARCO Oil Refinery

Types of Chemical Reactors. Nasir Hussain Production and Operations Engineer PARCO Oil Refinery Types of Chemical Reactors Nasir Hussain Production and Operations Engineer PARCO Oil Refinery Introduction Reactor is the heart of Chemical Process. A vessel designed to contain chemical reactions is

More information

Process Engineering Department summer semester 2017 Chair for Mechanical Process Engineering

Process Engineering Department summer semester 2017 Chair for Mechanical Process Engineering Process Engineering Department summer semester 2017 Chair for Mechanical Process Engineering Lecture: "Mechanical Process Engineering (Introduction into Particle Technology)" We. 09:00-11:00 G05- H4 Tutorial:

More information

Lace Diamond Mine DMS Commissioning

Lace Diamond Mine DMS Commissioning Lace Diamond Mine DMS Commissioning Derek Lahee Consulmet (Pty) Limited ABSTRACT This paper addresses the Lace Diamond Mine 100tph Fines DMS and 65tph Coarse DMS commissioning. Emphasis has been placed

More information

Development of a dynamic process model for the mechanical fluid separation in decanter centrifuges

Development of a dynamic process model for the mechanical fluid separation in decanter centrifuges Development of a dynamic process model for the mechanical fluid separation in decanter centrifuges Marco Gleiß a, Hermann Nirschl a a Institute for Mechanical Process Engineering and Mechanics, Karlsruhe

More information

Adsorption of Polar and Nonpolar Vapors on Selected Adsorbents: Breakthrough Curves and their Simulation

Adsorption of Polar and Nonpolar Vapors on Selected Adsorbents: Breakthrough Curves and their Simulation Adsorption of Polar and Nonpolar Vapors on Selected Adsorbents: Breakthrough Curves and their Simulation Dr. Robert Eschrich Quantachrome GmbH & Co. KG 2018-04-17 Leipziger Symposium on Dynamic Sorption

More information

Chapter 8 STATISTICAL ASSESSMENT OF NUMERICAL DIFFUSION

Chapter 8 STATISTICAL ASSESSMENT OF NUMERICAL DIFFUSION 84 hapter 8 STATISTIAL ASSESSMENT OF NUMERIAL DIFFUSION The assessment of the performance of high-order numerical methods regarding the numerical diffusion introduced in the solution of the scalar transport

More information

Lecture (9) Reactor Sizing. Figure (1). Information needed to predict what a reactor can do.

Lecture (9) Reactor Sizing. Figure (1). Information needed to predict what a reactor can do. Lecture (9) Reactor Sizing 1.Introduction Chemical kinetics is the study of chemical reaction rates and reaction mechanisms. The study of chemical reaction engineering (CRE) combines the study of chemical

More information

CHEMICAL ENGINEERING

CHEMICAL ENGINEERING CHEMICAL ENGINEERING Subject Code: CH Course Structure Sections/Units Section A Unit 1 Unit 2 Unit 3 Unit 4 Unit 5 Unit 6 Section B Section C Section D Section E Section F Section G Section H Section I

More information

Fill in the blanks. Q.1 The real stirrer tank reactor can be represented by model proposed by...

Fill in the blanks. Q.1 The real stirrer tank reactor can be represented by model proposed by... Fill in the blanks Q.1 The real stirrer tank reactor can be represented by model proposed by.... Q.2 The method of least square is minimizing the sum of the... errors. Q.3 The error regression can be quantified

More information

A population balance approach for continuous fluidized bed dryers

A population balance approach for continuous fluidized bed dryers A population balance approach for continuous fluidized bed dryers M. Peglow, U. Cunäus, C. Kettner, T. Metzger, E. Tsotsas, Thermal Process Engineering, University Magdeburg, 396 Magdeburg, ermany Abstract

More information

DEPARTMENT OF CHEMICAL ENGINEERING University of Engineering & Technology, Lahore. Mass Transfer Lab

DEPARTMENT OF CHEMICAL ENGINEERING University of Engineering & Technology, Lahore. Mass Transfer Lab DEPARTMENT OF CHEMICAL ENGINEERING University of Engineering & Technology, Lahore Mass Transfer Lab Introduction Separation equipments account for a major part of the capital investment in process industry.

More information

Updating the International Standard Classification of Occupations (ISCO) Draft ISCO-08 Group Definitions: Occupations in Chemicals

Updating the International Standard Classification of Occupations (ISCO) Draft ISCO-08 Group Definitions: Occupations in Chemicals International Labour Organization Organisation internationale du Travail Organización Internacional del Trabajo Updating the International Standard Classification of Occupations (ISCO) Draft ISCO-08 Group

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

Study on residence time distribution of CSTR using CFD

Study on residence time distribution of CSTR using CFD Indian Journal of Chemical Technology Vol. 3, March 16, pp. 114-1 Study on residence time distribution of CSTR using CFD Akhilesh Khapre*, Divya Rajavathsavai & Basudeb Munshi Department of Chemical Engineering,

More information

Models for Nonideal Reactors

Models for Nonideal Reactors Fogler_Web_Ch18.fm Page 1 Monday, October 9, 017 1:58 PM Models for Nonideal Reactors 18 Success is a journey, not a destination. Ben Sweetland Use the RTD to evaluate parameters. Overview. Not all tank

More information

Chapter 7 Mixing and Granulation

Chapter 7 Mixing and Granulation Chapter 7 Mixing and Granulation 7.1 Mixing and Segregation (Chapter 9) Mixing vs. segregation (1) Types of Mixture * Perfect mixing Random mixing Segregating mixing Figure 9.1 (2) Segregation 1) Causes

More information

SCANNING-PROBE TECHNIQUES OR APPARATUS; APPLICATIONS OF SCANNING-PROBE TECHNIQUES, e.g. SCANNING PROBE MICROSCOPY [SPM]

SCANNING-PROBE TECHNIQUES OR APPARATUS; APPLICATIONS OF SCANNING-PROBE TECHNIQUES, e.g. SCANNING PROBE MICROSCOPY [SPM] G01Q SCANNING-PROBE TECHNIQUES OR APPARATUS; APPLICATIONS OF SCANNING-PROBE TECHNIQUES, e.g. SCANNING PROBE MICROSCOPY [SPM] Scanning probes, i.e. devices having at least a tip of nanometre sized dimensions

More information

Diffusion and Adsorption in porous media. Ali Ahmadpour Chemical Eng. Dept. Ferdowsi University of Mashhad

Diffusion and Adsorption in porous media. Ali Ahmadpour Chemical Eng. Dept. Ferdowsi University of Mashhad Diffusion and Adsorption in porous media Ali Ahmadpour Chemical Eng. Dept. Ferdowsi University of Mashhad Contents Introduction Devices used to Measure Diffusion in Porous Solids Modes of transport in

More information

PREFACE. Julian C. Smith Peter Harriott. xvii

PREFACE. Julian C. Smith Peter Harriott. xvii PREFACE This sixth edition of the text on the unit operations of chemical engineering has been extensively revised and updated, with much new material and considerable condensation of some sections. Its

More information

IDEAL REACTORS FOR HOMOGENOUS REACTION AND THEIR PERFORMANCE EQUATIONS

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

More information

Specific heat capacity. Convective heat transfer coefficient. Thermal diffusivity. Lc ft, m Characteristic length (r for cylinder or sphere; for slab)

Specific heat capacity. Convective heat transfer coefficient. Thermal diffusivity. Lc ft, m Characteristic length (r for cylinder or sphere; for slab) Important Heat Transfer Parameters CBE 150A Midterm #3 Review Sheet General Parameters: q or or Heat transfer rate Heat flux (per unit area) Cp Specific heat capacity k Thermal conductivity h Convective

More information

THINK FLUID DYNAMIX Mixing, Homogenization & Blend Time. THINK Fluid Dynamix

THINK FLUID DYNAMIX Mixing, Homogenization & Blend Time. THINK Fluid Dynamix THINK FLUID DYNAMIX Mixing, Homogenization & Blend Time Provided by: THINK Fluid Dynamix Am Pestalozziring 21 D-91058 Erlangen (Germany) Tel. +49 (0)9131 69098-00 http://www.think-fd.com CFD ENGINEERING

More information

Non-Ideal Reactors. Definitions * Segregated flow - fluid elements do not mix, have different residence times - Need Residence Time Distribution

Non-Ideal Reactors. Definitions * Segregated flow - fluid elements do not mix, have different residence times - Need Residence Time Distribution Non-Ideal Reactors Deviations from ideal reactor behavior - Tank Reactors: inadequate mixing, stagnant regions, bypassing or short-circuiting Tubular Reactors: mixing in longitudinal direction, incomplete

More information

FIRST-ORDER AND SECOND-ORDER BREAKAGE RATE OF COARSE PARTICLES IN BALL MILL GRINDING

FIRST-ORDER AND SECOND-ORDER BREAKAGE RATE OF COARSE PARTICLES IN BALL MILL GRINDING Physicochem. Probl. Miner. Process. 52(1), 2016, 268 278 www.minproc.pwr.wroc.pl/journal/ Physicochemical Problems of Mineral Processing ISSN 1643-1049 (print) ISSN 2084-4735 (online) Received February

More information

SST3005 Fundamentals of Soil Science LAB 5 LABORATORY DETERMINATION OF SOIL TEXTURE: MECHANICAL ANALYSIS

SST3005 Fundamentals of Soil Science LAB 5 LABORATORY DETERMINATION OF SOIL TEXTURE: MECHANICAL ANALYSIS LAB 5 LABORATORY DETERMINATION OF SOIL TEXTURE: MECHANICAL ANALYSIS Learning outcomes The student is able to: 1. Separate soil particles : sand, silt and clay 2. determine the soil texture class using

More information

Data requirements for reactor selection. Professor John H Atherton

Data requirements for reactor selection. Professor John H Atherton Data requirements for reactor selection Professor John H Atherton What is my best option for manufacturing scale? Microreactor Mesoscale tubular reactor Tubular reactor OBR (oscillatory baffled flow reactor)

More information

A First Course on Kinetics and Reaction Engineering Unit 33. Axial Dispersion Model

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

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

Introduction to Mechanical Process Engineering WS 2013/2014

Introduction to Mechanical Process Engineering WS 2013/2014 Introduction to Mechanical rocess Engineering WS 2013/2014 rof. Dr.-Ing. Rolf Gimbel - FOR ERSONAL USE ONLY! - Institut für Energieund Umwelterfahrenstechnik (EUT) Department of rocess Engineering / Water

More information

RADIAL AND AXIAL MIXING OF PARTICLES IN A DRY BATCH BALL MILL

RADIAL AND AXIAL MIXING OF PARTICLES IN A DRY BATCH BALL MILL RADIAL AND AXIAL MIXING OF PARTICLES IN A DRY BATCH BALL MILL Clement Chibwana A dissertation submitted to the Faculty of Engineering and Built Environment, University of the Witwatersrand, Johannesburg,

More information

Tendency of blends for segregation

Tendency of blends for segregation Tendency of blends for segregation How to study it? Methods for measuring the segregation potential Louk Peffer 1 Outline/Themes Blends unmix Theory or reality Visual inspection Segregation mechanisms

More information

SOLAR ROCKET PROPULSION Ground and Space Technology Demonstration. Dr. Michael Holmes, AFRL/PRSS

SOLAR ROCKET PROPULSION Ground and Space Technology Demonstration. Dr. Michael Holmes, AFRL/PRSS SOLAR ROCKET PROPULSION Ground and Space Technology Demonstration Dr. Michael Holmes, AFRL/PRSS Solar Thermal Propulsion Concept Parabolic Mirror Sun Create thrust by collecting and focusing sunlight to

More information

Process Simulations Using Computer Technology. Steve Frankland Dargo Associates Ltd

Process Simulations Using Computer Technology. Steve Frankland Dargo Associates Ltd Process Simulations Using Computer Technology Steve Frankland Dargo Associates Ltd What is a Process Simulations? Mathematical prediction of the outcome of a physical or chemical process Linking of several

More information

Review: Nonideal Flow in a CSTR

Review: Nonideal Flow in a CSTR L3- Review: Nonideal Flow in a CSTR Ideal CSTR: uniform reactant concentration throughout the vessel Real stirred tank Relatively high reactant concentration at the feed entrance Relatively low concentration

More information

Modeling of Mixing in The Liquid Phase For Bubble Column

Modeling of Mixing in The Liquid Phase For Bubble Column Eng. & Tech. Journal, Vol.27, No.10, 2009 Phase For Bubble Column Abstract Dr.Ali H. Jawad* Received on:10/11/2008 Accepted on:5/3/2009 Hydrodynamic characteristics (mixing in the liquid phase) in a bubble

More information

Continuous Flow Reactions. From idea to production size scale up in 3 steps

Continuous Flow Reactions. From idea to production size scale up in 3 steps Continuous Flow Reactions From idea to production size scale up in 3 steps PIN NL Spring Session 13 04 2017 13 4 2017 PIN NL Spring Session 1 Topics Introduction Flowlink Continuous Flow Reactions What

More information

POE Concepts and Learning Objectives

POE Concepts and Learning Objectives POE Concepts and Learning Objectives Unit 1 Energy and Power Time Days: 49 days Lesson 1.1 Mechanisms (15 days): 1. Engineers and engineering technologists apply math, science, and disciplinespecific skills

More information

5. Collection and Analysis of. Rate Data

5. Collection and Analysis of. Rate Data 5. Collection and nalysis of o Objectives Rate Data - Determine the reaction order and specific reaction rate from experimental data obtained from either batch or flow reactors - Describe how to analyze

More information

AMRITA VISHWA VIDYAPEETHAM DEPARTMENT OF CHEMICAL ENGINEERING AND MATERIALS SCIENCE. PhD Entrance Examination - Syllabus

AMRITA VISHWA VIDYAPEETHAM DEPARTMENT OF CHEMICAL ENGINEERING AND MATERIALS SCIENCE. PhD Entrance Examination - Syllabus AMRITA VISHWA VIDYAPEETHAM DEPARTMENT OF CHEMICAL ENGINEERING AND MATERIALS SCIENCE PhD Entrance Examination - Syllabus The research being carried out in the department of Chemical Engineering & Materials

More information

S.E. (Chemical) (Second Semester) EXAMINATION, 2011 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100

S.E. (Chemical) (Second Semester) EXAMINATION, 2011 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100 Total No. of Questions 12] [Total No. of Printed Pages 7 [4062]-186 S.E. (Chemical) (Second Semester) EXAMINATION, 2011 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100 N.B. : (i) Answers

More information

Population Balance Modeling

Population Balance Modeling Population Balance Modeling JMBC-Particle Technology 2015 Pieter Vonk Advanced Chemical Engineering Solutions March 6 th, 2015 Overview Introduction & Industrial challenges Granulation processes Crystallization

More information

Biological Process Engineering An Analogical Approach to Fluid Flow, Heat Transfer, and Mass Transfer Applied to Biological Systems

Biological Process Engineering An Analogical Approach to Fluid Flow, Heat Transfer, and Mass Transfer Applied to Biological Systems Biological Process Engineering An Analogical Approach to Fluid Flow, Heat Transfer, and Mass Transfer Applied to Biological Systems Arthur T. Johnson, PhD, PE Biological Resources Engineering Department

More information

Models for Nonideal Reactors

Models for Nonideal Reactors Fogler_ECRE_CDROM.book Page 945 Wednesday, September 17, 8 5:1 PM Models for Nonideal Reactors 14 Success is a journey, not a destination. Ben Sweetland Use the RTD to evaluate parameters Overview Not

More information

POSITION R & D Officer M.Tech. No. of questions (Each question carries 1 mark) 1 Verbal Ability Quantitative Aptitude Test 34

POSITION R & D Officer M.Tech. No. of questions (Each question carries 1 mark) 1 Verbal Ability Quantitative Aptitude Test 34 POSITION R & D Officer M.Tech Candidates having M.Tech / M.E. Chemical Engg. with 60% marks (aggregate of all semesters/years) and 50% for SC/ST/PWD are being called for Computer Based Test basis the information

More information

429 LIGHT DIFFRACTION MEASUREMENT OF PARTICLE SIZE

429 LIGHT DIFFRACTION MEASUREMENT OF PARTICLE SIZE Search USP29 429 LIGHT DIFFRACTION MEASUREMENT OF PARTICLE SIZE Light diffraction is one of the most widely used techniques for measuring the size of a wide range of particles from very fine to very coarse.

More information

Chemical Reaction Engineering. Multiple Reactions. Dr.-Eng. Zayed Al-Hamamre

Chemical Reaction Engineering. Multiple Reactions. Dr.-Eng. Zayed Al-Hamamre Chemical Reaction Engineering Multiple Reactions Dr.-Eng. Zayed Al-Hamamre 1 Content Types of Reactions Selectivity Reaction Yield Parallel Reactions Series Reactions Net Rates of Reaction Complex Reactions

More information

An Introduction to Pharmaceutical & Chemical Process Technology. Paul Ashall

An Introduction to Pharmaceutical & Chemical Process Technology. Paul Ashall An Introduction to Pharmaceutical & Chemical Process Technology Paul Ashall Aspects of Industrial Chemical Processes Products Types of process Flowsheets Mass balances Energy balances Heat transfer and

More information

Continuous, efficient multistage extraction

Continuous, efficient multistage extraction Continuous, efficient multistage extraction Andrea Adamo Zaiput Flow Technologies Department of Chemical Engineering, MIT Munich 01 February 2017 Back ground - MIT s efforts in continuous manufacturing

More information

Advanced Transport Phenomena Module 6 - Lecture 28

Advanced Transport Phenomena Module 6 - Lecture 28 Mass Transport: Non-Ideal Flow Reactors Advanced Transport Phenomena Module 6 - Lecture 28 Dr. R. Nagarajan Professor Dept of Chemical Engineering IIT Madras 1 Simplest approach: apply overall material/

More information

SEDIMENTATION INTRODUCTION

SEDIMENTATION INTRODUCTION SEDIMENTATION INTRODUCTION Sedimentation is removal of particulate materials suspended in water by quiescent settling due to gravity Commonly used unit operation in water and wastewater treatment plants

More information

1. Introductory Material

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

More information

MODELING OF CONTINUOUS OSCILLATORY BAFFLED REACTOR FOR BIODIESEL PRODUCTION FROM JATROPHA OIL ABSTRACT

MODELING OF CONTINUOUS OSCILLATORY BAFFLED REACTOR FOR BIODIESEL PRODUCTION FROM JATROPHA OIL ABSTRACT MODELING OF CONTINUOUS OSCILLATORY BAFFLED REACTOR FOR BIODIESEL PRODUCTION FROM JATROPHA OIL B. K. Highina, I. M. Bugaje & B. Gutti Department of Chemical Engineering University of Maiduguri, Borno State,

More information

Principles Of Engineering Detailed Outline

Principles Of Engineering Detailed Outline Principles Of Engineering Detailed Outline Unit 1 Energy and Power Time Days: 115 days Lesson 1.0 Introduction to POE (15 days) 1. Introduction to classroom expectations, Engineering notebook, Pretest

More information

Analyzing Mass and Heat Transfer Equipment

Analyzing Mass and Heat Transfer Equipment Analyzing Mass and Heat Transfer Equipment (MHE) Analyzing Mass and Heat Transfer Equipment Scaling up to solving problems using process equipment requires both continuum and macroscopic knowledge of transport,

More information

Distributed Parameter Systems

Distributed Parameter Systems Distributed Parameter Systems Introduction All the apparatus dynamic experiments in the laboratory exhibit the effect known as "minimum phase dynamics". Process control loops are often based on simulations

More information

Heat Transfer Performance in Double-Pass Flat-Plate Heat Exchangers with External Recycle

Heat Transfer Performance in Double-Pass Flat-Plate Heat Exchangers with External Recycle Journal of Applied Science and Engineering, Vol. 17, No. 3, pp. 293 304 (2014) DOI: 10.6180/jase.2014.17.3.10 Heat Transfer Performance in Double-Pass Flat-Plate Heat Exchangers with External Recycle Ho-Ming

More information

Chemical Reaction Engineering - Part 16 - more reactors Richard K. Herz,

Chemical Reaction Engineering - Part 16 - more reactors Richard K. Herz, Chemical Reaction Engineering - Part 16 - more reactors Richard K. Herz, rherz@ucsd.edu, www.reactorlab.net More reactors So far we have learned about the three basic types of reactors: Batch, PFR, CSTR.

More information

Lecture 7. Sorption-Separation Equipment

Lecture 7. Sorption-Separation Equipment Lecture 7. Sorption-Separation Equipment Adsorption - Stirred-tank, slurry operation - Cyclic fixed-bed batch operation - Thermal (temperature)-swing adsorption - Fluidizing bed for adsorption and moving

More information

LECTURE 8. Hydraulic machines and systems II 2002 MIT PSDAM LAB

LECTURE 8. Hydraulic machines and systems II 2002 MIT PSDAM LAB LECTURE 8 Hydraulic machines and systems II Basic hydraulic machines & components Graphical Nomenclature Arrows show direction of flow Control Volume Pipe or hose with fluid flow Pipe or hose without fluid

More information

Prozess Investigation

Prozess Investigation Radiotracer in Prozess Investigation Fraunhofer Institute for Nondestructive Testing Dresden Dr. rer. nat. habil. Albert Zeuner Fraunhofer IZFP-D Maria-Reiche-Straße 2 D-01109 Dresden +49(0)351 / 888 15-611

More information

ANALYSIS OF LOW DENSITY PARTICLES USING DIFFERENTIAL CENTRIFUGAL SEDIMENTATION

ANALYSIS OF LOW DENSITY PARTICLES USING DIFFERENTIAL CENTRIFUGAL SEDIMENTATION ANALYSIS OF LOW DENSITY PARTICLES USING DIFFERENTIAL CENTRIFUGAL SEDIMENTATION Conventional Centrifugal Methods Centrifugal sedimentation of particles suspended in a fluid is a well known method (1, 2)

More information

Polymer Applications Understanding Polymer Activation. Presented by Rich Hopkins February 15, 2011

Polymer Applications Understanding Polymer Activation. Presented by Rich Hopkins February 15, 2011 Polymer Applications Understanding Polymer Activation Presented by Rich Hopkins February 15, 2011 Why Polymer? Helping particles settle faster Improving liquid/solid separation Some Applications Clarifiers

More information

Mixing of Liquids in Microfluidic Devices

Mixing of Liquids in Microfluidic Devices Mixing of Liquids in Microfluidic Devices Bruce A. Finlayson Professor Emeritus of Chemical Engineering University of Washington http://courses.washington.edu/microflo/ The mixing of liquids in eleven

More information

These subclasses are to be used according to the following general rules:

These subclasses are to be used according to the following general rules: CPC - B03D - 2017.08 B03D FLOTATION; DIFFERENTIAL SEDIMENTATION (sedimentation in general B01D 21/00; in combination with other separation of solids B03B; sink-float separation B03B 5/28; detergents, soaps

More information

Design and Optimisation of Batch Reactors

Design and Optimisation of Batch Reactors Design and Optimisation of Batch Reactors Jinzhong Zhang Supervisor: Professor Robin Smith 2-1 XVII PIRC Annual Research Meeting 2000 In recent years, a methodology has been developed for the systematic

More information

Detailed numerical investigations of two-phase flow and transport. narrow channels. Dr.-Ing. Martin Wörner. Institut für Kern- und Energietechnik

Detailed numerical investigations of two-phase flow and transport. narrow channels. Dr.-Ing. Martin Wörner. Institut für Kern- und Energietechnik Detailed numerical investigations of two-phase flow and transport INSTITUT phenomena FÜR KERN- UND ENERGIETECHNIK in narrow channels Dr.-Ing. Martin Wörner Opening Workshop Helmholtz Research School Energy-Related

More information

Technical Resource Package 1

Technical Resource Package 1 Technical Resource Package 1 Green Chemistry Impacts in Batch Chemical Processing UNIDO IAMC Toolkit Images may not be copied, transmitted or manipulated 1/5 The following list provides an overview of

More information

Recent developments in modelling of industrial dryers Ian C Kemp Process Manual Product Manager, Hyprotech, AEA Technology plc, Harwell, UK

Recent developments in modelling of industrial dryers Ian C Kemp Process Manual Product Manager, Hyprotech, AEA Technology plc, Harwell, UK Recent developments in modelling of industrial dryers Ian C Kemp Process Manual Product Manager, Hyprotech, AEA Technology plc, Harwell, UK Magdeburg - Slide 1 Scientific Approach to Dryer Design Overall

More information

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

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

More information

1) Batching Methods (Add Weigh or Loss In Weight) based on batch dispensing time, time between batches, head room, floor space, accuracy and budget.

1) Batching Methods (Add Weigh or Loss In Weight) based on batch dispensing time, time between batches, head room, floor space, accuracy and budget. Batching Batching Product Overview SELECTION DECISIONS 1) Batching Methods (Add Weigh or Loss In Weight) based on batch dispensing time, time between batches, head room, floor space, accuracy and budget.

More information

Axial profiles of heat transfer coefficients in a liquid film evaporator

Axial profiles of heat transfer coefficients in a liquid film evaporator Axial profiles of heat transfer coefficients in a liquid film evaporator Pavel Timár, Ján Stopka, Vladimír Báleš Department of Chemical and Biochemical Engineering, Faculty of Chemical and Food Technology,

More information

MODIFYING GELDART CLASSIFICATION FOR VARIOUS COHESION FORCES

MODIFYING GELDART CLASSIFICATION FOR VARIOUS COHESION FORCES 18th International Conference on TRANSPORT AN SEIMENTATION OF SOLI PARTICLES 11-15 September 2017, Prague, Czech Republic ISSN 0867-7964 ISBN 978-83-7717-269-8 MOIFYING GELART CLASSIFICATION FOR VARIOUS

More information

Water Pollution Control: Physical Methods. AWPPCE RPI Fall 2013

Water Pollution Control: Physical Methods. AWPPCE RPI Fall 2013 Water Pollution Control: Physical Methods AWPPCE RPI Fall 2013 Water Pollution Control Processes Water and Waste Water Treatment are usually carried out in specially designed vessels (reactors) under controlled

More information

3 Types of Heat Transfer

3 Types of Heat Transfer 3 Types of Heat Transfer The movement of heat from a warmer object to a cooler object. Heat Transfer- 1. Conduction Heat transfer by direct contact of molecules. In other words, when one molecule runs

More information

Process Design Decisions and Project Economics Prof. Dr. V. S. Moholkar Department of Chemical Engineering Indian Institute of Technology, Guwahati

Process Design Decisions and Project Economics Prof. Dr. V. S. Moholkar Department of Chemical Engineering Indian Institute of Technology, Guwahati Process Design Decisions and Project Economics Prof. Dr. V. S. Moholkar Department of Chemical Engineering Indian Institute of Technology, Guwahati Module - 2 Flowsheet Synthesis (Conceptual Design of

More information

ON THE CONDITIONS OF CLOGGING IN A HYDROCYCLONE. Dueck, Johann 1,2

ON THE CONDITIONS OF CLOGGING IN A HYDROCYCLONE. Dueck, Johann 1,2 ISBN 978-83-9784-8-3 ISSN 867-7964 ON THE CONDITIONS OF CLOGGING IN A HYDROCYCLONE Dueck, Johann 1, 1) L.N. Gumilyov Eurasian National University, Republic of Kazakhstan, ) Friedrich-Alexander, Universität

More information

Chemical Reaction Engineering

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

More information

Chemistry Instrumental Analysis Lecture 31. Chem 4631

Chemistry Instrumental Analysis Lecture 31. Chem 4631 Chemistry 4631 Instrumental Analysis Lecture 31 High Performance Liquid Chromatography (HPLC) High Performance Liquid Chromatography (HPLC) High Performance Liquid Chromatography (HPLC) Solvent Delivery

More information

Year 8 Tracking Document. Year 8 Science National Curriculum. Health and Lifestyle

Year 8 Tracking Document. Year 8 Science National Curriculum. Health and Lifestyle Health and Lifestyle Describe the components of a healthy diet Explain the role of each food group in the body Describe the test for starch, lipids, sugar and proteins Describe the positive test for each

More information

R13 SET - 1 '' ''' '' ' '''' Code No RT21033

R13 SET - 1 '' ''' '' ' '''' Code No RT21033 SET - 1 II B. Tech I Semester Supplementary Examinations, June - 2015 THERMODYNAMICS (Com. to ME, AE, AME) Time: 3 hours Max. Marks: 70 Note: 1. Question Paper consists of two parts (Part-A and Part-B)

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

Liquid Liquid Extraction

Liquid Liquid Extraction Liquid Liquid Extraction By Dr. Salih Rushdi 1 Introduction Liquid-liquid extraction (sometimes abbreviated LLX) is a mass transfer operation in which a solution (called the feed which is a mixture of

More information

Forced Convection: Inside Pipe HANNA ILYANI ZULHAIMI

Forced Convection: Inside Pipe HANNA ILYANI ZULHAIMI + Forced Convection: Inside Pipe HANNA ILYANI ZULHAIMI + OUTLINE u Introduction and Dimensionless Numbers u Heat Transfer Coefficient for Laminar Flow inside a Pipe u Heat Transfer Coefficient for Turbulent

More information

Review of Fluid Mechanics

Review of Fluid Mechanics Chapter 3 Review of Fluid Mechanics 3.1 Units and Basic Definitions Newton s Second law forms the basis of all units of measurement. For a particle of mass m subjected to a resultant force F the law may

More information