Block Flow Chart of a Typical Particle Processing System
|
|
- Earl Payne
- 6 years ago
- Views:
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 Jaime Benitez iwiley- INTERSCIENCE A JOHN WILEY & SONS, INC., PUBLICATION Preface Nomenclature xiii xv 1. FUNDAMENTALS OF MASS TRANSFER 1
More informationNirma 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 informationName 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 informationBAE 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 informationBASIC 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 informationChemical 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 informationTechnical 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 informationRADIOTRACER 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 informationAIRLIFT 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 informationGUJARAT 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 informationResidence 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 informationUSING 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 informationATOMISATION 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 informationHEAT 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 informationAttention 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 informationContents. 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 informationTypes 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 informationProcess 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 informationLace 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 informationDevelopment 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 informationAdsorption 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 informationChapter 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 informationLecture (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 informationCHEMICAL 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 informationFill 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 informationA 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 informationDEPARTMENT 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 informationUpdating 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 informationChemical 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 informationStudy 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 informationModels 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 informationChapter 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 informationSCANNING-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 informationDiffusion 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 informationPREFACE. 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 informationIDEAL 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 informationSpecific 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 informationTHINK 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 informationNon-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 informationFIRST-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 informationSST3005 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 informationData 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 informationA 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 informationTABLE 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 informationIntroduction 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 informationRADIAL 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 informationTendency 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 informationSOLAR 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 informationProcess 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 informationReview: 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 informationModeling 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 informationContinuous 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 informationPOE 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 information5. 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 informationAMRITA 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 informationS.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 informationPopulation 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 informationBiological 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 informationModels 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 informationPOSITION 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 information429 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 informationChemical 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 informationAn 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 informationContinuous, 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 informationAdvanced 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 informationSEDIMENTATION 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 information1. 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 informationMODELING 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 informationPrinciples 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 informationAnalyzing 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 informationDistributed 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 informationHeat 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 informationChemical 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 informationLecture 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 informationLECTURE 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 informationProzess 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 informationANALYSIS 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 informationPolymer 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 informationMixing 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 informationThese 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 informationDesign 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 informationDetailed 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 informationTechnical 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 informationRecent 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 informationEngineering 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 information1) 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 informationAxial 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 informationMODIFYING 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 informationWater 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 information3 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 informationProcess 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 informationON 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 informationChemical 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 informationChemistry 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 informationYear 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 informationR13 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 informationEngineering. 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 informationLiquid 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 informationForced 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 informationReview 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