Gilliland Correlation for Actual Reflux Ratio and Theoretical Stages Feed-Stage Location
|
|
- Gervase Curtis
- 5 years ago
- Views:
Transcription
1 Lecture 4. Approximate Multicomponent Methods (2) [Ch. 9] Minimum Reflux - In binary systems - In multicomponent systems - Underwood equation Gilliland Correlation for Actual Reflux Ratio and Theoretical Stages -Stage Location Distribution of Nonkey Components at Actual Reflux
2 Minimum Reflux in Binary Systems Minimum reflux - Infinite stages - Pinch point (or point of infinitude) - Most of the stages are crowded into a constant-composition composition zone Binary system, ideal conditions Binary system, nonideal conditions : location of pinch-point zone
3 Minimum Reflux in Multicomponent Systems Class (one pinch point): all components in the feed distribute to both the distillate and bottoms products (narrow-boiling-range range mixtures or the degree of separation between key components is not sharp) Class 2 (two pinch points): one or more of the components appear in only one product All components Not all LLK and HHK distributed (Class ) distributing (Class 2) All LLK, if any, distributing, but not all HHK distributing (Class 2) LLK: lighter than light key; HHK: heavier than heavy key : location of pinch-point zones
4 Underwood Equation for Minimum Reflux () Material balance over all stages y V x L x D i, i, i, D V L D y V x L x D j, j, j, D Phase equilibrium relation (phase compositions do not change in the pinch zone) y K x y K x i, i, i, j, j, j, V L D L D ( x id, / xi, ) ( ij, ) ( xjd, / xj, ) ( ) i, j Pinch-point zone or Class separation, flashed feed- and pinch-zone compositions are identical ( x i, xi, ) ( L ) LK, HK V L ( L / ) ( DxLK, D/ Lx LK, ) ( LK, HK) ( DxHK, D/ Lx HK, ) ( )
5 Underwood Equation for Minimum Reflux (2) Distribution of nonkey components ( L ) ( L / ) ( DxLK, D / LxLK, ) ( LK, HK) ( DxHK, D / LxHK, ) ( ) Replace LK with component i LK, HK ( L ) ( L / ) ( Dxi, D / Lxi, ) ( i, HK) ( DxHK, D / Lx HK, ) ( ) ihk, Dx id, ( ihk, ) Dx LKD, ( LKHK, ) ( ihk, ) Dx HKD, Lxi, ( LK, HK) Lx LK, ( LK, HK) Lx HK, Dx id, 0 x i, or all nonkey components in a Class separation
6 Gilliland Correlation for Actual Reflux Ratio and Theoretical Stages Gilliland correlation : empirical correlation N N{ N ( x, x, ), R ( z, x, q, ), R} Y X N N N id, ib, i, id, 544. X X exp X X R R R The value of N includes one stage for a partial reboiler and one stage for a partial condenser, if used A small initial i i increase in R above R causes a large decrease in N, but further changes in R have a much smaller effect on N
7 -Stage Location Suggestion of Brown and Martin (939) - Based on the enske equation (at total reflux conditions) - Not reliable except for fairly symmetrical feeds and separations N N R S ( NR) ( N ) S / 2 log ( xlk, D / zlk, )( zhk, / xhk, D ) log[( B ) ] / 2 log ( zlk, / xlk, B )( xhk, B / zhk, ) log[( D ) ] Empirical equation of Kirkbride 2 N z R HK, x LK, B B NS z LK, x HK, D D N R N S
8 Distribution of Nonkey Components or multicomponent mixtures at Actual Reflux - Total reflux condition: all components distribute to some extent between distillate and bottoms - Minimum reflux condition: none or only a few of the nonkey components distribute - Reflux ratio near imum: the product distribution lies between the two limits - High reflux ratio: the product distribution may lie outside the limits inferior separation
Approximate Methods Fenske-Underwood-Gilliland (FUG) Method Selection of Two Key Components
Lecture 3. Approximate Multicomponent Methods () [Ch. 9] Approximate Methods Fenske-Underwood-Gilliland (FUG) Method Selection of Two Key Components Column Operating Pressure Fenske Equation for Minimum
More informationAll Rights Reserved. Armando B. Corripio, PhD, P.E., Multicomponent Distillation Column Specifications... 2
Multicomponent Distillation All Rights Reserved. Armando B. Corripio, PhD, P.E., 2013 Contents Multicomponent Distillation... 1 1 Column Specifications... 2 1.1 Key Components and Sequencing Columns...
More informationVapor-liquid Separation Process MULTICOMPONENT DISTILLATION
Vapor-liquid Separation Process MULTICOMPONENT DISTILLATION Outline: Introduction to multicomponent distillation Phase Equilibria in Multicomponent Distillation (Pg. 737) Bubble-point and dew-point calculation
More informationShortcut Design Method for Columns Separating Azeotropic Mixtures
3908 Ind. Eng. Chem. Res. 2004, 43, 3908-3923 Shortcut Design Method for Columns Separating Azeotropic Mixtures Guilian Liu, Megan Jobson,*, Robin Smith, and Oliver M. Wahnschafft Department of Process
More informationMODULE 5: DISTILLATION
MOULE 5: ISTILLATION LECTURE NO. 3 5.2.2. Continuous distillation columns In contrast, continuous columns process a continuous feed stream. No interruptions occur unless there is a problem with the column
More informationShortcut Distillation. Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia
Shortcut Distillation Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia The use of separation column in HYSYS The column utilities in HYSYS can be used to model a wide variety of
More informationAn Efficient Design of Multi Component Distillation Column by Approximate & Rigorous Method
An Efficient Design of Multi Component Distillation Column by Approximate & Rigorous Method Syed Mujahed Ali Rizwan Senior Lecturer in Chemistry Challenger College, Moinabad, Hyderabad. Abstract: In this
More information[Thirumalesh*, 4.(8): August, 2015] ISSN: (I2OR), Publication Impact Factor: 3.785
IJESRT INTERNATIONAL JOURNAL OF ENGINEERING SCIENCES & RESEARCH TECHNOLOGY CASE STUDY ON MULTICOMPONENT DISTILLATION AND DISTILLATION COLUMN SEQUENCING Thirumalesh. B.S*, Ramesh.V * Assistant Professor
More information01/12/2009. F. Grisafi
Multicomponent distillation F. Grisafi 1 Introduction The problem of determining the stage and reflux requirements for multicomponent t distillations is much more complex than for binary mixtures. With
More informationAzeotropic Distillation Methods. Dr. Stathis Skouras, Gas Processing and LNG RDI Centre Trondheim, Statoil, Norway
Azeotropic Distillation Methods Dr. Stathis Skouras, Gas Processing and LNG RDI Centre Trondheim, Statoil, Norway Schedule Tuesday 1/12/2015: 09.45 12.30: Lecture - Natural Gas Processing 14.00 17.00:
More informationAvailable online Journal of Scientific and Engineering Research, 2018, 5(2): Research Article
Available online www.jsaer.com, 2018, 5(2):32-39 Research Article ISSN: 2394-2630 CODEN(USA): JSERBR A Shortcut Method for Modeling Multi-Component Distillation in an Existing Column Philomena K. Igbokwe
More informationReflections on the use of the McCabe and Thiele method
From the Selectedorks of João F Gomes January 2007 Reflections on the use of the McCabe and Thiele method Contact Author Start Your Own Selectedorks Notify Me of New ork Available at: http://works.bepress.com/joao_gomes/42
More informationBOUNDARY VALUE DESIGN METHOD FOR COMPLEX DEMETHANIZER COLUMNS
Distillation Absorption 2010 A.B. de Haan, H. Kooijman and A. Górak (Editors) All rights reserved by authors as per DA2010 copyright notice BOUNDARY AUE DESIGN METHOD FOR COMPEX DEMETHANIZER COUMNS Muneeb
More informationPhase Separation Degree of Freedom Analysis. Binary Vapor-Liquid Systems. Azeotropic Systems. - Gibbs phase rule F C P 2 -General analysis
Lecture 5. Single Equilibrium Stages (1) Phase Separation [Ch. 4] Degree of Freedom Analysis - Gibbs phase rule F CP2 -General analysis Binary Vapor-Liquid Systems - Examples of binary system - Phase equilibrium
More informationEXTENDED SMOKER S EQUATION FOR CALCULATING NUMBER OF STAGES IN DISTILLATION
EXTENDED SMOKER S EQUATION FOR CALCULATING NUMBER OF STAGES IN DISTILLATION Santanu Bandyopadhyay Energy Systems Engineering and Department of Mechanical Engineering, Indian Institute of Technology, Bombay,
More informationDETERMINATION OF OPTIMAL ENERGY EFFICIENT SEPARATION SCHEMES BASED ON DRIVING FORCES
DETERMINATION OF OPTIMAL ENERGY EFFICIENT SEPARATION SCHEMES BASED ON DRIVING FORCES Abstract Erik Bek-Pedersen, Rafiqul Gani CAPEC, Department of Chemical Engineering, Technical University of Denmark,
More informationTHERMAL INTEGRATION OF A DISTILLATION COLUMN THROUGH SIDE-EXCHANGERS
THERMAL INTEGRATION OF A DISTILLATION COLUMN THROUGH SIDE-EXCHANGERS Santanu Bandyopadhyay Energy Systems Engineering and Department of Mechanical Engineering, Indian Institute of Technology, Bombay, Powai,
More informationMODULE 5: DISTILLATION
MODULE 5: DISTILLATION LECTURE NO. 5 Determination of the stripping section operating line (SOL): The stripping section operating line (SOL) can be obtained from the ROL and q- line without doing any material
More informationChapter 4. Problem SM.7 Ethylbenzene/Styrene Column
Background Chapter 4. Problem SM.7 Ethylbenzene/Styrene Column In Problem SM.6 of the HYSYS manual, a modified form of successive substitution, called the Wegstein method, was used to close the material
More informationDISTILLATION. Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation
25 DISTILLATION Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation Distillation refers to the physical separation of a mixture into two or more fractions that have different
More informationLevel 4: General structure of separation system
Level 4: General structure of separation system Cheng-Ching Yu Dept of Chem. Eng. National Taiwan University ccyu@ntu.edu.tw 02-3365-1759 1 Separation Systems Typical reaction/separation structure Remark:
More informationAzeotropic distillation Example 1
Azeotropic distillation Example 1 Separate water from iso-butanol. The phase behavior for this mixture is interesting. There is a minimum boiling azeotrope formed as well as a liquid-liquid phase separation
More informationDesign and Analysis of Divided Wall Column
Proceedings of the 6th International Conference on Process Systems Engineering (PSE ASIA) 25-27 June 2013, Kuala Lumpur. Design and Analysis of Divided Wall Column M. Shamsuzzoha, a* Hiroya Seki b, Moonyong
More informationPlacement and Integration of Distillation column Module 06 Lecture 39
Module 06: Integration and placement of equipment Lecture 39: Placement and Integration of Distillation Column Key word: Pinch Technology, Pinch technology has established that good process integration
More informationAbsorption/Stripping
Absorption/Stripping Gas-liquid separation processes (Ch. 10) Cooling (condenser) Feed A+B Distillation(Ch.11) Absorption (Ch.10) Stripping (Ch.10) B COUNTER-CURRENT MULTISTAGE CONTACT OF GAS AND LIQUID
More informationThe most important nomenclature used in this report can be summarized in:
Notation The most important nomenclature used in this report can be summarized in: V Vapor flow rate V T Vapor flow rate in the top L Liquid flow rate D Distillation product B Bottom product q Liquid fraction
More informationNOTICE WARNING CONCERNING COPYRIGHT RESTRICTIONS: The copyright law of the United States (title 17, U.S. Code) governs the making of photocopies or
NOTICE WARNING CONCERNING COPYRIGHT RESTRICTIONS: The copyright law of the United States (title 17, U.S. Code) governs the making of photocopies or other reproductions of copyrighted material. Any copying
More informationDistillation. Sep-tek. Ch.11 (continued) Distillation (Multistage with reflux) Sigurd Skogestad. Separation of liquid mixtures by repeated evaporation
Sep-tek. Ch.11 (continued) Distillation (Multistage with reflux) Sigurd Skogestad Distillation Separation of liquid mixtures by repeated evaporation multi-stage with reflux Old name: Rectification Basis:
More informationMinimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements
616 Ind. Eng. Chem. Res. 2003, 42, 616-629 Minimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements Ivar J. Halvorsen and Sigurd Skogestad*
More informationMass Transfer Operations I Prof. BishnupadaMandal Department of Chemical Engineering Indian Institute of Technology, Guwahati
Mass Transfer Operations I Prof. BishnupadaMandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module -5 Distillation Lecture - 8 Fractional Distillation: Subcooled Reflux,
More informationIV Distillation Sequencing
IV Distillation Sequencing Outline 1. Basic Concepts of Distillation Sequence Design 2. Choice of Sequence and its Operating Pressure. 3. Performance of Distillation Column (Sieve tray and packed tower)
More informationSimulation and Analysis of Ordinary Distillation of Close Boiling Hydrocarbons Using ASPEN HYSYS
International Journal of Innovation and Applied Studies ISSN 2028-9324 Vol. 16 No. 4 Jun. 2016, pp. 805-813 2016 Innovative Space of Scientific Research Journals http://www.ijias.issr-journals.org/ Simulation
More informationSteady State Multiplicity and Stability in a Reactive Flash
Steady State Multiplicity and Stability in a Reactive Flash Iván E. Rodríguez, Alex Zheng and Michael F. Malone Department of Chemical Engineering University of Massachusetts Amherst, MA 01003 Abstract
More informationMass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati
Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module - 5 Distillation Lecture - 5 Fractional Distillation Welcome to the
More informationSIMULATION ANALYSIS OF FULLY THERMALLY COUPLED DISTILLATION COLUMN
Int. J. Chem. Sci.: 14(3), 2016, 1621-1632 ISSN 0972-768X www.sadgurupublications.com SIMULATION ANALYSIS OF FULLY THERMALLY COUPLED DISTILLATION COLUMN ASMITA PRAVIN PATIL * and S. M. JADHAV Chemical
More informationSeparation Trains Azeotropes. S,S&L Chapter 9.5 Terry A. Ring Chemical Engineering University of Utah
Separation Trains Azeotropes S,S&L Chapter 9.5 Terry A. Ring Chemical Engineering University of Utah Distillation Recycle Loops Closing Recycle Loops Matrix Mathematics Without Recycle Loop [P] x = y Straight
More informationPRINCIPLES 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 informationEffect of feed on optimal thermodynamic performance of a distillation column
Effect of feed on optimal thermodynamic performance of a distillation column Santanu Bandyopadhyay Energy Systems Engineering, Department of Mechanical Engineering, Indian Institute of Technology, Powai,
More informationOpen Archive Toulouse Archive Ouverte
Open Archive Toulouse Archive Ouverte OATAO is an open access repository that collects the work of Toulouse researchers and makes it freely available over the web where possible This is an author s version
More informationDistilla l tion n C olum u n
Distillation Column Distillation: Process in which a liquid or vapour mixture of two or more substances is separated into its component fractions of desired purity, by the application and removal of heat
More informationMinimum Energy Consumption in Multicomponent Distillation: III: Generalized Petlyuk Arrangements with more than Three Products
Minimum Energy Consumption in Multicomponent istillation: III: Generalized Petlyuk rrangements with more than Three Products Ivar J. Halvorsen and Sigurd Skogestad Norwegian University of Science and Technology,
More informationDistillation. JAMES R. FAIR Department of Chemical Engineering The University of Texas Austin, Texas. 5.1 INTRODUCTION 5.
PART Il I N D I V I D U A L S E P A R A T I O N P R O C E S S E S C H A P T E R 5 Distillation JAMES R. FAIR Department of Chemical Engineering The University of Texas Austin, Texas 5.1 INTRODUCTION 5.M
More informationDividing wall columns for heterogeneous azeotropic distillation
Dividing wall columns for heterogeneous azeotropic distillation Quang-Khoa Le 1, Ivar J. Halvorsen 2, Oleg Pajalic 3, Sigurd Skogestad 1* 1 Norwegian University of Science and Technology (NTNU), Trondheim,
More informationMass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati
Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module - 5 Distillation Lecture - 6 Fractional Distillation: McCabe Thiele
More informationGeneral approach separation
Summary septek Sigurd s part Equilibrium Flash Distillation Absorption/stripping Extraction Process control General approach separation 1. Overall material balance. What are the desired products? 2. Choose
More informationDistillation of a Complex Mixture. Part I: High Pressure Distillation Column Analysis: Modeling and Simulation
Entropy, 2007, 9, 58-72 Full Research Paper entropy ISS 099-4300 2007 by MDPI wwwmdpiorg/entropy Distillation of a Complex Mixture Part I: High Pressure Distillation Column Analysis: Modeling and Simulation
More informationComparison of Conventional and Middle Vessel Batch Reactive Distillation Column: Application to Hydrolysis of Methyl Lactate to Lactic Acid
A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 35, 2013 Guest Editors: Petar Varbanov, Jiří Klemeš, Panos Seferlis, Athanasios I. Papadopoulos, Spyros Voutetakis Copyright 2013, AIDIC Servizi
More informationMODELLING OF CRUDE OIL DISTILLATION UNITS FOR RETROFITTING PURPOSES
JICEC05 Jordan International Chemical Engineering Conference V -4 September 005, Amman, Jordan MODELLIG OF CUDE OIL DISTILLATIO UITS FO ETOFITTIG PUPOSES M. Gadalla, *, Z. Olujic, M. Jobson, +,. Smith
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 informationEquipment Design and Costs for Separating Homogeneous Mixtures
Equipment Design and Costs for Separating Homogeneous Mixtures Dr. Syeda Sultana Razia Department of Chemical Engineering, Bangladesh University of Engineering and Technology (BUET), Dhaka -1000 1. Distillation
More informationCH2351 Chemical Engineering Thermodynamics II Unit I, II Phase Equilibria. Dr. M. Subramanian
CH2351 Chemical Engineering Thermodynamics II Unit I, II Phase Equilibria Dr. M. Subramanian Associate Professor Department of Chemical Engineering Sri Sivasubramaniya Nadar College of Engineering Kalavakkam
More informationA comparative study on the recovery of 1,2-dichloroethane and the removal of benzene contained in the byproducts of VCM process
Korean J. Chem. Eng., 27(3), 970-976 (2010) DOI: 10.1007/s11814-010-0206-7 RAPID COMMUNICATION A comparative study on the recovery of 1,2-dichloroethane and the removal of benzene contained in the byproducts
More informationMake distillation boundaries work for you!
Make distillation boundaries work for you! Michaela Tapp*, Simon T. Holland, Diane Hildebrandt and David Glasser Centre for Optimization, Modeling and Process Synthesis School of Process and Materials
More informationModelling and Simulation of Fermentation Product Purification for Local Vinegar using Batch Distillation
Modelling and Simulation of Fermentation Product Purification for Local Vinegar using Batch Distillation Faezah Bt Bakar University Malaysia Pahang, Kuantan, Malaysia ieyjah89_rose@yahoo.com.my Abstract
More informationEXPERIMENTAL SIMULATION OF DISTILLATION COLUMN PROFILE MAPS. Tshepo Sehole David Modise
EXPERIMENTAL SIMULATION OF DISTILLATION COLUMN PROFILE MAPS Tshepo Sehole David Modise A thesis submitted to the Faculty of Engineering and the Built Environment, University of the Witwatersrand, Johannesburg,
More informationInvariant rectifying-stripping curves for targeting minimum energy and feed location in distillation
Invariant rectifying-stripping curves for targeting minimum energy and feed location in distillation Santanu Bandyopadhyay a, Ranjan K. Malik b, Uday V. Shenoy c, * a Energy Systems Engineering, Department
More informationDistillation. This is often given as the definition of relative volatility, it can be calculated directly from vapor-liquid equilibrium data.
Distillation Distillation may be defined as the separation of the components of a liquid mixture by a process involving partial vaporization. The vapor evolved is usually recovered by condensation. Volatility
More informationResources for Students. Separation Process Principles, 2 nd Edition. J. D. Seader
Resources for Students using Separation Process Principles, 2 nd Edition by J. D. Seader Copyright 2005 John Wiley & Sons, Inc. All rights reserved. Table of Contents 1. Study Questions for each chapter........................
More informationDistillation is a method of separating mixtures based
Distillation Distillation is a method of separating mixtures based on differences in their volatilities in a boiling liquid mixture. Distillation is a unit operation, or a physical separation process,
More informationEfficient Feed Preheat Targeting for Distillation by Feed Splitting
European Symposium on Computer Arded Aided Process Engineering 15 L. Puigjaner and A. Espuña (Editors) 2005 Elsevier Science B.V. All rights reserved. Efficient Feed Preheat Targeting for Distillation
More informationEntrainer Selection Rules for the Separation of Azeotropic and Close-Boiling-Temperature Mixtures by Homogeneous Batch Distillation Process
Ind. Eng. Chem. Res. 2001, 40, 2729-2741 2729 Entrainer Selection Rules for the Separation of Azeotropic and Close-Boiling-Temperature Mixtures by Homogeneous Batch Distillation Process Ivonne Rodríguez-Donis,,
More informationChapter 4: Column Distillation: Internal Stage-by-Stage Balances
Chapter 4: Column Distillation: Internal Stage-by-Stage Balances In Chapter 3 (Introduction to Column Distillation), we performed the external balances or the balances around the distillation column To
More informationDistillation pinch points and more
Available online at www.sciencedirect.com Computers and Chemical Engineering 32 (2008) 1350 1372 Distillation pinch points and more Angelo Lucia a,, Amit Amale a, Ross Taylor b a Department of Chemical
More informationSee section and the dew and bubble point calculations in example 11.9.
Solution 1.1 See section 11.3.2 and the dew and bubble point calculations in example 11.9. This type of problem is best solved using a spread-sheet, see the solution to problem 11.2. Solution 11.2 This
More informationPressure Swing Distillation with Aspen Plus V8.0
Pressure Swing Distillation with Aspen Plus V8.0 1. Lesson Objectives Aspen Plus property analysis RadFrac distillation modeling Design Specs NQ Curves Tear streams Understand and overcome azeotrope Select
More informationHeterogeneous Azeotropic Distillation Operational Policies and Control
Heterogeneous Azeotropic Distillation Operational Policies and Control Claudia J. G. Vasconcelos * and Maria Regina Wolf-Maciel State University of Campinas, School of Chemical Engineering, Campinas/SP,
More informationVapor-liquid equilibrium
Vapor-liquid equilibrium From Wikipedia, the free encyclopedia Vapor-liquid equilibrium, abbreviated as VLE by some, is a condition where a liquid and its vapor (gas phase) are in equilibrium with each
More informationCALCULATION OF THE COMPRESSIBILITY FACTOR AND FUGACITY IN OIL-GAS SYSTEMS USING CUBIC EQUATIONS OF STATE
CALCULATION OF THE COMPRESSIBILITY FACTOR AND FUGACITY IN OIL-GAS SYSTEMS USING CUBIC EQUATIONS OF STATE V. P. de MATOS MARTINS 1, A. M. BARBOSA NETO 1, A. C. BANNWART 1 1 University of Campinas, Mechanical
More informationShortcut methods for complex distillation columns : part 2-- number of stages and feed tray location
Carnegie Mellon University Research Showcase @ CMU Department of Chemical Engineering Carnegie Institute of Technology 1979 Shortcut methods for complex distillation columns : part 2-- number of stages
More informationProblem 2 Distillation of air (20%) Solution
Problem 2 Distillation of air (20%) A feed with two components (79 mole% N 2 and 21% O 2 ) is to be separated by continuous distillation. (a) Compute equilibrium data (y,x) at 1 atm for N 2 -O 2 at x=0,
More informationQUESTION 1 The boiling temperature of hydrocarbons making up crude oil depends on the strength of intermolecular forces known as:
QUESTION 1 The boiling temperature of hydrocarbons making up crude oil depends on the strength of intermolecular forces known as: B C D Hydrogen bonding. Dipole-dipole interactions. Dispersion forces.
More informationOn the Synthesis of Distillation Sequences for Mixtures of Water, Hydrogen Chloride and Hydrogen Fluoride P. Pöllmann, SGL GROUP A.J.
On the Synthesis of Distillation Sequences for Mixtures of Water, Hydrogen Chloride and Hydrogen Fluoride P. Pöllmann, SGL GROUP A.J. Gerbino, AQSim (Speaker) Problem Statement Given... An aqueous feed
More informationComparison of distillation arrangement for the recovery process of dimethyl sulfoxide
Korean J. Chem. Eng., 24(3), 438-444 (2007) SHORT COMMUNICATION Comparison of distillation arrangement for the recovery process of dimethyl sulfoxide Jungho Cho and Dong Min Kim* Department of Chemical
More informationAggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems
Aggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems Ravindra S. Kamath 1, Ignacio E. Grossmann 1,*, and Lorenz T. Biegler 1 1 Chemical Engineering Department,
More informationBatchExtractiveDistillationwithLightEntrainer
V. VARGA et al., Batch Extractive Distillation with Light Entrainer, Chem. Biochem. Eng. Q. 20 (1) XXX XXX (2006) 1 BatchExtractiveDistillationwithLightEntrainer V. Varga,*, ** E. Rev,*,+ V. Gerbaud,**
More informationTOPIC: Conceptual Flowsheet for Production of Benzene from Toluene. Proposed Solution:
Norwegian University of Science and Technology Course: Energy and Process Department of Energy and Process Engineering No.: TEP 4230 Trondheim, 17.09.04, T. Gundersen Part: Production Systems Task: 5 Year:
More informationPRESSURE SWING BATCH DISTILLATION FOR HOMOGENOUS AZEOTROPIC SEPARATION
PRESSURE SWING BATCH DISTILLATION FOR HOMOGENOUS AZEOTROPIC SEPARATION Jens-Uwe Repke 1, Andreas Klein 1, David Bogle 2,Günter Wozny 1 1 Technical University Berlin, Department of Process- and Plant Dynamics,
More informationTemperature enthalpy curve for energy targeting of distillation columns
Temperature enthalpy curve for energy targeting of distillation columns Santanu Bandyopadhyay, Ranjan K. Malik and Uday V. Shenoy * Energy Systems Engineering, Department of Mechanical Engineering, Computer
More informationThe Simulation of the TBP Curve of Thymol Essence and the Separation of Natural Components with ASPEN plus Software
The Simulation of the TBP Curve of Thymol Essence and the Separation of Natural Components with ASPEN plus Software Varasteh Nobari A. 1, Tahmasebi H.A. 2, Aghili S. 3 1.Department of Chemical Engineering,
More informationChemical Process Design / Diseño de Procesos Químicos
Chemical Process Design / Diseño de Procesos Químicos Topic 4.7. Flash Javier R. Viguri Fuente Eva Cifrian Bemposta Department of Chemistry and Process & Resource Engineering GER Green Engineering and
More informationEXPERIMENTAL SIMULATION OF DISTILLATION COLUMN PROFILE MAPS. Tshepo Sehole David Modise
EXPERIMENTAL SIMULATION OF DISTILLATION COLUMN PROFILE MAPS Tshepo Sehole David Modise A thesis submitted to the Faculty of Engineering and the Built Environment, University of the Witwatersrand, Johannesburg,
More informationMinimum Energy Requirements in Complex Distillation Arrangements
Minimum Energy Requirements in Complex Distillation Arrangements by A thesis submitted for the degree of Dr.Ing. May 2001 Department of Chemical Engineering Norwegian University of Science and Technology
More informationSimulation of Ethanol Dehydration Using Cyclohexane as an Entrainer
Simulation of Ethanol Dehydration Using Cyclohexane as an Entrainer 2013 년 9 월 23 일 ( 월 ) 공주대학교화학공학부조정호 Limit of Distillation by Azeotrope 1.0 Ethanol / Water System Distillation range is restricted by
More informationRate-based design of integrated distillation sequences
17 th European Symposium on Computer Aided Process Engineering ESCAPE17 V. Plesu and P.S. Agachi (Editors) 2007 Elsevier B.V. All rights reserved. 1 Rate-based design of integrated distillation sequences
More informationContents. 1 Introduction and guide for this text 1. 2 Equilibrium and entropy 6. 3 Energy and how the microscopic world works 21
Preface Reference tables Table A Counting and combinatorics formulae Table B Useful integrals, expansions, and approximations Table C Extensive thermodynamic potentials Table D Intensive per-particle thermodynamic
More informationCork Institute of Technology. Autumn 2005 CE 2.7 Separation Process & Particle Technology (Time: 3 Hours) Section A
Cork Institute of Technology Bachelor of Engineering (Honours) in Chemical and Process Engineering Stage 2 (Bachelor of Engineering in Chemical and Process Engineering Stage 2) (NFQ Level 8) Autumn 2005
More informationMinimum Energy Operation of Petlyuk Distillation Columns - Nonsharp Product Specifications
Proceedings of the 1 st Annual Gas Processing ymposium H. Alfadala, G.V. Rex Reklaitis and M.M. El-Hawagi (Editors) 2009 Elsevier.V. All rights reserved. Minimum Energy Operation of Petlyuk istillation
More informationA NON-LINEAR WAVE MODEL WITH VARIABLE MOLAR FLOWS FOR DYNAMIC BEHAVIOUR AND DISTURBANCE PROPAGATION IN DISTILLATION COLUMNS
A NON-LINEAR WAVE MODEL WITH VARIABLE MOLAR FLOWS FOR DYNAMIC BEHAVIOUR AND DISTURBANCE PROPAGATION IN DISTILLATION COLUMNS Nick Hankins Department of Engineering Science, The University of Oxford, Parks
More informationDistillation Course MSO2015
Distillation Course MSO2015 Distillation Distillation is a process in which a liquid or vapour mixture of two or more substances is separated into its component fractions of desired purity, by the application
More informationMinimum Energy Demand and Split Feasibility for a Class of Reactive Distillation Columns
Minimum Energy emand and Split easibility for a Class of Reactive istillation Columns Rosa Y. Urdaneta, Jürgen ausa + and olfgang Marquardt * Lehrstuhl für Prozesstechnik RTH Aachen University, Templergraben
More informationThe effect of branched alcohol isomers on the separation of alkanes and alcohols with supercritical CO 2
The effect of branched alcohol isomers on the separation of alkanes and alcohols with supercritical CO 2 M. Zamudio, C.E. Schwarz, J.H. Knoetze* Department of Process Engineering, University of Stellenbosch,
More information,, Seong-Bo Kim,Hai-SongBae, and Jeong-Sik Han
Jungho Cho, So-Jin Park,, Myung-Jae Choi,, Seong-Bo Kim,Hai-SongBae, and Jeong-Sik Han Department of Chemical Engineering, Dong-Yang University, Kyoungbuk, 750-711, Korea *Department of Chemical Engineering,
More informationDEl'ERMINATION OF THE OPTIMUM FEED PLATE LOCATION IN MULTICOMPONENT DISTILLATION COLUMNS GLENN A. COMBS I( Bachelor of Science
OKLAHOMA STATE UNIVERSITY LIBRARY NOV 16 1973 DEl'ERMINATION OF THE OPTIMUM FEED PLATE LOCATION IN MULTICOMPONENT DISTILLATION COLUMNS By GLENN A. COMBS I( Bachelor of Science Oklahoma State University
More informationPhase Transitions in Multicomponent Systems
Physics 127b: Statistical Mechanics Phase Transitions in Multicomponent Systems The ibbs Phase Rule Consider a system with n components (different types of molecules) with r s in equilibrium. The state
More informationChemSep Tutorial: Distillation with Hypothetical Components
ChemSep Tutorial: Distillation with Hypothetical Components Harry Kooijman and Ross Taylor Here we use ChemSep to solve a complex multicomponent distillation problem presented in a paper entitled Multistage
More informationDistillation. Senior Design CHE 396 Andreas Linninger. Innovative Solutions. Michael Redel Alycia Novoa Tanya Goldina Michelle Englert
Distillation Senior Design CHE 396 Andreas Linninger Innovative Solutions Michael Redel Alycia Novoa Tanya Goldina Michelle Englert Table of Contents Introduction 3 Flowsheet 4 Limitations 5 Applicability
More informationDistillation. Presented by : Nabanita Deka
Distillation OPTIMIZATION FOR MAXIMISATION Presented by : Nabanita Deka LPG department OIL INDIA LIMITED DATED-04.03.2011 Basics of mass transfer Mass transfer : Transfer of material from one homogeneous
More informationChapter 2 Equilibria, Bubble Points, Dewpoints, Flash Calculations, and Activity Coefficients
Chapter 2 Equilibria, Bubble Points, Dewpoints, Flash Calculations, and Activity Coefficients 2.1 Vapour Pressure Calculations The basis for all phase equilibrium calculations are the vapour pressures
More informationVariational Inference for Monte Carlo Objectives
Variational Inference for Monte Carlo Objectives Andriy Mnih, Danilo Rezende June 21, 2016 1 / 18 Introduction Variational training of directed generative models has been widely adopted. Results depend
More informationECH 4224L Unit Operations Lab I Thin Film Evaporator. Introduction. Objective
Introduction In this experiment, you will use thin-film evaporator (TFE) to separate a mixture of water and ethylene glycol (EG). In a TFE a mixture of two fluids runs down a heated inner wall of a cylindrical
More information