and Absorption '92 Distillation UWVERSITftTSBIBUOTKEX WfORNtATlONSBlBUOTHEK HANNOVER Hemisphere Publishing Corporation
|
|
|
- Vivien Strickland
- 6 years ago
- Views:
Transcription
1 Distillation and Absorption '92 UWVERSITftTSBIBUOTKEX HANNOVER WfORNtATlONSBlBUOTHEK Institution of Chemical Engineers, Rugby, UK Hemisphere Publishing Corporation A Member of the Taylor & Francis Group New York Philadelphia London i
2 Contents Papers Dynamics, measurement, control Paper 1 Page Al Paper 2 PageA17 Integrated design and control of a binary distillation column A. Abbas, P.L. Yue andp.e. Sawyer (University of Bath, UK) Dynamics and optimal control of distributed-discrete staged fractionators F.Y. Wang and IX Cameron (University of Queensland, Australia) Paper 3 PageA33 Paper 4 t A429 Paper 5 Page A51 Online optimization of distillation column using new semirigorousdynamic model S. Ganguly and D.N. Saraf (Indian Institute of Technology, India) Dynamics and control of a distillation column with a sidestream A. Koggersbcl and S.B. Jorgensen (Technical University of Denmark, Denmark) Keynote Address Reactive distillation by design M.F. Doherty and G. Buzad (University of Massachusetts, USA) Absorption, distillation with chemical reaction Paper 6 t Page A391 Sour gas absorption and regenerative distillation H.-J. Bart and K. Burtscher (Technical University ofgraz, Austria) vii
3 Paper 7 Page A69 The influence of surface phenomena on the interfacial area during absorption/desorption on a sieve plate R. Pohorocki, J. Kruszewski and B. Duczmal (Warsaw Technical University, Poland) Paper 8 t Page A451 Experimental investigation and modelling of gas-liquid absorption with a high thermal effect A. Ramadane (SNEA-DRDIE, France), Z. Aoufoussi (ELF Atochem, France) and H. Le Goff (LSGC CNRS ENSICINPL, France) Sequencing and expert systems Paper 9 Page A77 Diabatic distillation simulation-optimisation of a column with integrated heat exchangers P. Le Goff, R. Rivero and T. Cachot (Laboratoire des Sciences du Ginie Chimique, France) and A. Ramadane (SNEA, France) Paper 10 t Page A461 Knowledge based synthesis of energy integrated distillation columnsand sequences W. Schtittenhelm and K.H. Simmrock (University of Dortmund, Germany) Paper 11 Definition and computation of distillation boundaries Page A91 a new approach O. Mekiffer and K. Hartmann (Berlin Adlershof Scientific Centre, Germany) Packing 1 Paper 12 Page A99 Paper 13 t Page A481 Random packing performance in light ends distillation D. Nutter (Nutter Engineering, USA), F,C. Sllvey (deceased, formerly with Mobil Research and Development Corporation, USA) and B.K. Stober (Mobil Research and Development Corporation, USA) Evidence of vapour backmixing in packed columns in the case of high pressure distillation F.J. Zuiderweg (Consultant, The Netherlands) and D.E. Nutter (Nutter Engineering, USA) viii
4 Paper 14 +PageA489 A comprehensive model for the performance of columns containing structured packings J.L. Bravo (JaegerProducts Inc, USA), J.A. Rocha (Instituto Technologico de Celaya, Mexico) and J.R. Fair (University of Texas at Austin, USA) Paper 15 Page A109 Flooding and pressure drop prediction for structured packings H.Z. Kister (Brown & Root Braun, USA) and D.R. Gill (Simulation Sciences Inc, USA) Paper 16 PageA125 Impact of low pressure drop structured packing on air distillation R. Agrawal, D.W. Woodward, K.A. Ludwig and D.L. Bennett (Air Products and Chemicals Inc, USA) Paper 17 Page Al 39 Some Keynote Address of distillation research and industrial progress applications in China K.T. Yu (Tianjin University, China) Equipment, plants and batch distillation processes, Paper 18 Page A167 The design of spinning cone distillation columns S.J. Sykes (CSIRO, Australia) and R.G.H. Prince (University of Sydney, Australia) Paper 19 t Page A403 Short path distillation W. Fischer and D. Bethge (UIC GmbH, Germany) Packing 2 Paper 20 Page A181 Marangoni effect, liquid phase resistanceor maldistribution? F.J. Zuiderweg (Consultant, The Netherlands) and T. Yanagi (Fractionation Research Inc, USA) IX
5 Paper 21 t Page A369 Analysis of gas entries of packed columns for two-phase-flow P. Suess (Sulzer Bros Ltd, Switzerland) Paper 22 Page Al 91 in Paper 23 Page A201 Study on the temperature field and mass transfer process a column with structured packing X.J, Yuan (Tianjin University, China), G.Q. Dong (Academia Sinica, China) and S.Y. Wang (Tianjin University, China) Modelling of hydraulic and separation performance of large diametercolumns containing structured packings F. Stoter, Z. Olujic and J. de Graauw (Delft University of Technology, The Netherlands) Trays 1 Paper 24 PageA211 Paper 25 Page A221 Paper 26 Page A235 Paper 27 Page A245 Use of gamma scanning to obtain quantitative hydraulic data on a commercial scale J.G. Kunesh, D.W. King II and C.W. Fitz Jr. (Fractionation Research Inc, USA) The effect of spray structure on the spray froth transition on sieve trays W.K. Kwan, R.K.F. Ng, L.W.M. So and P.F.Y Wong (University of Hong Kong, Hong Kong) Hydrodynamics and mass transfer on vibrating valve plates E. B6kassy-Molna>, B. Korda and I. Takacs (Technical University of Budapest, Hungary) Flow pa tterns on trays and interactions with the whole fluid dynamics S. Weiss, N. Ahr and H. Herfurth (Technical University of Merseburg, Germany) Paper 28 Flow patterns and on temperatures profiles a 2.44m Page A257 diameter sieve tray K.E. Porter (Aston University, UK), K.T. Yu (Tianjin University, China), S. Chambers (Aston University, UK) and M.Q. Zhang (Tianjin University, China) x
6 Thermodynamics, azeotropic and extractive distillation, models Paper 29 Page A277 Paper 30 t Page A415 Paper 31 Page A293 Paper 32 Page A309 Paper 33 Page A329 Efficient and accurate computation of thermodynamic properties for design of separa tion processes R. Gani and A. Fredenslund (Technical University of Denmark, Denmark) Industrial applications of a nonequilibrium model of distillation and absorption operations R. Taylor, H.A. Kooijman (Clarkson University, USA) and M.R. Woodman (BP Engineering, UK) A generalized approach to phase equilibria: recent developments in the prediction of vapour-liquid equilibria from a generalized London potential J. Homer, J.D. Jenkins, K.E. Porter and A.I. Kakhu (Aston University, UK) Distillation processes for the separation of ternary zeotropic and azeotropic mixtures J.G. Stichlmair and J.-R. Herguijuela (University of Essen, Germany) Simulation of atmospheric crude towers including packed bed pump-around zones using a rate-based simulator K.J. McNulty and S.G. Chatterjee (Koch Engineering Research, USA) Trays 2 Paper 34 t AS 19 Paper 35 Page A345 Intensification of mass transfer in two-phase gas-liquid flows N.N. Kulov (Kumakov Institute of General and Inorganic Chemistry, Russia) A new high performance flow control tray I.J. Urua, J.T. Lavin (BOC Cryoplants, UK) and M.W. Biddulph (University of Nottingham, UK) Paper 36 Page A361 Varioflex valve tray, a high performance mass transfer device R. Billet (Ruhr University Bochum, Germany) xi
7 Paper 37 t Page A509 High capacity Nye trays G. de Bruyn (Glitsch Inc, USA), H.A. Gangriwala (Glitsch UK) and J.O. Nye (Nye Engineering, USA) Closing Address Paper 38 Page A385 Distillation and current absorption technology: market and new developments R.C. Darton (University of Oxford, UK) xii
A NEW PRESSURE DROP MODEL FOR STRUCTURED PACKING
A NEW PRESSURE DROP MODEL FOR STRUCTURED PACKING H.A. Kooijman*, K.R. Krishnamurthy* & M.W. Biddulph * The BOC Group, Murray Hill, NJ 07974, USA. ABSTRACT A new pressure drop model for Mellapak 750YL,
Distillation the most important unit operation. Predict Distillation Tray Efficiency. Reactions and Separations
Predict Distillation Tray Efficiency Markus Duss Sulzer Chemtech Ltd Ross Taylor Clarkson Univ. An empirical technique the O Connell correlation is widely used to estimate the efficiency of cross-flow
A Rate-Based Equation-Oriented Parallel Column Model: Application to Dividing Wall Columns
A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 69, 2018 Guest Editors: Elisabetta Brunazzi, Eva Sorensen Copyright 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-66-2; ISSN 2283-9216 The Italian
SEPARATION PERFORMANCE OF STRUCTURED PACKED COLUMNS: A COMPARISON OF TWO MODELLING APPROACHES
SEPARATION PERFORMANCE OF STRUCTURED PACKED COLUMNS: A COMPARISON OF TWO MODELLING APPROACHES A. Shilkin and E.Y. Kenig Department of Biochemical and Chemical Engineering, University of Dortmund, Emil-Figge-Str.
A MODIFIED MODEL OF COMPUTATIONAL MASS TRANSFER FOR DISTILLATION COLUMN
A MODIFIED MODEL OF COMPUTATIONAL MASS TRANSFER FOR DISTILLATION COLUMN Z. M. Sun, X. G. Yuan, C. J. Liu, K. T. Yu State Key Laboratory for Chemical Engineering (Tianjin University) and School of Chemical
Application of the Wallis Plot for the Determination of the Loading Limits of Structured Packings and Sandwich Packings
1165 A publication of CHEMICA ENINEERIN TRANSACTIONS VO. 45, 15 uest Editors: Petar Sabev Varbanov, Jiří Jaromír Klemeš, Sharifah Rafidah Wan Alwi, Jun Yow Yong, Xia iu Copyright 15, AIDIC Servizi S.r.l.,
Study of Clear Liquid Height and Dry Pressure Drop Models for Valve Trays
A publication of CHEMICA ENGINEERING TRANSACTIONS VO. 69, 18 Guest Editors: Elisabetta Brunazzi, Eva Sorensen Copyright 18, AIDIC Servizi S.r.l. ISBN 978-88-9568-66-; ISSN 83-916 The Italian Association
Benchmarking Mass Transfer Correlations with a Nonequilibrium Model
Benchmarking Mass Transfer Correlations with a Nonequilibrium Model Harry Kooijman & Ross Taylor Clarkson University Packed Column Design Column Diameter: Capacity: F-factor or C-factor Pressure Drop:
Mass Transfer and Separation Processes
Principles of Mass Transfer and Separation Processes Binay K. Dutta Universiti Teknologi Petronas Malaysia New Delhi-110001 2009 PRINCIPLES OF MASS TRANSFER AND SEPARATION PROCESSES Binay K. Dutta 2007
Hydraulic and Mass Transfer Performances of a Commercial Hybrid Packing: The RSP200X - Key Modelling Parameters for Gas Treatment Applications
A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 69, 2018 Guest Editors: Elisabetta Brunazzi, Eva Sorensen Copyright 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-66-2; ISSN 2283-9216 The Italian
Wikisheet Dividing Wall Column
Wikisheet Divided Wall Column Dividing Wall Column Conventional Columns System Objective Contribute to energy efficiency program Background, Wikisheets Process Intensification within the PIN-NL program
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
Incorporating Reality Into Process Simulation. Nathan Massey Chemstations, Inc. January 10, 2002
Incorporating Reality Into Process Simulation Nathan Massey Chemstations, Inc. January 10, 2002 Levels of Reality in Process Simulation 1. Data Accuracy and Comprehensiveness Physical Properties Phase
A Rate-Based Equation-Oriented Parallel Column Model: Application to Dividing Wall Columns
A Rate-Based Equation-Oriented Parallel Column Model: Application to Dividing Wall Columns Jingsong Zhou, Harry Kooijman, and Ross Taylor Department of Chemical and Biomolecular Engineering Clarkson University
CFD SIMULATIONS OF BENZENE TOLUENE SYSTEM OVER SIEVE TRAY
CFD SIMULATIONS OF BENZENE TOLUENE SYSTEM OVER SIEVE TRAY Sumit Singh M.Tech, Department of Chemical Engineering Dr. B R Ambedkar National Institute of Technology, Jalandhar, India sumit_nitj@yahoo.com
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.
INTEGRATION OF DESIGN AND CONTROL FOR ENERGY INTEGRATED DISTILLATION
INTEGRATION OF DESIGN AND CONTROL FOR ENERGY INTEGRATED DISTILLATION Hongwen Li, Rafiqul Gani, Sten Bay Jørgensen CAPEC, Department of Chemical Engineering Technical University of Denmark, Lyngby, Denmark
Quick Guide QUICK GUIDE. Activity 1: Determine the Reaction Rate in the Presence or Absence of an Enzyme
Activity 1: Determine the Reaction Rate in the Presence or Absence of an 1. Find your 15 ml conical tubes labeled Stop Solution, 1.5 mm Substrate, and Buffer. Write your initials on each tube. 2. Label
HEAT TRANSFER THERMAL MANAGEMENT OF ELECTRONICS YOUNES SHABANY. C\ CRC Press W / Taylor Si Francis Group Boca Raton London New York
HEAT TRANSFER THERMAL MANAGEMENT OF ELECTRONICS YOUNES SHABANY C\ CRC Press W / Taylor Si Francis Group Boca Raton London New York CRC Press is an imprint of the Taylor & Francis Group, an informa business
NOMENCLATURE FOR CHROMATOGRAPHY NOMENCLATURE FOR SUPERCRITICAL FLUID CHROMATOGRAPHY AND EXTRACTION
INTERNATIONAL UNION OF PURE AND APPLIED CHEMISTRY ANALYTICAL CHEMISTRY DIVISION COMMISSION ON CHROMATOGRAPHY AND OTHER ANALYTICAL SEPARATIONS NOMENCLATURE FOR CHROMATOGRAPHY (Supplement NOMENCLATURE FOR
AJCHE 2012, Vol. 12, No. 1, Synthesis of Ternary Homogeneous Azeotropic Distillation Sequences: Entrainer Selection
AJCHE 2012, Vol. 12, No. 1, 20 33 Synthesis of Ternary Homogeneous Azeotropic Distillation Sequences: Entrainer Selection Sutijan *,1 Megan Jobson 2 Robin Smith 2 1 Department of Chemical Engineering,
Batch extractive distillation of mixture methanol-acetonitrile using aniline as a asolvent
48 Pol. J. Chem. Polish Tech., Journal Vol. 14, of No. Chemical 3, 2012 Technology, 14, 3, 48 53, 10.2478/v10026-012-0083-4 Batch extractive distillation of mixture methanol-acetonitrile using aniline
THREE-DIMENSIONAL SIMULATION OF LIQUID FLOW ON A SIEVE TRAY UNDER DIFFERENT INCLINATIONS
Brazilian Journal of Chemical Engineering ISSN 0104-6632 Printed in Brazil www.abeq.org.br/bjche Vol. 31, No. 04, pp. 905-912, October - December, 2014 dx.doi.org/10.1590/0104-6632.20140314s00003038 THREE-DIMENSIONA
Equipment 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
Tray Columns: Performance. Further Reading. Design Calculations. Conclusions. Introduction
1140 II / DISTILLATION / Tray Columns: Performance to the minimum area to the minimum area required for vapour}liquid disengagement. The DCBUSF determines the approach of the downcomer froth height to
viridis Columns Bringing a New Dimension to SFC Combining state-of-the-art media manufacturing with industry leading column technology, Viridis
[ viridis columns ] viridis Columns Bringing a New Dimension to SFC Combining state-of-the-art media manufacturing with industry leading column technology, Viridis Supercritical Fluid Chromatography (SFC)
[ Care and Use Manual ]
![[ Care and Use Manual ]](/thumbs/94/118749905.jpg "[ Care and Use Manual ]")
Oasis HLB DISKS I. Introduction Oasis HLB is a Hydrophilic-Lipophilic-Balanced, water-wettable, reversed-phase sorbent for all your SPE needs. It is made from a specific ratio of two monomers, the hydrophilic
2017 Source of Foreign Income Earned By Fund
2017 Source of Foreign Income Earned By Fund Putnam Emerging Markets Equity Fund EIN: 26-2670607 FYE: 08/31/2017 Statement Pursuant to 1.853-4: The fund is hereby electing to apply code section 853 for
THERMODYNAMIC INSIGHT ON EXTRACTIVE DISTILLATION WITH ENTRAINER FORMING NEW AZEOTROPES
Distillation Absorption 2010 A.. de Haan, H. Kooijman and A. Górak (Editors) All rights reserved by authors as per DA2010 copyright notice THERMODYNAMIC INSIGHT ON EXTRTIVE DISTILLATION WITH ENTRAINER
Ethane-Ethylene Rectification Column s Parametric Examination
1477 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 70, 2018 Guest Editors: Timothy G. Walmsley, Petar S. Varbanov, Rongxin Su, Jiří J. Klemeš Copyright 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-67-9;
Active Flow Technology Understanding How the Flow Rate Profile Affects the Chromatographic Efficiency
Active Flow Technology Understanding How the Flow Rate Profile Affects the Chromatographic Efficiency Anthony Edge, 1 Luisa Pereira, 1 Dafydd Milton 1 and Andrew Shalliker 2 1 Thermo Fisher Scientific,
Open 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
Export Destinations and Input Prices. Appendix A
Export Destinations and Input Prices Paulo Bastos Joana Silva Eric Verhoogen Jan. 2016 Appendix A For Online Publication Figure A1. Real Exchange Rate, Selected Richer Export Destinations UK USA Sweden
CFD SIMULATION OF MULTIPHASE FLOW IN A SIEVE TRAY OF A DISTILLATION COLUMN
CFD SIMULATION OF MULTIPHASE FLOW IN A SIEVE TRAY OF A DISTILLATION COLUMN a Teleen, J. G.; a Werle, L. O. 1 ; a Marangoni, C.; a Quadri, M. B.; Machado, R. A. F. a Federal University of Santa Catarina-
A Sequential and Hierarchical Approach for the Feasibility Analysis and the Preliminary Synthesis and Design of Reactive Distillation Processes
A Sequential and Hierarchical Approach for the Feasibility Analysis and the Preliminary Synthesis and Design of Reactive Distillation Processes Raphaële Thery, Xuân-Mi Meyer 1, Xavier Joulia Laboratoire
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)
UvA-DARE (Digital Academic Repository) Mass transfer effects in distillation Springer, P.A.M. Link to publication
UvA-DARE (Digital Academic Repository) Mass transfer effects in distillation Springer, P.A.M. Link to publication Citation for published version (APA): Springer, P. A. M. (2004). Mass transfer effects
Estimation of the Number of Distillation Sequences with Dividing Wall Column for Multi-component Separation
343 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 61, 017 Guest Editors: Petar S Varbanov, Rongxin Su, Hon Loong Lam, Xia Liu, Jiří J Klemeš Copyright 017, AIDIC Servizi S.r.l. ISBN 978-88-95608-51-8;
University School of Chemical Technology
University School of Chemical Technology Guru Gobind Singh Indraprastha University Syllabus of Examination B.Tech/M.Tech Dual Degree (Chemical Engineering) (4 th Semester) (w.e.f. August 2004 Batch) Page
Science & Technologies SURFACE TENSION EFFECTS IN SIEVE PLATE DISTILLATION COLUMN
SURFACE TENSION EFFECTS IN SIEVE PLATE DISTILLATION COLUMN Zhelcho Stefanov, Mariana Karaivanova University Prof.d-r Assen Zlatarov Bourgas 8, Bulgaria ABSTRACT Rectification is one of the methods for
SIEVE TRAY EFFICIENCY USING CFD MODELING AND SIMULATION
SIEVE TRAY EFFICIENCY USING CFD MODELING AND SIMULATION Getye Gesit* School of Chemical and Bio Engineering Addis Ababa Institute of Technology, Addis Ababa University ABSTRACT In this work, computational
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
Nigerian Capital Importation QUARTER THREE 2016
Nigerian Capital Importation QUARTER THREE 2016 _ November 2016 Capital Importation Data The data on Capital Importation used in this report was obtained from the Central Bank of Nigeria (CBN). The data
INTRODUCTION TO CATALYTIC COMBUSTION
INTRODUCTION TO CATALYTIC COMBUSTION R.E. Hayes Professor of Chemical Engineering Department of Chemical and Materials Engineering University of Alberta, Canada and S.T. Kolaczkowski Professor of Chemical
CONTROL PROPERTIES ANALYSIS OF ALTERNATE SCHEMES TO THERMALLY COUPLED DISTILLATION SCHEMES
8th International IFAC Symposium on Dynamics and Control of Process Systems Preprints Vol.1, June 6-8, 2007, Cancún, Mexico CONTROL PROPERTIES ANALYSIS OF ALTERNATE SCHEMES TO THERMALLY COUPLED DISTILLATION
TSK. Flap-Type Flowmeter. Range: to GPM Accuracy: ± 2.5% of Full Scale P max. : 580 PSI T max
Flap-Type Flowmeter measuring monitoring analyzing TSK Range: 6.6...26.4 to 880...6600 GPM Accuracy: ± 2.5% of Full Scale P max : 580 PSI T max : -40 572 F Connection: Wafer Flange 1.5" 20" ASME Material:,
Feasibility of separation of ternary mixtures by pressure swing batch distillation
10th nternational Symposium on Process Systems Engineering - PSE2009 Rita Maria de Brito Alves, Claudio Augusto Oller do Nascimento and Evaristo Chalbaud Biscaia Jr. (Editors) 2009 Elsevier B.V. All rights
Research Article Studies on a Foam System of Ultralow Interfacial Tension Applied in Daqing Oilfield after Polymer Flooding
Chemistry Volume 213, Article ID 15274, 6 pages http://dx.doi.org/1.1155/213/15274 Research Article Studies on a Foam System of Ultralow Interfacial Tension Applied in Daqing Oilfield after Polymer Flooding
Operation and Control of Reactive Distillation for Synthesis of Methyl Formate
Asian Journal of Chemistry; Vol. 25, No. 8 (3), 477-482 http://dx.doi.org/.4233/ajchem.3.37a Operation and Control of Reactive Distillation for Synthesis of Methyl Formate JIE YANG, PENG BAI * and KUN
RATE-BASED MODELING OF TWO COMMERCIAL SCALE H 2 S STRIPPING COLUMNS
Distillation Absorption A.B. de Haan, H. Kooijman and A. Górak (Editors) All rights reserved by authors as per DA copyright notice RATE-BASED MODELING OF TWO COMMERCIAL SCALE H 2 S STRIPPING COLUMNS Ross
IN QUALITATIVE ANALYSIS,
IN QUALITATIVE ANALYSIS, YOU VE ALWAYS HAD TO CHOOSE BETWEEN ACCURACY AND THROUGHPUT. NOW THERE S NO REASON TO ever have to. WATERS QUALITATIVE ANALYSIS solutions Waters ACQUITY UPLC System with the Waters
Fast, Effective XPS Point Analysis of Metal Components
Application Note: 52297 Fast, Effective XPS Point Analysis of Metal Components Chris Baily and Tim Nunney, Thermo Fisher Scientific, East Grinstead, West Sussex, UK Key Words K-Alpha Auto-Analysis Multi-Spectrum
University School of Chemical Technology
University School of Chemical Technology Guru Gobind Singh Indraprastha University Syllabus of Examination B.Tech/M.Tech Dual Degree (Chemical Engineering) (5 th Semester) (w.e.f. August 2004 Batch) Page
Study of arrangements for distillation of quaternary mixtures using less than n-1 columns
Instituto Tecnologico de Aguascalientes From the SelectedWorks of Adrian Bonilla-Petriciolet 2008 Study of arrangements for distillation of quaternary mixtures using less than n-1 columns J.G. Segovia-Hernández,
Cyclone Click to go to the page. Cyclone
Cyclone.0311.2 Click to go to the page Cyclone The Cyclone (1,000-8,000 CFM) Suitable for collection of virtually any type of dust Applications: Heavy Moulding Grinding Planing Cabinet Shops Dust Transfer
Parity Reversion of Absolute Purchasing Power Parity Zhi-bai ZHANG 1,a,* and Zhi-cun BIAN 2,b
2016 3 rd International Conference on Economics and Management (ICEM 2016) ISBN: 978-1-60595-368-7 Parity Reversion of Absolute Purchasing Power Parity Zhi-bai ZHANG 1,a,* and Zhi-cun BIAN 2,b 1,2 School
[ OSTRO PASS-THROUGH SAMPLE PREPARATION PRODUCT ] The Simpler Way to Cleaner Samples
![[ OSTRO PASS-THROUGH SAMPLE PREPARATION PRODUCT ] The Simpler Way to Cleaner Samples](/thumbs/81/83980731.jpg "[ OSTRO PASS-THROUGH SAMPLE PREPARATION PRODUCT ] The Simpler Way to Cleaner Samples")
[ OSTRO PASS-THROUGH SAMPLE PREPARATION PRODUCT ] The Simpler Way to Cleaner Samples SIMPLE EASY EFFICIENT DEPENDABLE 2 waters.com/ostro 3 SIMPLE The Ostro Pass-Through Sample Preparation Product provides
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
Appendix B: Detailed tables showing overall figures by country and measure
44 country and measure % who report that they are very happy Source: World Values Survey, 2010-2014 except United States, Pew Research Center 2012 Gender and Generations survey and Argentina 32% 32% 36%
Design and Control Properties of Arrangements for Distillation of Four Component Mixtures Using Less Than N-1 Columns
D. M. MÉNDEZ-VALENCIA et al., Design and Control Properties of Arrangements, Chem. Biochem. Eng. Q. 22 (3) 273 283 (2008) 273 Design and Control Properties of Arrangements for Distillation of Four Component
Towards intensified separation processes in gas/vapour-liquid systems. Chair of Fluid Process Engineering Prof. Dr.-Ing.
Towards intensified separation processes in gas/vapour-liquid systems Prof. Dr.-Ing. Eugeny Kenig Why intensification? - Requests through global changes Fast population growth Rising life expectations
Make 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
Foundations of Ultraprecision Mechanism Design
Foundations of Ultraprecision Mechanism Design S.T. Smith University of North Carolina at Charlotte, USA and D.G. Chetwynd University of Warwick, UK GORDON AND BREACH SCIENCE PUBLISHERS Switzerland Australia
Systematic optimization-based integrated chemical product-process design framework
Systematic optimization-based integrated chemical product-process design framework Stefano Cignitti*, Seyed Soheil Mansouri, John M. Woodley, Jens Abildskov Process and Systems Engineering Centre (PROSYS),
CFD Simulation and Experimental Study of New Developed Centrifugal Trays
CFD Simulation and Experimental Study of New Developed Centrifugal Trays N. Naziri, R. Zadghaffari, and H. Naziri Abstract In this work, a computational fluid dynamics (CFD) model is developed to predict
MASS TRANSFER AND GAS ABSORPTION EQUIPMENT
MASS TRANSFER AND GAS ABSORPTION EQUIPMENT Mark J McCready University of Notre Dame Indiana, USA TOPICS Review of heat transfer and heat exchangers Some fundamental aspects of mass transfer Analysis of
A Prior Distribution of Bayesian Nonparametrics Incorporating Multiple Distances
A Prior Distribution of Bayesian Nonparametrics Incorporating Multiple Distances Brian M. Hartman 1 David B. Dahl 1 Debabrata Talukdar 2 Bani K. Mallick 1 1 Department of Statistics Texas A&M University
A Strategy for an Unknown Screening Approach on Environmental Samples Using HRAM Mass Spectrometry
A Strategy for an Unknown Screening Approach on Environmental Samples Using HRAM Mass Spectrometry Olaf Scheibner, 1 Patrizia van Baar, 2 Florian Wode, 2 Uwe Dünnbier, 2 Kristi Akervik, 3 Jamie Humphrie,
Isobaric Vapor Liquid Equilibria of Systems containing N-Alkanes and Alkoxyethanols
Isobaric Vapor Liquid Equilibria of Systems containing N-Alkanes and Alkoxyethanols Sunghyun Jang, Moon Sam Shin, Yongjin Lee, Hwayong Kim * School of Chemical Engineering & Institute of Chemical Processes,
INTERNATIONAL STANDARD
INTERNATIONAL STANDARD INTERNATIONAL ORGANIZATION FOR STANDARDIZATIONWEWlYHAPOCIHAR OPrAHM3ALlMR l-l0 CTAH~APTbl3ALWl.ORGANlSATlON INTERNATIONALE DE NORMALISATION Determination of water - Karl Fischer
Comparison of models for the prediction of hydrodynamic parameters in structured packing columns for biogas purification
Comparison of models for the prediction of hydrodynamic parameters in structured packing columns for biogas purification Hamadi Cherif, Christophe Coquelet, Paolo Stringari, Denis Clodic, Joseph Toubassy
COPERNICUS FOUNDATION POLISH ASTRONOMY, AL UJAZDOWSKIE 4, WARSAW, POLAND, ,
SCIENCE CITATION INDEX - ASTRONOMY & ASTROPHYSICS - JOURNAL LIST Total journals: 38 1. ACTA ASTRONOMICA Quarterly ISSN: 0001-5237 COPERNICUS FOUNDATION POLISH ASTRONOMY, AL UJAZDOWSKIE 4, WARSAW, POLAND,
Insights Into the Nanoworld Analysis of Nanoparticles with ICP-MS
Insights Into the Nanoworld Analysis of Nanoparticles with ICP-MS Daniel Kutscher, 1 Jörg Bettmer, 2 Torsten Lindemann, 1 Shona McSheehy-Ducos, 1 Lothar Rottmann 1 1 Thermo Fisher Scientific, Germany 2
EMEA Rents and Yields MarketView
Dec-94 Dec-95 Dec-96 Dec-97 Dec-98 Dec-99 Dec-00 Dec-01 Dec-02 Dec-03 Dec-04 Dec-05 Dec-06 Dec-07 Dec-08 Dec-09 Dec-10 Dec-11 Dec-12 Dec-94 Dec-95 Dec-96 Dec-97 Dec-98 Dec-99 Dec-00 Dec-01 Dec-02 Dec-03
Theoretical Evaluation of Ultrasonic Velocity in Binary Liquid Mixtures of Alcohols [S] + Benzene
![Theoretical Evaluation of Ultrasonic Velocity in Binary Liquid Mixtures of Alcohols [S] + Benzene](/thumbs/83/87131825.jpg "Theoretical Evaluation of Ultrasonic Velocity in Binary Liquid Mixtures of Alcohols [S] + Benzene")
International Letters of Chemistry, Physics and Astronomy Online: 2013-09-21 ISSN: 2299-3843, Vol. 7, pp 18-35 doi:10.18052/www.scipress.com/ilcpa.7.18 2013 SciPress Ltd., Switzerland Theoretical Evaluation
THERMODYNAMIC ANALYSIS OF MULTICOMPONENT DISTILLATION-REACTION PROCESSES FOR CONCEPTUAL PROCESS DESIGN
THERMODYNAMIC ANALYSIS OF MULTICOMPONENT DISTILLATION-REACTION PROCESSES FOR CONCEPTUAL PROCESS DESIGN Oliver Ryll, Sergej Blagov 1, Hans Hasse Institute of Thermodynamics and Thermal Process Engineering,
Preparative Chromatography
Edited by Henner Andreas Seidel-Morgenstern Michael Schulte, and Preparative Chromatography Completely Revised and Updated Edition VCH Verlag GmbH & Co. KGaA About List of List of Notations XIX XXI 1 Introduction
An 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
Triple Column Pressure-Swing Distillation for Ternary Mixture of Methyl Ethyl Ketone /Isopropanol /Ethanol
649 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 61, 2017 Guest Editors: Petar S Varbanov, Rongxin Su, Hon Loong Lam, Xia Liu, Jiří J Klemeš Copyright 2017, AIDIC Servizi S.r.l. ISBN 978-88-95608-51-8;
Network Young Membrains (NYM14) Permeation through NF and UF membranes
Network Young Membrains (NYM14) Permeation through NF and UF membranes Patrizia Marchetti/ Lonza Ltd/ Imperial College London (UK), 20-22 September 2012 Transport mechanisms through membranes no pores
1.7µm Fortis C18 UHPLC Columns
Strength in Technology.7µm Fortis C8 Columns Ultra High Pressure Chromatography Increase Efficiency Increase Speed Improve Resolution Greater Sensitivity Wider Linear flow rate range .7µm Columns - 8m/g
INDUSTRIAL APPLICATION OF A NEW BATCH EXTRACTIVE DISTILLATION OPERATIONAL POLICY
INDUSTRIAL APPLICATION OF A NEW BATCH EXTRACTIVE DISTILLATION OPERATIONAL POLICY Lang P. 1, Gy. Kovacs 2, B. Kotai 1, J. Gaal-Szilagyi 2, G. Modla 1 1 BUTE, Department of Process Engineering, H-1521 Budapest
Product Data. Brüel & Kjær B. Sound Intensity Calibrator Type 3541
Product Data Sound Intensity Calibrator Type 3541 USES: Sound intensity and particle velocity calibrations Sound pressure calibration Measurement of pressure-residual intensity index FEATURES: Intensity
Michael Schultes, Werner Grosshans, Steffen Müller and Michael Rink, Raschig GmbH, Germany, present a modern liquid distributor and redistributor
Michael Schultes, Werner Grosshans, Steffen Müller and Michael Rink, Raschig GmbH, Germany, present a modern liquid distributor and redistributor design. All the mod Part 1 cons In recent years, great
Evaluation of the Characteristic of Adsorption in a Double-Effect Adsorption Chiller with FAM-Z01
Journal of Materials Science and Chemical Engineering, 2016, 4, 8-19 http://www.scirp.org/journal/msce ISSN Online: 2327-6053 ISSN Print: 2327-6045 Evaluation of the Characteristic of Adsorption in a Double-Effect
MODELING OF A DISTILLATION COLUMN USING BOND GRAPHS
MODELING OF A DISTILLATION COLUMN USING BOND GRAPHS by Braden Alan Brooks Copyright Braden Alan Brooks 1993 A Thesis Submitted to the Faculty of the Department of Electrical & Computer Engineering In Partial
A long-term global forecast for the extraction of oil and gas from shale formations
A long-term global forecast for the extraction of oil and gas from shale formations Finding Petroleum, London, 10/10/2012 Per Magnus Nysveen Rystad Energy This document is the property of Rystad Energy.
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
Improved Throughput and Reproducibility for Targeted Protein Quantification Using a New High-Performance Triple Quadrupole Mass Spectrometer
Improved Throughput and Reproducibility for Targeted Protein Quantification Using a New High-Performance Triple Quadrupole Mass Spectrometer Reiko Kiyonami, Mary Blackburn, Andreas FR Hühme: Thermo Fisher
Monitoring Protein PEGylation with Ion Exchange Chromatography
Monitoring Protein PEGylation with Ion Exchange Chromatography Peter Yu, Deanna Hurum, Jinyuan (Leo) Wang, 2 Terry Zhang, 2 and Jeffrey Rohrer Thermo Fisher Scientific, Sunnyvale, CA; 2 Thermo Fisher Scientific,
Dynamic Effects of Diabatization in Distillation Columns
Downloaded from orbit.dtu.dk on: Dec 27, 2018 Dynamic Effects of Diabatization in Distillation Columns Bisgaard, Thomas Publication date: 2012 Document Version Publisher's PDF, also known as Version of
SELECTIVE REMOVAL OF CARBON DIOXIDE FROM AQUEOUS AMMONIA SOLUTIONS
Distillation Absorption 2010 A.B. de Haan, H. Kooijman and A. Górak (Editors) All rights reserved by authors as per DA2010 copyright notice SELECTIVE REMOVAL OF CARBON DIOXIDE FROM AQUEOUS AMMONIA SOLUTIONS
Distillation. 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:
Using thermodynamics to assess the molecular interactions of tetrabutylphosphonium carboxylate-water mixtures
10.1071/CH18481_AC CSIRO 2019 Australian Journal of Chemistry Supplementary Material Using thermodynamics to assess the molecular interactions of tetrabutylphosphonium carboxylate-water mixtures Darius
Curriculum Vitae. Education Background
Curriculum Vitae Hu ZHANG MOE Key Laboratory of Thermo-Fluid Science and Engineering, School of Energy and Power Engineering, Xi an Jiaotong University, Xi an, 710049, China Mechanical Engineering, University
EXPERIMENTS IN PHYSICAL CHEMISTRY
EXPERIMENTS IN PHYSICAL CHEMISTRY SIXTH EDITION DAVID P. SHOEMAKER CARL W. GARLAND JOSEPH W. NIBLER The Late Emeritus Professor of Chemistry Professor of Chemistry Professor of Chemistry Oregon State University
ANALYSIS OF BASIC COMPOUNDS
COMPARISON OF Fully AND Superficially POROUS PARTICLE COLUMNS FOR THE ANALYSIS OF BASIC COMPOUNDS Kenneth J. Fountain, Jane Xu, Zhe Yin, Pamela C. Iraneta, Diane M. Diehl Waters Corporation GOAL Compare
Implementation and Operation of a Dividing-Wall Distillation Column
746 S. Hernández et al. Fabricio Omar Barroso-Muñoz 1 Salvador Hernández 1 Juan Gabriel Segovia- Hernández 1 Héctor Hernández-Escoto 1 Vicente Rico-Ramírez 2 Rosa-Hilda Chávez 3 1 Departamento de Ingeniería
ia PU BLi s g C o M Pa K T Wa i n CD-1576
M h M y CD-1576 o M Pa g C n ar ia PU BLi s in K T Wa i n ed National Geography Standards National Geography Standards Teachers leading discussions while completing units and activities is a prerequisite
Synthesis of Azeotropic Separation Systems by Case-Based Reasoning
Synthesis of Azeotropic Separation Systems by Case-Based Reasoning Timo Seuranen 1, Elina Pajula 2, Markku Hurme 1 1 Helsinki University of Technology, Laboratory of Plant Design, P.O. Box 6100, FIN-02015