Summit:Technology and Opportunity

Size: px
Start display at page:

Download "Summit:Technology and Opportunity"

Transcription

1 Study of the gas-liquid CO 2 absorption in aqueous monoethanolamine solutions: development of a new experimental tool C. Wylock, S. Dehaeck, E. Boulay, P. Colinet and B. Haut CO 2 Summit:Technology and Opportunity Vail, USA June, 7 th, 2010 Applied Science Faculty, Université Libre de Bruxelles

2 CO 2 capture process by Cansolv Technologies Inc. Absorption in amine solutions regeneration by boiling Packed column Applied Science Faculty, Université Libre de Bruxelles Page 2

3 Best amine selection Target : Fast reactivity with CO 2 High absorption capacity Low energy (heating) regeneration cost High stability Screening of several amine mixtures Applied Science Faculty, Université Libre de Bruxelles Page 3

4 This work Propose a new experimental tool to determine the gas-liquid mass transfer coefficient Will (hopefully) contribute to: Amine selection Absorber design Applied on monoethanolamine (MEA) as a test case Applied Science Faculty, Université Libre de Bruxelles Page 4

5 Outline Description of the tool and procedure Experimental setup Overview of the procedure Mathematical modeling Calibration Mass transfer coefficient estimation Results and discussion Conclusion Applied Science Faculty, Université Libre de Bruxelles Page 5

6 Experimental setup The absorption of a pure gaseous CO 2 in an aqueous MEA solution is realized in a Hele-Shaw cell Applied Science Faculty, Université Libre de Bruxelles Page 6

7 Experimental setup The absorption of a pure gaseous CO 2 in an aqueous MEA solution is realized in a Hele-Shaw cell CO 2 Water-MEA Applied Science Faculty, Université Libre de Bruxelles Page 7

8 Experimental setup The absorption of a pure gaseous CO 2 in an aqueous MEA solution is realized in a Hele-Shaw cell CO 2 Water-MEA Refractive index variations in the liquid phase induced by this absorption are visualized using a Mach- Zehnder interferometer Applied Science Faculty, Université Libre de Bruxelles Page 8

9 Experimental setup Mach-Zehnder interferometer (MZI) block-diagram Applied Science Faculty, Université Libre de Bruxelles Page 9

10 Experimental setup Refractive index variations are computed from the interferogram variations thanks to an image processing program (Dehaeck et al., 2008) Applied Science Faculty, Université Libre de Bruxelles Page 10

11 Experimental setup Refractive index variations are computed from the interferogram variations thanks to an image processing program (Dehaeck et al., 2008) Time evolution of the refractive index profiles Modeling of the phenomena by a 1-D model Applied Science Faculty, Université Libre de Bruxelles Page 11

12 Overview of the procedure Gas-liquid absorption experiments 1-D mass transfer model (with physico-chemical parameters) MZI Experimental profiles of refractive index variation n exp Parameter fitting Equation solver Simulated profiles of concentration variation C sim COMPARISON Simulated profiles of refractive index variation n sim Calibration by refractometry correlation n = f ( C ) Applied Science Faculty, Université Libre de Bruxelles Page 12

13 Overview of the procedure Gas-liquid absorption experiments 1-D mass transfer model (with physico-chemical parameters) MZI Experimental profiles of refractive index variation n exp Parameter fitting Equation solver Simulated profiles of concentration variation C sim COMPARISON Simulated profiles of refractive index variation n sim Calibration by refractometry correlation n = f ( C ) Applied Science Faculty, Université Libre de Bruxelles Page 13

14 Mathematical modeling Schematic view of the gas-liquid absorption (MEA = RNH 2 with R = CH 2 CH 2 OH) x=0 Gas - liquid equilibrium Diffusion Gaseous phase Interface MEA aqueous solution (close to the interface) Chemical reactions X Depth in the liquid phase Page 14

15 Mathematical modeling Mass transfer equations in the liquid phase + appropriate boundary and initial conditions with Applied Science Faculty, Université Libre de Bruxelles Page 15

16 Mathematical modeling Equations solved using the COMSOL Multiphysics software time evolution of the concentration profiles Converted into refractive index profiles by calibration Applied Science Faculty, Université Libre de Bruxelles Page 16

17 Overview of the procedure Gas-liquid absorption experiments 1-D mass transfer model (with physico-chemical parameters) MZI Experimental profiles of refractive index variation n exp Parameter fitting Equation solver Simulated profiles of concentration variation C sim COMPARISON Simulated profiles of refractive index variation n sim Calibration by refractometry correlation n = f ( C ) Applied Science Faculty, Université Libre de Bruxelles Page 17

18 Calibration Calibration curves identified by refractometry n measured for several concentrations in MEA n measured for several concentrations in MEA and several dissolved CO 2 amount Applied Science Faculty, Université Libre de Bruxelles Page 18

19 Overview of the procedure Gas-liquid absorption experiments 1-D mass transfer model (with physico-chemical parameters) MZI Experimental profiles of refractive index variation n exp Parameter fitting Equation solver Simulated profiles of concentration variation C sim COMPARISON Simulated profiles of refractive index variation n sim Calibration by refractometry correlation n = f ( C ) Applied Science Faculty, Université Libre de Bruxelles Page 19

20 Parameter fitting Method Let and be the experimental and the simulated (with a parameter set P) refractive index variation at time t j and position x i, respectively Estimation of P that minimizes using the fminsearch routine of COMSOL Script Comparison Simulated profiles Parameter fitting Experimental profiles Applied Science Faculty, Université Libre de Bruxelles Page 20

21 Results and discussion Comparison of experiments (dot) and simulated (dash) A good comparison is observed when fitted parameters are used Fitting OK Physico-chemical parameter estimation Parameters Fitted value Literature value D RNH2 [m 2 /s] k 1 [m 3 /mol s] h CO2 [mol/m 3 Pa] A good agreement is obtained A. Aboudheir et al., CES, 58, 5195 W. van Swaaij, et al, CES, 39, 207 W. van Swaaij et al., JCE Data, 33, 29 Applied Science Faculty, Université Libre de Bruxelles Page 21

22 Conclusion Simulated refractive index variation profiles (using fitted parameter values): agree pretty well with experimental profiles Fitted parameter values: in agreement with values estimated using literature correlations Procedure seems operational for the CO 2 absorption in MEA aqueous solutions Will be applied to study gas-liquid CO 2 absorption in solvents provided by Cansolv Applied Science Faculty, Université Libre de Bruxelles Page 22

23 Thanks for your kind attention.

Experimental study of CO 2 absorption dynamics in an aqueous amine solution using Mach-Zehnder interferometry

Experimental study of CO 2 absorption dynamics in an aqueous amine solution using Mach-Zehnder interferometry Experimental study of CO 2 absorption dynamics in an aqueous amine solution using Mach-Zehnder interferometry C. Wylock, S. Dehaeck, D. Alonso, P. Colinet and B. Haut GLS - 11 Coex, Seoul, Korea August,

More information

COMPARTMENTAL MODELLING OF AN INDUSTRIAL BUBBLE COLUMN

COMPARTMENTAL MODELLING OF AN INDUSTRIAL BUBBLE COLUMN COMPARTMENTAL MODELLING OF AN INDUSTRIAL BUBBLE COLUMN Christophe Wylock 1, Aurélie Larcy 1, Thierry Cartage 2, Benoît Haut 1 1 Transfers, Interfaces and Processes (TIPs) Chemical Engineering Unit, Université

More information

Transfer Rate in a Reacting Flow for the Refined Sodium Bicarbonate Production Process

Transfer Rate in a Reacting Flow for the Refined Sodium Bicarbonate Production Process Presented at the COMSOL Conference 2008 Hannover COMSOL Conference Hannover November, 6 th, 2008 Study of the CO 2 Transfer Rate in a Reacting Flow for the Refined Sodium Bicarbonate Production Process

More information

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

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

More information

Available online at ScienceDirect. Energy Procedia 63 (2014 ) GHGT USA

Available online at  ScienceDirect. Energy Procedia 63 (2014 ) GHGT USA Available online at www.sciencedirect.com ScienceDirect Energy Procedia 63 (2014 ) 1487 1496 GHGT-12 CO 2 mass transfer and solubility in aqueous primary and secondary amine Le Li a, Gary Rochelle a, *

More information

A rational approach to amine mixture formulation for CO 2 capture applications. Trondheim CCS Conference - 6 June 14 16, 2011 Graeme Puxty

A rational approach to amine mixture formulation for CO 2 capture applications. Trondheim CCS Conference - 6 June 14 16, 2011 Graeme Puxty A rational approach to amine mixture formulation for CO 2 capture applications Trondheim CCS Conference - 6 June 14 16, 2011 Graeme Puxty The ideal solvent for CO 2 post-combustion capture: Process challenges

More information

Development of reactive chemical absorbents at the CSIRO

Development of reactive chemical absorbents at the CSIRO Development of reactive chemical absorbents at the CSIRO HiPerCap Workshop, March 25 2015 Graeme Puxty Research Team Leader CSIRO ENERGY FLAGSHIP CSIRO s chemical absorbent research program Concept Kinetics,

More information

Py x P P P. Py x P. sat. dq du PdV. abs Q S. An Innovative Approach in the G U TS PV P P G U TS PV T H U PV H U PV. abs. Py x P. sat.

Py x P P P. Py x P. sat. dq du PdV. abs Q S. An Innovative Approach in the G U TS PV P P G U TS PV T H U PV H U PV. abs. Py x P. sat. E a 1 1 sat sat ln Py x P Py x P K H k Ae R E sat a Py x P 1 1 sat ln K1 R Py x P K H k Ae R 1 CO P H 1 1 abs ln K H H 1/ R Q C 1 1 CO P ln S K H K1 R 1 P H abs H P K1 R CP 1 K1 R 1/ R S Q P 1 E a E du

More information

MASS TRANSFER AND GAS ABSORPTION EQUIPMENT

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

More information

Mass 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 Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module - 4 Absorption Lecture - 3 Packed Tower Design Part 2 (Refer Slide

More information

Carbon dioxide removal processes by alkanolamines in aqueous organic solvents Hamborg, Espen Steinseth

Carbon dioxide removal processes by alkanolamines in aqueous organic solvents Hamborg, Espen Steinseth University of Groningen Carbon dioxide removal processes by alkanolamines in aqueous organic solvents Hamborg, Espen Steinseth IMPORTANT NOTE: You are advised to consult the publisher's version (publisher's

More information

Finite Element Modules for Enhancing Undergraduate Transport Courses: Application to Fuel Cell Fundamentals

Finite Element Modules for Enhancing Undergraduate Transport Courses: Application to Fuel Cell Fundamentals Finite Element Modules for Enhancing Undergraduate Transport Courses: Application to Fuel Cell Fundamentals Originally published in 007 American Society for Engineering Education Conference Proceedings

More information

Mass Transfer in a Small Scale Flue Gas Absorber Experimental and Modeling

Mass Transfer in a Small Scale Flue Gas Absorber Experimental and Modeling Mass Transfer in a Small Scale Flue Gas Absorber Experimental and Modeling P.J.G. Huttenhuis, E.P. van Elk, S. Van Loo, G.F. Versteeg Procede Gas Treating B.V., The Netherlands 11 th MEETING of the INTERNATIONAL

More information

Non-intrusive sensing of air velocity, humidity, and temperature using TDLAS

Non-intrusive sensing of air velocity, humidity, and temperature using TDLAS Non-intrusive sensing of air velocity, humidity, and temperature using TDLAS TDLAS: Tunable Diode Laser Absorption Spectroscopy Suhyeon Park Mechanical Engineering, Virginia Tech Advisor Dr. Lin Ma Aerospace

More information

Computational Fluid Dynamic Study On The Decomposition Of Methane Gas Into Hydrogen And Solid Carbon In A Packed Bed Fluid Catalytic Cracking Reactor

Computational Fluid Dynamic Study On The Decomposition Of Methane Gas Into Hydrogen And Solid Carbon In A Packed Bed Fluid Catalytic Cracking Reactor IOSR Journal of Applied Chemistry (IOSR-JAC) e-issn: 2278-5736. Volume 4, Issue 2 (Mar. Apr. 2013), PP 32-41 Computational Fluid Dynamic Study On The Decomposition Of Methane Gas Into Hydrogen And Solid

More information

Chapter Four. Experimental

Chapter Four. Experimental Chapter Four 4.1 Materials N,N-Diethyl monoethanolamine (purity 98%) used in all experiments was purchased from Spectrochem Pvt. Ltd., Mumbai. N-Ethyl monoethanolamine, N-(- aminoethyl)ethanolamine, diethanolamine,

More information

Optimal design of a CO 2 absorption unit and assessment of solvent degradation

Optimal design of a CO 2 absorption unit and assessment of solvent degradation Optimal design of a CO 2 absorption unit and assessment of solvent degradation Mid-term Presentation Grégoire Léonard Table of Content 1. Introduction 2. Objectives 3. Modeling and optimal design 4. Solvent

More information

Available online at Energy Procedia 1 (2009) (2008) GHGT-9

Available online at  Energy Procedia 1 (2009) (2008) GHGT-9 Available online at www.sciencedirect.com Energy Procedia 1 (2009) (2008) 1257 1264 000 000 Energy Procedia www.elsevier.com/locate/procedia www.elsevier.com/locate/xxx GHGT-9 Solubility of CO 2 in Aqueous

More information

MODELING AND EXPERIMENTAL STUDY OF CARBON DIOXIDE ABSORPTION INTO AQUEOUS AMINE BASED SOLVENTS

MODELING AND EXPERIMENTAL STUDY OF CARBON DIOXIDE ABSORPTION INTO AQUEOUS AMINE BASED SOLVENTS Distillation Absorption 010 A.B. de Haan, H. Kooijman and A. Górak (Editors) All rights reserved by authors as per DA010 copyright notice MODELING AND EXPERIMENTAL STUDY OF CARBON DIOXIDE ABSORPTION INTO

More information

5. What is the name of the phase transition that occurs when a solid is converted directly into a gas (without going through the liquid phase)?

5. What is the name of the phase transition that occurs when a solid is converted directly into a gas (without going through the liquid phase)? 1. If the volume of a confined gas is doubled while the temperature remains constant, what change (if any) would be observed in the pressure? a. It would be half as large. b. It would double. c. It would

More information

Part I.

Part I. Part I bblee@unimp . Introduction to Mass Transfer and Diffusion 2. Molecular Diffusion in Gasses 3. Molecular Diffusion in Liquids Part I 4. Molecular Diffusion in Biological Solutions and Gels 5. Molecular

More information

CHEM 254 EXPERIMENT 7. Phase Diagrams - Liquid Vapour Equilibrium for two component solutions

CHEM 254 EXPERIMENT 7. Phase Diagrams - Liquid Vapour Equilibrium for two component solutions pressure CHEM 254 EXPERIMENT 7 Phase Diagrams - Liquid Vapour Equilibrium for two component solutions The partial pressures of the components of an ideal solution of two volatile liquids are related to

More information

PCC3 CONFERENCE The role of bicarbonate(hco 3- ) in the VLE of DEAB and blended MEA-DEAB systems under

PCC3 CONFERENCE The role of bicarbonate(hco 3- ) in the VLE of DEAB and blended MEA-DEAB systems under 1 PCC3 CONFERENCE The role of bicarbonate(hco 3- ) in the VLE of DEAB and blended MEA-DEAB systems under room and regeneration temperatures, an NMR study. Huancong Shi, 1, 2 Raphael Idem, 1 * Abdulaziz

More information

Kinetics of carbonate systems

Kinetics of carbonate systems 1 Kinetics of carbonate systems Hanna Knuutila Trondheim, 15 June 009 Outline Activity and concentration based kinetic constant Kinetic constant of infinite dilution Promotion Conclusions 3 String of discs

More information

Simulation of CO 2 removal in a split-flow gas sweetening process

Simulation of CO 2 removal in a split-flow gas sweetening process Korean J. Chem. Eng., 28(3), 643-648 (2011) DOI: 10.1007/s11814-010-0446-6 INVITED REVIEW PAPER Simulation of CO 2 removal in a split-flow gas sweetening process Hyung Kun Bae, Sung Young Kim, and Bomsock

More information

Digital Holographic Measurement of Nanometric Optical Excitation on Soft Matter by Optical Pressure and Photothermal Interactions

Digital Holographic Measurement of Nanometric Optical Excitation on Soft Matter by Optical Pressure and Photothermal Interactions Ph.D. Dissertation Defense September 5, 2012 Digital Holographic Measurement of Nanometric Optical Excitation on Soft Matter by Optical Pressure and Photothermal Interactions David C. Clark Digital Holography

More information

different model parameter correlations and thermodynamic models

different model parameter correlations and thermodynamic models 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 CO2 absorption into loaded aqueous MEA solutions: impact of different model parameter correlations and thermodynamic models on the absorption rate

More information

Diffusive Evolution of Gaseous and Hydrate Horizons of Methane in Seabed

Diffusive Evolution of Gaseous and Hydrate Horizons of Methane in Seabed Diffusive Evolution of Gaseous and Hydrate Horizons of Methane in Seabed Denis S. Goldobin (University of Leicester), et al. ( Quaternary Hydrate Stability ) MethaneNet Early Career Workshop Milton Keynes

More information

Heat of Absorption of CO 2 in Aqueous Solutions of DEEA, MAPA and their Mixture

Heat of Absorption of CO 2 in Aqueous Solutions of DEEA, MAPA and their Mixture Available online at www.sciencedirect.com Energy Procedia 37 (2013 ) 1532 1542 GHGT-11 Heat of Absorption of CO 2 in Aqueous Solutions of DEEA, MAPA and their Mixture Muhammad Waseem Arshad a, Nicolas

More information

Chapter 8: Physical Equilibria

Chapter 8: Physical Equilibria Chapter 8: Physical Equilibria Our first foray into equilibria is to examine phenomena associated with two phases of matter achieving equilibrium in which the free energy in each phase is the same and

More information

A NEW SOLVENT FOR CO2 CAPTURE R.

A NEW SOLVENT FOR CO2 CAPTURE R. A NEW SOLVENT FOR CO 2 CAPTURE R. Viscardi, G. Vanga and V. Barbarossa vincenzo.barbarossa@enea.it C.R. Casaccia ENEA; via Anguillarese, 301; 00123 S. M. Galeria-Roma Abstract This experimental study describes

More information

Simulation of gas sweetening process using new formulated amine solutions by developed package and HYSYS

Simulation of gas sweetening process using new formulated amine solutions by developed package and HYSYS Simulation of gas sweetening process using new formulated amine solutions by developed package and Mohammad Irani 1 ١, Reza Dorosti 2, Akbar Zamaniyan 1, Marziye Zare 1- Research Institute of Petroleum

More information

A Numerical Investigation of Laser Heating Including the Phase Change Process in Relation to Laser Drilling

A Numerical Investigation of Laser Heating Including the Phase Change Process in Relation to Laser Drilling A Numerical Investigation of Laser Heating Including the Phase Change Process in Relation to Laser Drilling I.Z. Naqavi, E. Savory & R.J. Martinuzzi Advanced Fluid Mechanics Research Group Department of

More information

Kinetic enhancement of adsorbent for CO2 capture from atmosphere by porous material

Kinetic enhancement of adsorbent for CO2 capture from atmosphere by porous material Engineering Conferences International ECI Digital Archives CO2 Summit II: Technologies and Opportunities Proceedings Spring 4-13-2016 Kinetic enhancement of adsorbent for CO2 capture from atmosphere by

More information

The reactions we have dealt with so far in chemistry are considered irreversible.

The reactions we have dealt with so far in chemistry are considered irreversible. 1. Equilibrium Students: model static and dynamic equilibrium and analyse the differences between open and closed systems investigate the relationship between collision theory and reaction rate in order

More information

CHAPTER 3 MODELLING AND ANALYSIS OF THE PACKED COLUMN

CHAPTER 3 MODELLING AND ANALYSIS OF THE PACKED COLUMN 37 CHAPTER 3 MODELLING AND ANALYSIS OF THE PACKED COLUMN Absorption in a chemical process refers to a mass transfer between gas and liquid which transfers one or more components from the gas phase to the

More information

AQUEOUS SOLUTIONS OF PYRROLIDINE FOR CARBON DIOXIDE CAPTURE

AQUEOUS SOLUTIONS OF PYRROLIDINE FOR CARBON DIOXIDE CAPTURE Distillation bsorption 21.B. de Haan, H. Kooijman and. Górak (Editors) ll rights reserved by authors as per D21 copyright notice QUEOUS SOLUTIONS OF PYRROLIDINE FOR CRBON DIOXIDE CPTURE ntonio Blanco,

More information

Analysis of Performance of Packed Columns

Analysis of Performance of Packed Columns Analysis of Performance of Packed Columns There are two packed column experiments in the Unit Operations lab: Liquid-Liquid Extraction (LLE) and Gas Absorption (GA). In both of these experiments, a solute

More information

Current status of R&D in post combustion CO 2 capture

Current status of R&D in post combustion CO 2 capture Current status of R&D in post combustion CO 2 capture Kaj Thomsen, Ph.D. Center for Energy Resources Engineering, CERE DTU Chemical Engineering Technical University of Denmark Outline Choice of solvent

More information

Multidimensional, Non-Isothermal, Dynamic Modelling Of Planar Solid Oxide Fuel Cells

Multidimensional, Non-Isothermal, Dynamic Modelling Of Planar Solid Oxide Fuel Cells Multidimensional, Non-Isothermal, Dynamic Modelling Of Planar Solid Oxide Fuel Cells K. Tseronis a, I. Kookos b, C. Theodoropoulos a* a School of Chemical Engineering and Analytical Science, University

More information

Rigorous Modeling of a CO 2 -MEA Stripping System

Rigorous Modeling of a CO 2 -MEA Stripping System A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 57, 2017 Guest Editors: Sauro Pierucci, Jiří Jaromír Klemeš, Laura Piazza, Serafim Bakalis Copyright 2017, AIDIC Servizi S.r.l. ISBN 978-88-95608-48-8;

More information

Chapter 10: CHM 2045 (Dr. Capps)

Chapter 10: CHM 2045 (Dr. Capps) Phase Diagram Phase diagrams for CO 2 and H 2 O Chapter 13. Solutions and Their Physical Properties Shows pressures and temperatures at which gaseous, liquid, and solid phases can exist. Allows us to predict

More information

CHEMICALLY-DRIVEN HYDRODYNAMIC INSTABILITIES. Anne De Wit Nonlinear Physical Chemistry Unit Université Libre de Bruxelles

CHEMICALLY-DRIVEN HYDRODYNAMIC INSTABILITIES. Anne De Wit Nonlinear Physical Chemistry Unit Université Libre de Bruxelles CHEMICALLY-DRIVEN HYDRODYNAMIC INSTABILITIES Anne De Wit Nonlinear Physical Chemistry Unit Université Libre de Bruxelles 1 Scientific questions Chemical reactions can induce changes in viscosity or density

More information

Understanding Transport Phenomena Concepts in Chemical Engineering with COMSOL Multiphysics

Understanding Transport Phenomena Concepts in Chemical Engineering with COMSOL Multiphysics Understanding Transport Phenomena Concepts in Chemical Engineering with COMSOL Multiphysics Erick S. Vasquez, Ph.D. Department of Chemical and Materials Engineering, University of Dayton, Dayton, OH, USA

More information

Kinetics of absorption of carbon dioxide in aqueous ammonia solutions Derks, P. W. J.; Versteeg, Geert

Kinetics of absorption of carbon dioxide in aqueous ammonia solutions Derks, P. W. J.; Versteeg, Geert University of Groningen Kinetics of absorption of carbon dioxide in aqueous ammonia solutions Ders, P. W. J.; Versteeg, Geert Published in: Energy Procedia DOI: 10.1016/j.egypro.009.01.150 IMPORTANT NOTE:

More information

PHASE CHEMISTRY AND COLLIGATIVE PROPERTIES

PHASE CHEMISTRY AND COLLIGATIVE PROPERTIES PHASE CHEMISTRY AND COLLIGATIVE PROPERTIES Phase Diagrams Solutions Solution Concentrations Colligative Properties Brown et al., Chapter 10, 385 394, Chapter 11, 423-437 CHEM120 Lecture Series Two : 2013/01

More information

Ionic Liquids for Post Combustion CO 2 -Absorption

Ionic Liquids for Post Combustion CO 2 -Absorption Ionic Liquids for Post Combustion CO 2 -Absorption 12th MEETING of the INTERNATIONAL POST-COMBUSTION CO 2 CAPTURE NETWORK David Wappel 1), Guenter Gronald 2), Roland Kalb 3) and Josef Draxler 1) 1) University

More information

Mathematical Modeling of Oil Shale Pyrolysis

Mathematical Modeling of Oil Shale Pyrolysis October, 19 th, 2011 Mathematical Modeling of Oil Shale Pyrolysis Pankaj Tiwari Jacob Bauman Milind Deo Department of Chemical Engineering University of Utah, Salt Lake City, Utah http://from50000feet.wordpress.com

More information

Faculty of Technology, Telemark University College, Kjølnes Ring 56, 3918 Porsgrunn, Norway. 2. Tel-Tek, Kjølnes Ring 30, 3918 Porsgrunn, Norway.

Faculty of Technology, Telemark University College, Kjølnes Ring 56, 3918 Porsgrunn, Norway. 2. Tel-Tek, Kjølnes Ring 30, 3918 Porsgrunn, Norway. Attempts to Predict Absorption Equilibria Klaus J. Jens 1,2, Dag A. Eimer 1,2, Bjørnar Arstad 3, Zulkifli Idris 1, Cristina Perinu 1, Gamunu Samarakoon 1 and John Arild Svendsen 1 1 Faculty of Technology,

More information

Separation through Dialysis

Separation through Dialysis Separation through Dialysis SOLVED WITH COMSOL MULTIPHYSICS 3.5a COPYRIGHT 2008. All right reserved. No part of this documentation may be photocopied or reproduced in any form without prior written consent

More information

Modeling Deep-Bed Grain Drying Using COMSOL Multiphysics

Modeling Deep-Bed Grain Drying Using COMSOL Multiphysics Modeling Deep-Bed Grain Drying Using COMSOL Multiphysics Ramadan ElGamal a,b, Frederik Ronsse a, Jan G. Pieters a, * a Faculty of Bioscience Engineering, Department of Biosystems Engineering, Coupure Links

More information

Humidity Mass Transfer Analysis in Packed Powder Detergents

Humidity Mass Transfer Analysis in Packed Powder Detergents Humidity Mass Transfer Analysis in Packed Powder Detergents Vincenzo Guida, Lino Scelsi, and Fabio Zonfrilli * 1 Procter & Gamble Research & Development *Corresponding author: Procter & Gamble, Via Ardeatina

More information

Chemical Equilibrium. Professor Bice Martincigh. Equilibrium

Chemical Equilibrium. Professor Bice Martincigh. Equilibrium Chemical Equilibrium by Professor Bice Martincigh Equilibrium involves reversible reactions Some reactions appear to go only in one direction are said to go to completion. indicated by All reactions are

More information

SAMPLE CHEMISTRY QUESTIONS MIXTURE OF UNIT 3 & 4 MATERIALS

SAMPLE CHEMISTRY QUESTIONS MIXTURE OF UNIT 3 & 4 MATERIALS SAMPLE CHEMISTRY QUESTIONS MIXTURE OF UNIT 3 & 4 MATERIALS QUESTION 1 The equation describing the production of butyl ethanoate is given below. Catalyst C4H 9OH CH 3COOH CH 3COOC 4H 9 H 2O( l ) 0.0500

More information

Viscosity data of aqueous MDEA [Bmim][BF 4 ] solutions within carbon capture operating conditions

Viscosity data of aqueous MDEA [Bmim][BF 4 ] solutions within carbon capture operating conditions Available online at www.sciencedirect.com Energy Procedia 00 (2016) 000 000 www.elsevier.com/locate/procedia The 8 th International Conference on Applied Energy ICAE2016 Viscosity data of aqueous MDEA

More information

Section 1 What Is a Solution? Chapter 13. Mixtures

Section 1 What Is a Solution? Chapter 13. Mixtures Mixtures Mixtures can either be heterogeneous or homogeneous. The particles of a heterogeneous mixture are large enough to see under a microscope. In a homogeneous mixture, however, the particles are molecule-sized,

More information

A Comparative Study of Carbon Capture for Different Power Plants

A Comparative Study of Carbon Capture for Different Power Plants 1783 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 45, 2015 Guest Editors: Petar Sabev Varbanov, Jiří Jaromír Klemeš, Sharifah Rafidah Wan Alwi, Jun Yow Yong, Xia Liu Copyright 2015, AIDIC Servizi

More information

Extract: A new Simulation Software for Liquid-Liquid Extraction Process

Extract: A new Simulation Software for Liquid-Liquid Extraction Process Extract: A new Simulation Software for Liquid-Liquid Extraction Process A. Hadj Seyd 1, Lanezt 2, M. L. Belfar 2, T. Gharib 1, A. Kemassi 3, F. Ben Brahim 3 1 University Mohamed Khider-Biskra. B.P. 145

More information

Modeling the next battery generation: Lithium-sulfur and lithium-air cells

Modeling the next battery generation: Lithium-sulfur and lithium-air cells Modeling the next battery generation: Lithium-sulfur and lithium-air cells D. N. Fronczek, T. Danner, B. Horstmann, Wolfgang G. Bessler German Aerospace Center (DLR) University Stuttgart (ITW) Helmholtz

More information

(ii) the total kinetic energy of the gas molecules (1 mark) (iii) the total potential energy of the gas molecules (1 mark)

(ii) the total kinetic energy of the gas molecules (1 mark) (iii) the total potential energy of the gas molecules (1 mark) NAME : F.5 ( ) Marks: /70 FORM FOUR PHYSICS REVISION TEST on HEAT Allowed: 70 minutes This paper consists of two sections. Section A (50 marks) consists of the structure-type questions, and Section B (20

More information

Comparison of Equilibrium- Stage and Rate Based Model of an Absorption Column for a CO2-MEA system

Comparison of Equilibrium- Stage and Rate Based Model of an Absorption Column for a CO2-MEA system Comparison of Equilibrium- Stage and Rate Based Model of an Absorption Column for a CO2-MEA system Comparison of Equilibrium-Stage and Rate Based Model of an Absorption Column for a CO2-MEA system By

More information

2 Copyright Pearson Education, Inc., or its affiliates. All Rights Reserved.

2 Copyright Pearson Education, Inc., or its affiliates. All Rights Reserved. CHEMISTRY & YOU Chapter 17 Thermochemistry 17.1 The Flow of Energy 17. Measuring and Expressing Enthalpy Changes 17.3 Heat in Changes of State 17.4 Calculating Heats of Reaction Why does sweating help

More information

DATA THAT YOU MAY USE UNITS Conventional Volume ml or cm 3 = cm 3 or 10-3 dm 3 Liter (L) = dm 3 Pressure atm = 760 torr = Pa CONSTANTS

DATA THAT YOU MAY USE UNITS Conventional Volume ml or cm 3 = cm 3 or 10-3 dm 3 Liter (L) = dm 3 Pressure atm = 760 torr = Pa CONSTANTS DATA THAT YOU MAY USE UNITS Conventional S.I. Volume ml or cm 3 = cm 3 or 0-3 dm 3 Liter (L) = dm 3 Pressure atm = 760 torr =.03 0 5 Pa torr = 33.3 Pa Temperature C 0 C = 73.5 K PV L-atm =.03 0 5 dm 3

More information

DETERMINATION OF KINETICS IN GAS-LIQUID REACTION SYSTEMS. AN OVERVIEW

DETERMINATION OF KINETICS IN GAS-LIQUID REACTION SYSTEMS. AN OVERVIEW DOI: 10.2478/v10216-011-0014-y ECOL CHEM ENG S. 2012; 19(2):175-196 Hanna KIERZKOWSKA-PAWLAK 1 DETERMINATION OF KINETICS IN GAS-LIQUID REACTION SYSTEMS. AN OVERVIEW PRZEGLĄD METOD WYZNACZANIA KINETYKI

More information

Solids, Liquids and Gases

Solids, Liquids and Gases WHY? Why is water usually a liquid and not a gas? Why does liquid water boil at such a high temperature for such a small molecule? Why does ice float on water? Why do snowflakes have 6 sides? Why is I

More information

Lecture 1: Physical Equilibria The Temperature Dependence of Vapor Pressure

Lecture 1: Physical Equilibria The Temperature Dependence of Vapor Pressure Lecture 1: Physical Equilibria The Temperature Dependence of Vapor Pressure Our first foray into equilibria is to examine phenomena associated with two phases of matter achieving equilibrium in which the

More information

Carbon dioxide removal processes by alkanolamines in aqueous organic solvents Hamborg, Espen Steinseth

Carbon dioxide removal processes by alkanolamines in aqueous organic solvents Hamborg, Espen Steinseth University of Groningen Carbon dioxide removal processes by alkanolamines in aqueous organic solvents Hamborg, Espen Steinseth IMPORTANT NOTE: You are advised to consult the publisher's version (publisher's

More information

Experimental study into carbon dioxide solubility and species distribution in aqueous alkanolamine solutions

Experimental study into carbon dioxide solubility and species distribution in aqueous alkanolamine solutions Air Pollution XX 515 Experimental study into carbon dioxide solubility and species distribution in aqueous alkanolamine solutions H. Yamada, T. Higashii, F. A. Chowdhury, K. Goto S. Kazama Research Institute

More information

Base your answers to questions 1 through 4 on the information below and on your knowledge of chemistry.

Base your answers to questions 1 through 4 on the information below and on your knowledge of chemistry. Base your answers to questions 1 through 4 on the information below and on your knowledge of A student prepares two 141-gram mixtures, A and B. Each mixture consists of, sand, and at 15 C. Both mixtures

More information

CH2351 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 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 information

Le Châtelier's Principle. Chemical Equilibria & the Application of Le Châtelier s Principle to General Equilibria. Using Le Châtelier's Principle

Le Châtelier's Principle. Chemical Equilibria & the Application of Le Châtelier s Principle to General Equilibria. Using Le Châtelier's Principle Chemical Equilibria & the Application of Le Châtelier s Principle to General Equilibria CHEM 107 T. Hughbanks Le Châtelier's Principle When a change is imposed on a system at equilibrium, the system will

More information

CO 2 CAPTURE BY ABSORPTION IN ACTIVATED AQUEOUS SOLUTIONS OF N,N-DIETHYLETHANOLOAMINE

CO 2 CAPTURE BY ABSORPTION IN ACTIVATED AQUEOUS SOLUTIONS OF N,N-DIETHYLETHANOLOAMINE DOI: 10.1515/eces-017-0016 EL CHEM ENG S. 017;4():39-48 Ewelina KRUSZCZAK 1 and Hanna KIERZKOWSKA-PAWLAK 1* CAPTURE BY ABSORPTION IN ACTIVATED AQUEOUS SOLUTIONS OF N,N-DIETHYLETHANOLOAMINE ABSORPCYJNE

More information

Modeling and Simulation of Absorption Column of Natural Gas Sweetening Unit by Mass Transfer Method

Modeling and Simulation of Absorption Column of Natural Gas Sweetening Unit by Mass Transfer Method Modeling and Simulation of Absorption Column of Natural Gas Sweetening Unit by Mass Transfer Method Mahmood Sahabi, Mansoor Shirvani*, Mohammad Reza Dehghani * Faculty of Chemical Engineering, Iran University

More information

ANSWERS CIRCLE CORRECT SECTION

ANSWERS CIRCLE CORRECT SECTION CHEMISTRY 162 - EXAM I June 08, 2009 Name: SIGN: RU ID Number Choose the one best answer for each question and write the letter preceding it in the appropriate space on this answer sheet. Only the answer

More information

Welcome to chemistry

Welcome to chemistry Welcome to chemistry Science a search for facts about the world around us understanding the past, predicting the future Aristotle (384-322 B.C.) one can work out all the laws that govern the universe by

More information

REMOVE THIS PAGE PRIOR TO STARTING EXAM.

REMOVE THIS PAGE PRIOR TO STARTING EXAM. REMOVE THIS PAGE PRIOR TO STARTING EXAM. 1 2 ANSWER KEY CHEMISTRY F14O3 SECOND EXAM 11/10/99 PROFESSOR J. MORROW PRINT NAME, LAST: FIRST: I.D.# : MAXIMUM POINT VALUE IS IN PARENTHESES 1. (15) 9. (15) 17.

More information

Chapter 17: Phenomena

Chapter 17: Phenomena Chapter 17: Phenomena Phenomena: Different masses of solute were added to 1 kg of either H 2 O or C 6 H 6. The boiling and freezing points of the solutions were then measured. Examine the data to determine

More information

Solutions. Chapter 14 Solutions. Ion-Ion Forces (Ionic Bonding) Attraction Between Ions and Permanent Dipoles. Covalent Bonding Forces

Solutions. Chapter 14 Solutions. Ion-Ion Forces (Ionic Bonding) Attraction Between Ions and Permanent Dipoles. Covalent Bonding Forces Solutions Chapter 14 1 Brief Review of Major Topics in Chapter 13, Intermolecular forces Ion-Ion Forces (Ionic Bonding) 2 Na + Cl - in salt These are the strongest forces. Lead to solids with high melting

More information

Comparison of Carbon Dioxide Absorption in Aqueous MEA, DEA, TEA, and AMP Solutions

Comparison of Carbon Dioxide Absorption in Aqueous MEA, DEA, TEA, and AMP Solutions Carbon Dioxide Capture Using Amine Solutions Bull. Korean Chem. Soc. 2013, Vol. 34, No. 3 783 http://dx.doi.org/10.5012/bkcs.2013.34.3.783 Comparison of Carbon Dioxide Absorption in Aqueous MEA, DEA, TEA,

More information

Regeneration Section of CO 2 Capture Plant by MEA Scrubbing with a Rate-Based Model

Regeneration Section of CO 2 Capture Plant by MEA Scrubbing with a Rate-Based Model A publication of 1849 CHEMICAL ENGINEERING TRANSACTIONS VOL. 3, 013 Chief Editors: Sauro Pierucci, Jiří J. Klemeš Copyright 013, AIDIC Servizi S.r.l., ISBN 978-88-95608-3-5; ISSN 1974-9791 The Italian

More information

Example 14.1 Expressing Equilibrium Constants for Chemical Equations

Example 14.1 Expressing Equilibrium Constants for Chemical Equations Example 14.1 Expressing Equilibrium Constants for Chemical Equations For Practice 14.1 Express the equilibrium constant for the combustion of propane as shown by the balanced chemical equation: Example

More information

(g) burns according to this reaction? D) CH 4 (g) + 2O 2 (g) CO 2 (g) + 2H 2 O(l)

(g) burns according to this reaction? D) CH 4 (g) + 2O 2 (g) CO 2 (g) + 2H 2 O(l) Name: 7171-1 - Page 1 1) In a chemical reaction, the difference between the potential energy of the products and the potential energy of the reactants is defined as the A) heat of reaction B) ionization

More information

Recap: Introduction 12/1/2015. EVE 402 Air Pollution Generation and Control. Adsorption

Recap: Introduction 12/1/2015. EVE 402 Air Pollution Generation and Control. Adsorption EVE 402 Air Pollution Generation and Control Chapter #6 Lectures Adsorption Recap: Solubility: the extent of absorption into the bulk liquid after the gas has diffused through the interface An internal

More information

Australian Journal of Basic and Applied Sciences

Australian Journal of Basic and Applied Sciences ISSN:1991-8178 Australian Journal of Basic and Applied Sciences Journal home page: www.ajbasweb.com Dynamic Modelling of Carbon Dioxide For Different Solvent Faezah Isa, Haslinda Zabiri, Pravin Chandran

More information

Science & Technologies SURFACE TENSION EFFECTS IN SIEVE PLATE DISTILLATION COLUMN

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

More information

2SO 2(g) + O 2(g) Increasing the temperature. (Total 1 mark) Enthalpy data for the reacting species are given in the table below.

2SO 2(g) + O 2(g) Increasing the temperature. (Total 1 mark) Enthalpy data for the reacting species are given in the table below. Q1.Which change would alter the value of the equilibrium constant (K p) for this reaction? 2SO 2(g) + O 2(g) 2SO 3(g) A Increasing the total pressure of the system. Increasing the concentration of sulfur

More information

1. All the solutions have the same molality. 2. All the solutions have the same molarity.

1. All the solutions have the same molality. 2. All the solutions have the same molarity. I. (41 points) A. (12 points) Write your answers on the blanks provided. 1. Which of the following solutes would be more soluble in water? a. CH 3 OH or C 17 H 35 OH b. C 2 H 5 Cl or NaCl c. CHCl 3 or

More information

C. S. R. Prasad, H. Z. Fani, S. B. Menon

C. S. R. Prasad, H. Z. Fani, S. B. Menon Heterogeneous Bunsen Reaction nalysis & Experimental study of Chemical absorption of Sulfur dioxide and dissolution of Iodine into aqueous reacting system C. S. R. Prasad, H. Z. Fani, S. B. Menon Chemical

More information

Reaction Monitoring in Chemical Engineering with Quantitative Online NMR Spectroscopy

Reaction Monitoring in Chemical Engineering with Quantitative Online NMR Spectroscopy Reaction Monitoring in Chemical Engineering with Quantitative nline MR Spectroscopy Hans Hasse 1, Sebastian Hoch 1, Erik von Harbou 1, Klaus Albert 2 1 Laboratory of, Technische Universität Kaiserslautern,

More information

SOLUTIONS. Chapter Test B. A. Matching. Column A. Column B. Name Date Class. 418 Core Teaching Resources

SOLUTIONS. Chapter Test B. A. Matching. Column A. Column B. Name Date Class. 418 Core Teaching Resources 16 SOLUTIONS Chapter Test B A. Matching Match each term in Column B to the correct description in Column A. Write the letter of the correct term on the line. Column A Column B 1. the number of moles of

More information

CFD Modeling of Hollow Fiber Membrane Contactor for Post-Combustion CO 2 Capture

CFD Modeling of Hollow Fiber Membrane Contactor for Post-Combustion CO 2 Capture 1 CFD Modeling of Hollow Fiber Membrane Contactor for Post-Combustion CO 2 Capture Muhammad Saeed, Liyuan Deng* Membrane Research Group (Memfo), Department of Chemical Engineering, Norwegian University

More information

Carbon dioxide removal by alkanolamines in aqueous organic solvents Hamborg, Espen S.; Derks, Peter W.J.; Elk, Edwin P. van; Versteeg, Geert F.

Carbon dioxide removal by alkanolamines in aqueous organic solvents Hamborg, Espen S.; Derks, Peter W.J.; Elk, Edwin P. van; Versteeg, Geert F. University of Groningen Carbon dioxide removal by alkanolamines in aqueous organic solvents Hamborg, Espen S.; Derks, Peter W.J.; Elk, Edwin P. van; Versteeg, Geert F. Published in: Energy Procedia DOI:

More information

Exercise 2-4. Titration of a Buffer Solution EXERCISE OBJECTIVES

Exercise 2-4. Titration of a Buffer Solution EXERCISE OBJECTIVES Exercise 2-4 Titration of a Buffer Solution EXERCISE OBJECTIVES To define the terms buffer solution and buffer capacity; To titrate a buffer solution with a weak acid solution; To plot a graph using the

More information

Solubility of carbon dioxide in aqueous solutions of 2-amino-2-ethyl-1,3-propanediol

Solubility of carbon dioxide in aqueous solutions of 2-amino-2-ethyl-1,3-propanediol Fluid Phase Equilibria 202 (2002) 359 366 Solubility of carbon dioxide in aqueous solutions of 2-amino-2-ethyl-1,3-propanediol Jung-Yeon Park a, Sang Jun Yoon a, Huen Lee a,, Ji-Ho Yoon b, Jae-Goo Shim

More information

Available online at ScienceDirect. Energy Procedia 63 (2014 ) GHGT-12

Available online at   ScienceDirect. Energy Procedia 63 (2014 ) GHGT-12 Available online at www.sciencedirect.com ScienceDirect Energy Procedia 63 (2014 ) 1854 1862 GHGT-12 Screening tests of new hybrid solvents for the post-combustion CO 2 capture process by chemical absorption

More information

Absorption of carbon dioxide into non-aqueous solutions of N-methyldiethanolamine

Absorption of carbon dioxide into non-aqueous solutions of N-methyldiethanolamine Korean J. Chem. Eng., 23(5), 806-811 (2006) SHORT COMMUNICATION Absorption of carbon dioxide into non-aqueous solutions of N-methyldiethanolamine Sang-Wook Park, Joon-Wook Lee, Byoung-Sik Choi and Jae-Wook

More information

Effect of Gas Flow Rate and Gas Composition in Ar/CH 4 Inductively Coupled Plasmas

Effect of Gas Flow Rate and Gas Composition in Ar/CH 4 Inductively Coupled Plasmas COMSOL CONFERENCE BOSTON 2011 Effect of Gas Flow Rate and Gas Composition in Ar/CH 4 Inductively Coupled Plasmas Keisoku Engineering System Co., Ltd., JAPAN Dr. Lizhu Tong October 14, 2011 1 Contents 1.

More information

Scale-up problems are often perceived as difficult. Here the reaction calorimetry has proven to be

Scale-up problems are often perceived as difficult. Here the reaction calorimetry has proven to be APPLICATION OF REACTION CALORIMETRY FOR THE SOLUTION OF SCALE-UP PROBLEMS A paper from the RC User Forum Europe, Interlaken, 1995 Francis Stoessel, Ciba AG, Basel, Switzerland. Scale-up problems are often

More information

Chromatography. Gas Chromatography

Chromatography. Gas Chromatography Chromatography Chromatography is essentially the separation of a mixture into its component parts for qualitative and quantitative analysis. The basis of separation is the partitioning of the analyte mixture

More information

DATE: POGIL: Colligative Properties Part 1

DATE: POGIL: Colligative Properties Part 1 NAME: AP Chemistry DATE: POGIL: Colligative Properties Part 1 Why? There is a general misconception that adding sodium chloride to cooking water for pasta increases the temperature of the boiling water

More information