DOCSLIB.ORG

Carbon Dioxide Capture by Chemical Absorption: a Solvent Comparison Study

Total Page：16

File Type：pdf, Size：1020Kb

Download full-text PDF Read full-text
Carbon Dioxide Capture by Chemical Absorption: a Solvent Comparison Study Carbon Dioxide Capture by Chemical Absorption: A Solvent Comparison Study by Anusha Kothandaraman B. Chem. Eng. Institute of Chemical Technology, University of Mumbai, 2005 M.S. Chemical Engineering Practice Massachusetts Institute of Technology, 2006 SUBMITTED TO THE DEPARTMENT OF CHEMICAL ENGINEERING IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF DOCTOR OF PHILOSOPHY IN CHEMICAL ENGINEERING PRACTICE AT THE MASSACHUSETTS INSTITUTE OF TECHNOLOGY JUNE 2010 © 2010 Massachusetts Institute of Technology All rights reserved. Signature of Author……………………………………………………………………………………… Department of Chemical Engineering May 20, 2010 Certified by……………………………………………………….………………………………… Gregory J. McRae Hoyt C. Hottel Professor of Chemical Engineering Thesis Supervisor Accepted by……………………………………………………………………………….................... William M. Deen Carbon P. Dubbs Professor of Chemical Engineering Chairman, Committee for Graduate Students 1 2 Carbon Dioxide Capture by Chemical Absorption: A Solvent Comparison Study by Anusha Kothandaraman Submitted to the Department of Chemical Engineering on May 20, 2010 in partial fulfillment of the requirements of the Degree of Doctor of Philosophy in Chemical Engineering Practice Abstract In the light of increasing fears about climate change, greenhouse gas mitigation technologies have assumed growing importance. In the United States, energy related CO2 emissions accounted for 98% of the total emissions in 2007 with electricity generation accounting for 40% of the total1. Carbon capture and sequestration (CCS) is one of the options that can enable the utilization of fossil fuels with lower CO2 emissions. Of the different technologies for CO2 capture, capture of CO2 by chemical absorption is the technology that is closest to commercialization. While a number of different solvents for use in chemical absorption of CO2 have been proposed, a systematic comparison of performance of different solvents has not been performed and claims on the performance of different solvents vary widely. This thesis focuses on developing a consistent framework for an objective comparison of the performance of different solvents. This framework has been applied to evaluate the performance of three different solvents – monoethanolamine, potassium carbonate and chilled ammonia. In this thesis, comprehensive flowsheet models have been built for each of the solvent systems, using ASPEN Plus as the modeling tool. In order to ensure an objective and consistent comparison of the performance of different solvent systems, the representation of physical properties, thermodynamics and kinetics had to be verified and corrected as required in ASPEN Plus. The ASPEN RateSep module was used to facilitate the computation of mass transfer characteristics of the system for sizing calculations. For each solvent system, many parametric simulations were performed to identify the effect on energy consumption in the system. The overall energy consumption in the CO2 capture and compression system was calculated and an evaluation of the required equipment size for critical equipment in the system was performed. The degradation characteristics and environmental impact of the solvents were also investigated. In addition, different flowsheet configurations were explored to optimize the energy recuperation for each system. 3 Monoethanolamine (MEA) was evaluated as the base case system in this thesis. Simulations showed the energy penalty for CO2 capture from flue gas from coal-fired power plants to be 0.01572 kWh/gmol CO2. The energy penalty from CO2 regeneration accounted for 60% of the energy penalty while the compression work accounted for 30%. The process flexibility in the MEA system was limited by degradation reactions. It was found that different flowsheet configurations for energy recuperation in the MEA system did not improve energy efficiency significantly. Chilled ammonia was explored as an alternative to MEA for use in new coal-fired power plants as well as for retrofitting existing power plants. The overall energy penalty for CO2 capture in chilled ammonia was found to be higher than in the MEA system, though energy requirements for CO2 regeneration were found to be lower. The energy penalty for 85% capture of CO2 in the chilled ammonia system was estimated to be 0.021 kWh/gmol CO2. As compared to the MEA system, the breakdown of the energy requirements was different with refrigeration in the absorber accounting for 44% of the energy penalty. This illustrates the need to perform a systemwide comparison of different solvents in order to evaluate the performance of various solvent systems. The use of potassium carbonate as a solvent for CO2 capture was evaluated for use in Integrated Reforming Combined Cycle (IRCC) system. With potassium carbonate, a high partial pressure of CO2 in the flue gas is required. Different schemes for energy recuperation in the system were investigated and the energy consumption was reduced by 22% over the base case. An optimized version of the potassium carbonate flowsheet was developed for an IRCC application with a reboiler duty of 1980 kJ/kg. In conclusion, a framework for the comparison of the performance of different solvents for CO2 capture has been developed and the performance of monoethanolamine, chilled ammonia and potassium carbonate has been compared. From the standpoint of energy consumption, for existing power plants the use of MEA is found to be the best choice while for future design of power plants, potassium carbonate appears to be an attractive alternative. An economic analysis based on the technical findings in this thesis will help in identifying the optimal choices for various large, stationary sources of CO2. Thesis Supervisor: Gregory J. McRae Title: Hoyt C. Hottel Professor of Chemical Engineering 1: Energy Information Administration, Electric Power Annual 2007: A Summary. 2009: Washington D.C. 4 Acknowledgements I would like to begin by sincerely thanking my advisor, Prof. Greg McRae for his constant support, guidance and mentorship over the course of this thesis. He gave me the freedom to define my thesis statement and always acted as a very helpful sounding board for my ideas. Whenever I was bereft of ideas, my discussions with him and his insights always helped me get back on the right track. He has always encouraged me to explore a wide variety of opportunities. I have truly learnt a lot from him over the past 5 years and for this, I am very grateful. I would also like to thank my thesis committee members – Howard Herzog, Prof. William Green and Prof. Ahmed Ghoniem for their valuable suggestions and advice. My collaborators at NTNU – Prof. Olav Bolland and Lars Nord were always ready to help me in understanding the power cycles and power plant modeling and I thank them for their time and helpful discussions. I am also very thankful to Randy Field for all his help with the ASPEN modeling in this work. I am very grateful to the Norwegian Research Council, StatoilHyrdo, the Henry Bromfield Rogers Fellowship at MIT and the BPCL scholarship for the funding they have provided that has aided me greatly in the completion of this work. Past and present members of the McRae group have been great sources of cheer and comfort during the past 5 years and I am grateful to them for their support. I would like to thank Ingrid Berkelmans, Bo Gong, Alex Lewis, Mihai Anton, Ken Hu, Carolyn Seto, Adekunle Adeyemo, Arman Haidari, Chuang-Chung Lee, Sara Passone, Jeremy Johnson and Patrick deMan for their friendship over the years. I would also like to thank Joan Chisholm, Liz Webb and Mary Gallagher for their support over the years and for making my life at MIT so much easier. On a personal note, I know that this work could not have been completed without the tremendous support of my friends and family. I would like to thank my friends at MIT for all the good memories they have provided over the past few years. Ravi has been a great source of strength and support for me through each step of the journey and I thank him for his constant encouragement, optimism and belief in me. Finally, my gratitude to my parents is beyond measure – all through my life, they have always sacrificed to ensure that I had the best opportunities possible and they have constantly believed in me and encouraged me to dream big and to pursue those dreams. I cannot put into words what their support has meant to me over the years and I dedicate this thesis to them. 5 Table of contents CHAPTER 1: INTRODUCTION.................................................................................. 24 1.1 Motivation for carbon capture and sequestration ........................................... 24 1.2 Brief overview of CO2 capture systems............................................................. 26 1.2.1 Post-combustion capture............................................................................... 27 1.2.2 Oxyfuel combustion...................................................................................... 29 1.2.3 Chemical looping combustion ...................................................................... 32 1.2.4 Precombustion capture.................................................................................. 34 1.3 Current status of CO2 capture technology ....................................................... 40 1.4 Solvent systems for chemical absorption .......................................................... 43 1.5 Thesis objectives.................................................................................................
Load more

Recommended publications
  • Understanding Variation in Partition Coefficient, Kd, Values: Volume II
    United States Office of Air and Radiation EPA 402-R-99-004B Environmental Protection August 1999 Agency UNDERSTANDING VARIATION IN PARTITION COEFFICIENT, Kd, VALUES Volume II: Review of Geochemistry and Available Kd Values for Cadmium, Cesium, Chromium, Lead, Plutonium, Radon, Strontium, Thorium, Tritium (3H), and Uranium UNDERSTANDING VARIATION IN PARTITION COEFFICIENT, Kd, VALUES Volume II: Review of Geochemistry and Available Kd Values for Cadmium, Cesium, Chromium, Lead, Plutonium, Radon, Strontium, Thorium, Tritium (3H), and Uranium August 1999 A Cooperative Effort By: Office of Radiation and Indoor Air Office of Solid Waste and Emergency Response U.S. Environmental Protection Agency Washington, DC 20460 Office of Environmental Restoration U.S. Department of Energy Washington, DC 20585 NOTICE The following two-volume report is intended solely as guidance to EPA and other environmental professionals. This document does not constitute rulemaking by the Agency, and cannot be relied on to create a substantive or procedural right enforceable by any party in litigation with the United States. EPA may take action that is at variance with the information, policies, and procedures in this document and may change them at any time without public notice. Reference herein to any specific commercial products, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government. ii FOREWORD Understanding the long-term behavior of contaminants in the subsurface is becoming increasingly more important as the nation addresses groundwater contamination. Groundwater contamination is a national concern as about 50 percent of the United States population receives its drinking water from groundwater.
    [Show full text]
  • Solubility and Aggregation of Selected Proteins Interpreted on the Basis of Hydrophobicity Distribution
    International Journal of Molecular Sciences Article Solubility and Aggregation of Selected Proteins Interpreted on the Basis of Hydrophobicity Distribution Magdalena Ptak-Kaczor 1,2, Mateusz Banach 1 , Katarzyna Stapor 3 , Piotr Fabian 3 , Leszek Konieczny 4 and Irena Roterman 1,2,* 1 Department of Bioinformatics and Telemedicine, Jagiellonian University—Medical College, Medyczna 7, 30-688 Kraków, Poland; [email protected] (M.P.-K.); [email protected] (M.B.) 2 Faculty of Physics, Astronomy and Applied Computer Science, Jagiellonian University, Łojasiewicza 11, 30-348 Kraków, Poland 3 Institute of Computer Science, Silesian University of Technology, Akademicka 16, 44-100 Gliwice, Poland; [email protected] (K.S.); [email protected] (P.F.) 4 Chair of Medical Biochemistry—Jagiellonian University—Medical College, Kopernika 7, 31-034 Kraków, Poland; [email protected] * Correspondence: [email protected] Abstract: Protein solubility is based on the compatibility of the specific protein surface with the polar aquatic environment. The exposure of polar residues to the protein surface promotes the protein’s solubility in the polar environment. The aquatic environment also influences the folding process by favoring the centralization of hydrophobic residues with the simultaneous exposure to polar residues. The degree of compatibility of the residue distribution, with the model of the concentration of hydrophobic residues in the center of the molecule, with the simultaneous exposure of polar residues is determined by the sequence of amino acids in the chain. The fuzzy oil drop model enables the quantification of the degree of compatibility of the hydrophobicity distribution Citation: Ptak-Kaczor, M.; Banach, M.; Stapor, K.; Fabian, P.; Konieczny, observed in the protein to a form fully consistent with the Gaussian 3D function, which expresses L.; Roterman, I.
    [Show full text]
  • Solubility & Density
    Natural Resources - Water WHAT’S SO SPECIAL ABOUT WATER: SOLUBILITY & DENSITY Activity Plan – Science Series ACTpa025 BACKGROUND Project Skills: Water is able to “dissolve” other substances. The molecules of water attract and • Discovery of chemical associate with the molecules of the substance that dissolves in it. Youth will have fun and physical properties discovering and using their critical thinking to determine why water can dissolve some of water. things and not others. Life Skills: • Critical thinking – Key vocabulary words: develops wider • Solvent is a substance that dissolves other substances, thus forming a solution. comprehension, has Water dissolves more substances than any other and is known as the “universal capacity to consider solvent.” more information • Density is a term to describe thickness of consistency or impenetrability. The scientific formula to determine density is mass divided by volume. Science Skills: • Hypothesis is an explanation for a set of facts that can be tested. (American • Making hypotheses Heritage Dictionary) • The atom is the smallest unit of matter that can take part in a chemical reaction. Academic Standards: It is the building block of matter. The activity complements • A molecule consists of two or more atoms chemically bonded together. this academic standard: • Science C.4.2. Use the WHAT TO DO science content being Activity: Density learned to ask questions, 1. Take a clear jar, add ¼ cup colored water, ¼ cup vegetable oil, and ¼ cup dark plan investigations, corn syrup slowly. Dark corn syrup is preferable to light so that it can easily be make observations, make distinguished from the oil. predictions and offer 2.
    [Show full text]
  • THE SOLUBILITY of GASES in LIQUIDS Introductory Information C
    THE SOLUBILITY OF GASES IN LIQUIDS Introductory Information C. L. Young, R. Battino, and H. L. Clever INTRODUCTION The Solubility Data Project aims to make a comprehensive search of the literature for data on the solubility of gases, liquids and solids in liquids. Data of suitable accuracy are compiled into data sheets set out in a uniform format. The data for each system are evaluated and where data of sufficient accuracy are available values are recommended and in some cases a smoothing equation is given to represent the variation of solubility with pressure and/or temperature. A text giving an evaluation and recommended values and the compiled data sheets are published on consecutive pages. The following paper by E. Wilhelm gives a rigorous thermodynamic treatment on the solubility of gases in liquids. DEFINITION OF GAS SOLUBILITY The distinction between vapor-liquid equilibria and the solubility of gases in liquids is arbitrary. It is generally accepted that the equilibrium set up at 300K between a typical gas such as argon and a liquid such as water is gas-liquid solubility whereas the equilibrium set up between hexane and cyclohexane at 350K is an example of vapor-liquid equilibrium. However, the distinction between gas-liquid solubility and vapor-liquid equilibrium is often not so clear. The equilibria set up between methane and propane above the critical temperature of methane and below the criti­ cal temperature of propane may be classed as vapor-liquid equilibrium or as gas-liquid solubility depending on the particular range of pressure considered and the particular worker concerned.
    [Show full text]
  • Modeling Gas Absorption
    Project Number: WMC 4028 Modeling Gas Absorption A Major Qualifying Project Report submitted to the Faculty of the WORCESTER POLYTECHNIC INSTITUTE in partial fulfillment of the requirements for the Degree of Bachelor of Science by _______________________________________ Yaminah Z. Jackson Date: April 24, 2008 Approved: _________________________________________ Professor William M. Clark, Project Advisor ABSTRACT This project sought to analyze the gas absorption process as an efficient way in which to remove pollutants, such as carbon dioxide from gas streams. The designed absorption lab for CM 4402 was used to collect data based on the change in composition throughout the column. The recorded and necessary calculated values were then used to create a simulation model using COMSOL Multiphysics, as a supplemental learning tool for students in CM 4402. 2 TABLE OF CONTENTS ABSTRACT ................................................................................................................................................................. 2 TABLE OF CONTENTS ............................................................................................................................................ 3 INTRODUCTION ....................................................................................................................................................... 5 ANTHROPOGENIC SOURCES ..................................................................................................................................... 5 FINDING A SOLUTION
    [Show full text]
  • THE SOLUBILITY of GASES in LIQUIDS INTRODUCTION the Solubility Data Project Aims to Make a Comprehensive Search of the Lit- Erat
    THE SOLUBILITY OF GASES IN LIQUIDS R. Battino, H. L. Clever and C. L. Young INTRODUCTION The Solubility Data Project aims to make a comprehensive search of the lit­ erature for data on the solubility of gases, liquids and solids in liquids. Data of suitable accuracy are compiled into data sheets set out in a uni­ form format. The data for each system are evaluated and where data of suf­ ficient accuracy are available values recommended and in some cases a smoothing equation suggested to represent the variation of solubility with pressure and/or temperature. A text giving an evaluation and recommended values and the compiled data sheets are pUblished on consecutive pages. DEFINITION OF GAS SOLUBILITY The distinction between vapor-liquid equilibria and the solUbility of gases in liquids is arbitrary. It is generally accepted that the equilibrium set up at 300K between a typical gas such as argon and a liquid such as water is gas liquid solubility whereas the equilibrium set up between hexane and cyclohexane at 350K is an example of vapor-liquid equilibrium. However, the distinction between gas-liquid solUbility and vapor-liquid equilibrium is often not so clear. The equilibria set up between methane and propane above the critical temperature of methane and below the critical temperature of propane may be classed as vapor-liquid equilibrium or as gas-liquid solu­ bility depending on the particular range of pressure considered and the par­ ticular worker concerned. The difficulty partly stems from our inability to rigorously distinguish between a gas, a vapor, and a liquid, which has been discussed in numerous textbooks.
    [Show full text]
  • Biotransformation: Basic Concepts (1)
    Chapter 5 Absorption, Distribution, Metabolism, and Elimination of Toxics Biotransformation: Basic Concepts (1) • Renal excretion of chemicals Biotransformation: Basic Concepts (2) • Biological basis for xenobiotic metabolism: – To convert lipid-soluble, non-polar, non-excretable forms of chemicals to water-soluble, polar forms that are excretable in bile and urine. – The transformation process may take place as a result of the interaction of the toxic substance with enzymes found primarily in the cell endoplasmic reticulum, cytoplasm, and mitochondria. – The liver is the primary organ where biotransformation occurs. Biotransformation: Basic Concepts (3) Biotransformation: Basic Concepts (4) • Interaction with these enzymes may change the toxicant to either a less or a more toxic form. • Generally, biotransformation occurs in two phases. – Phase I involves catabolic reactions that break down the toxicant into various components. • Catabolic reactions include oxidation, reduction, and hydrolysis. – Oxidation occurs when a molecule combines with oxygen, loses hydrogen, or loses one or more electrons. – Reduction occurs when a molecule combines with hydrogen, loses oxygen, or gains one or more electrons. – Hydrolysis is the process in which a chemical compound is split into smaller molecules by reacting with water. • In most cases these reactions make the chemical less toxic, more water soluble, and easier to excrete. Biotransformation: Basic Concepts (5) – Phase II reactions involves the binding of molecules to either the original toxic molecule or the toxic molecule metabolite derived from the Phase I reactions. The final product is usually water soluble and, therefore, easier to excrete from the body. • Phase II reactions include glucuronidation, sulfation, acetylation, methylation, conjugation with glutathione, and conjugation with amino acids (such as glycine, taurine, and glutamic acid).
    [Show full text]
  • Design Guidelines for Carbon Dioxide Scrubbers I
    "NCSCTECH MAN 4110-1-83 I (REVISION A) S00 TECHNICAL MANUAL tow DESIGN GUIDELINES FOR CARBON DIOXIDE SCRUBBERS I MAY 1983 REVISED JULY 1985 Prepared by M. L. NUCKOLS, A. PURER, G. A. DEASON I OF * Approved for public release; , J 1"73 distribution unlimited NAVAL COASTAL SYSTEMS CENTER PANAMA CITY, FLORIDA 32407 85. .U 15 (O SECURITY CLASSIFICATION OF TNIS PAGE (When Data Entered) R O DOCULMENTATIONkB PAGE READ INSTRUCTIONS REPORT DOCUMENTATION~ PAGE BEFORE COMPLETING FORM 1. REPORT NUMBER 2a. GOVT AQCMCSION N (.SAECIP F.NTTSChALOG NUMBER "NCSC TECHMAN 4110-1-83 (Rev A) A, -NI ' 4. TITLE (and Subtitle) S. TYPE OF REPORT & PERIOD COVERED "Design Guidelines for Carbon Dioxide Scrubbers '" 6. PERFORMING ORG. REPORT N UMBER A' 7. AUTHOR(&) 8. CONTRACT OR GRANT NUMBER(S) M. L. Nuckols, A. Purer, and G. A. Deason 9. PERFORMING ORGANIZATION NAME AND ADDRESS 10. PROGRAM ELEMENT, PROJECT. TASK AREA 6t WORK UNIT NUMBERS Naval Coastal PanaaLSystems 3407Project CenterCty, S0394, Task Area Panama City, FL 32407210,WrUnt2 22102, Work Unit 02 II. CONTROLLING OFFICE NAME AND ADDRE1S t2. REPORT 3ATE May 1983 Rev. July 1985 13, NUMBER OF PAGES 69 14- MONI TORING AGENCY NAME & ADDRESS(if different from Controtling Office) 15. SECURITY CLASS. (of this report) UNCLASSIFIED ISa. OECL ASSI FICATION/DOWNGRADING _ __N•AEOULE 16. DISTRIBUTION STATEMENT (of thia Repott) Approved for public release; distribution unlimited. 17. DISTRIBUTION STATEMENT (of the abstract entered In Block 20, If different from Report) IS. SUPPLEMENTARY NOTES II. KEY WORDS (Continue on reverse side If noceassry and Identify by block number) Carbon Dioxide; Scrubbers; Absorption; Design; Life Support; Pressure; "Swimmer Diver; Environmental Effects; Diving., 20.
    [Show full text]
  • Computational and Experimental Models for the Prediction of Intestinal Drug Solubility and Absorption
    &RPSUHKHQVLYH6XPPDULHVRI8SSVDOD'LVVHUWDWLRQV IURPWKH)DFXOW\RI3KDUPDF\ &RPSXWDWLRQDODQG([SHULPHQWDO 0RGHOVIRUWKH3UHGLFWLRQ RI,QWHVWLQDO'UXJ6ROXELOLW\ DQG$EVRUSWLRQ %< &+5,67(/$6%(5*675g0 $&7$81,9(56,7$7,6836$/,(16,6 8336$/$ Dissertation for the Degree of Doctor of Philosophy (Faculty of Pharmacy) in Pharmaceutics presented at Uppsala University in 2003 ABSTRACT Bergström, C. A. S., 2003. Computational and Experimental Models for the Prediction of Intestinal Drug Solubility and Absorption. Acta Universitatis Upsaliensis. Comprehensive Summaries of Uppsala Dissertations from the Faculty of Pharmacy 295. 66 pp. Uppsala. ISBN 91-554-5747-9. New effective experimental techniques in medicinal chemistry and pharmacology have resulted in a vast increase in the number of pharmacologically interesting compounds. However, the number of new drugs undergoing clinical trial has not augmented at the same pace, which in part has been attributed to poor absorption of the compounds. The main objective of this thesis was to investigate whether computer-based models devised from calculated molecular descriptors can be used to predict aqueous drug solubility, an important property influencing the absorption process. For this purpose, both experimental and computational studies were performed. A new small-scale shake flask method for experimental solubility determination of crystalline compounds was devised. This method was used to experimentally determine solubility values used for the computational model development and to investigate the pH-dependent solubility of drugs. In the computer-based studies, rapidly calculated molecular descriptors were used to predict aqueous solubility and the melting point, a solid state characteristic of importance for the solubility. To predict the absorption process, drug permeability across the intestinal epithelium was also modeled.
    [Show full text]
  • Raoult's Law – Partition Law
    BAE 820 Physical Principles of Environmental Systems Henry’s Law - Raoult's Law – Partition law Dr. Zifei Liu Biological and Agricultural Engineering Henry's law • At a constant temperature, the amount of a given gas that dissolves in a given type and volume of liquid is directly proportional to the partial pressure of that gas in equilibrium with that liquid. Pi = KHCi • Where Pi is the partial pressure of the gaseous solute above the solution, C is the i William Henry concentration of the dissolved gas and KH (1774-1836) is Henry’s constant with the dimensions of pressure divided by concentration. KH is different for each solute-solvent pair. Biological and Agricultural Engineering 2 Henry's law For a gas mixture, Henry's law helps to predict the amount of each gas which will go into solution. When a gas is in contact with the surface of a liquid, the amount of the gas which will go into solution is proportional to the partial pressure of that gas. An equivalent way of stating the law is that the solubility of a gas in a liquid is directly proportional to the partial pressure of the gas above the liquid. the solubility of gases generally decreases with increasing temperature. A simple rationale for Henry's law is that if the partial pressure of a gas is twice as high, then on the average twice as many molecules will hit the liquid surface in a given time interval, Biological and Agricultural Engineering 3 Air-water equilibrium Dissolution Pg or Cg Air (atm, Pa, mol/L, ppm, …) At equilibrium, Pg KH = Caq Water Caq (mol/L, mole ratio, ppm, …) Volatilization Biological and Agricultural Engineering 4 Various units of the Henry’s constant (gases in water at 25ºC) Form of K =P/C K =C /P K =P/x K =C /C equation H, pc aq H, cp aq H, px H, cc aq gas Units L∙atm/mol mol/(L∙atm) atm dimensionless -3 4 -2 O2 769 1.3×10 4.26×10 3.18×10 -4 4 -2 N2 1639 6.1×10 9.08×10 1.49×10 -2 3 CO2 29 3.4×10 1.63×10 0.832 Since all KH may be referred to as Henry's law constants, we must be quite careful to check the units, and note which version of the equation is being used.
    [Show full text]
  • Capture of Co2 Using Water Scrubbing
    CAPTURE OF CO2 USING WATER SCRUBBING Report Number PH3/26 July 2000 This document has been prepared for the Executive Committee of the Programme. It is not a publication of the Operating Agent, International Energy Agency or its Secretariat. Title: Capture of CO2 using water scrubbing Reference number: PH3/26 Date issued: July 2000 Other remarks: Background to the Study The leading options for CO2 capture are based on scrubbing with regenerable solvents. A potentially simpler alternative would be once-through scrubbing with seawater, followed by direct discharge of the CO2-laden seawater into the deep ocean. This would avoid the cost, complexity and energy losses associated with regenerating the scrubbing solvent and compressing the CO2 gas. This report presents the results of a scoping study on options for CO2 capture using water scrubbing. The study was carried out for IEA GHG by URS New Zealand Ltd. (formerly Woodward Clyde (NZ) Ltd.) Approach Adopted A range of power generation processes involving seawater scrubbing has been examined. A scoping assessment has been carried out to identify the most promising processes based on coal and natural gas fuels. Outline designs of CO2 capture processes have been prepared and comparative plant performances and costs estimated. From this, the key parameters that influence the potential for water-based capture processes are identified and the sensitivity of costs and performance to variations in these parameters assessed. CO2-la den seawater would normally need to be discharged at depths greater than about 1500m, to minimise environmental impacts and to ensure that the CO2 remained in the ocean for a long period of time.
    [Show full text]
  • Test Chemical Solubility Protocol
    Test Method Protocol for Solubility Determination Phase III - Validation Study September 24, 2003 TEST METHOD PROTOCOL for Solubility Determination In Vitro Cytotoxicity Validation Study Phase III September 24, 2003 Prepared by The National Toxicology Program (NTP) Interagency Center for the Evaluation of Alternative Toxicological Methods (NICEATM) Based on Standard Operating Procedure Recommendations from an International Workshop Organized by the Interagency Coordinating Committee on the Validation of Alternative Methods (ICCVAM) National Institute of Environmental Health Sciences (NIEHS) National Institutes of Health (NIH) U.S. Public Health Service Department of Health and Human Services 1 Test Method Protocol for Solubility Determination Phase III - Validation Study September 24, 2003 TEST METHOD PROTOCOL Solubility Determination Phase III I. PURPOSE The purpose of this study is to evaluate the cytotoxicity of test chemicals using the BALB/c 3T3 Neutral Red Uptake (NRU) and normal human keratinocyte (NHK) cytotoxicity tests. The data will be used to evaluate the intra- and inter-laboratory reproducibility of the assay and effectiveness of the cytotoxicity assay to predict the starting doses for rodent acute oral systemic toxicity assays. This test method protocol outlines the procedures for performing solubility determinations for the in vitro validation study organized by NICEATM and the European Centre for the Validation of Alternative Methods (ECVAM) and sponsored by NIEHS, U.S. Environmental Protection Agency, and ECVAM. This test method protocol applies to all personnel involved with performing the solubility testing. A. Solubility Test The solubility tests will be performed to determine the best solvent to use for each of the 60 blinded/coded test chemicals to be tested in the 3T3 and NHK NRU cytotoxicity tests II.
    [Show full text]