A New Thermodynamic Correlation for Apparent Henry's Law Constants, Infinite Dilution Activity Coefficient and Solubility of M
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
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. -
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. -
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. -
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. -
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. -
Dissociation Constants and Ph-Titration Curves at Constant Ionic Strength from Electrometric Titrations in Cells Without Liquid
U. S. DEPARTMENT OF COMMERCE NATIONAL BUREAU OF STANDARDS RESEARCH PAPER RP1537 Part of Journal of Research of the N.ational Bureau of Standards, Volume 30, May 1943 DISSOCIATION CONSTANTS AND pH-TITRATION CURVES AT CONSTANT IONIC STRENGTH FROM ELECTRO METRIC TITRATIONS IN CELLS WITHOUT LIQUID JUNCTION : TITRATIONS OF FORMIC ACID AND ACETIC ACID By Roger G. Bates, Gerda L. Siegel, and S. F. Acree ABSTRACT An improved method for obtaining the titration curves of monobasic acids is outlined. The sample, 0.005 mole of the sodium salt of the weak acid, is dissolver! in 100 ml of a 0.05-m solution of sodium chloride and titrated electrometrically with an acid-salt mixture in a hydrogen-silver-chloride cell without liquid junction. The acid-salt mixture has the composition: nitric acid, 0.1 m; pot assium nitrate, 0.05 m; sodium chloride, 0.05 m. The titration therefore is performed in a. medium of constant chloride concentration and of practically unchanging ionic strength (1'=0.1) . The calculations of pH values and of dissociation constants from the emf values are outlined. The tit ration curves and dissociation constants of formic acid and of acetic acid at 25 0 C were obtained by this method. The pK values (negative logarithms of the dissociation constants) were found to be 3.742 and 4. 754, respectively. CONTENTS Page I . Tntroduction __ _____ ~ __ _______ . ______ __ ______ ____ ________________ 347 II. Discussion of the titrat ion metbod __ __ ___ ______ _______ ______ ______ _ 348 1. Ti t;at~on. clU,:es at constant ionic strength from cells without ltqUld JunctlOlL - - - _ - __ _ - __ __ ____ ____ _____ __ _____ ____ __ _ 349 2. -
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). -
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. -
Simple Mixtures
Simple mixtures Before dealing with chemical reactions, here we consider mixtures of substances that do not react together. At this stage we deal mainly with binary mixtures (mixtures of two components, A and B). We therefore often be able to simplify equations using the relation xA + xB = 1. A restriction in this chapter – we consider mainly non-electrolyte solutions – the solute is not present as ions. The thermodynamic description of mixtures We already considered the partial pressure – the contribution of one component to the total pressure, when we were dealing with the properties of gas mixtures. Here we introduce other analogous partial properties. Partial molar quantities: describe the contribution (per mole) that a substance makes to an overall property of mixture. The partial molar volume, VJ – the contribution J makes to the total volume of a mixture. Although 1 mol of a substance has a characteristic volume when it is pure, 1 mol of a substance can make different contributions to the total volume of a mixture because molecules pack together in different ways in the pure substances and in mixtures. Imagine a huge volume of pure water. When a further 1 3 mol H2O is added, the volume increases by 18 cm . When we add 1 mol H2O to a huge volume of pure ethanol, the volume increases by only 14 cm3. 18 cm3 – the volume occupied per mole of water molecules in pure water. 14 cm3 – the volume occupied per mole of water molecules in virtually pure ethanol. The partial molar volume of water in pure water is 18 cm3 and the partial molar volume of water in pure ethanol is 14 cm3 – there is so much ethanol present that each H2O molecule is surrounded by ethanol molecules and the packing of the molecules results in the water molecules occupying only 14 cm3. -
Chapter 9 Ideal and Real Solutions
2/26/2016 CHAPTER 9 IDEAL AND REAL SOLUTIONS • Raoult’s law: ideal solution • Henry’s law: real solution • Activity: correlation with chemical potential and chemical equilibrium Ideal Solution • Raoult’s law: The partial pressure (Pi) of each component in a solution is directly proportional to the vapor pressure of the corresponding pure substance (Pi*) and that the proportionality constant is the mole fraction (xi) of the component in the liquid • Ideal solution • any liquid that obeys Raoult’s law • In a binary liquid, A-A, A-B, and B-B interactions are equally strong 1 2/26/2016 Chemical Potential of a Component in the Gas and Solution Phases • If the liquid and vapor phases of a solution are in equilibrium • For a pure liquid, Ideal Solution • ∆ ∑ Similar to ideal gas mixing • ∆ ∑ 2 2/26/2016 Example 9.2 • An ideal solution is made from 5 mole of benzene and 3.25 mole of toluene. (a) Calculate Gmixing and Smixing at 298 K and 1 bar. (b) Is mixing a spontaneous process? ∆ ∆ Ideal Solution Model for Binary Solutions • Both components obey Rault’s law • Mole fractions in the vapor phase (yi) Benzene + DCE 3 2/26/2016 Ideal Solution Mole fraction in the vapor phase Variation of Total Pressure with x and y 4 2/26/2016 Average Composition (z) • , , , , ,, • In the liquid phase, • In the vapor phase, za x b yb x c yc Phase Rule • In a binary solution, F = C – p + 2 = 4 – p, as C = 2 5 2/26/2016 Example 9.3 • An ideal solution of 5 mole of benzene and 3.25 mole of toluene is placed in a piston and cylinder assembly. -
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. -
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.