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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. -
Henry's Law Constants and Micellar Partitioning of Volatile Organic
38 J. Chem. Eng. Data 2000, 45, 38-47 Henry’s Law Constants and Micellar Partitioning of Volatile Organic Compounds in Surfactant Solutions Leland M. Vane* and Eugene L. Giroux United States Environmental Protection Agency, National Risk Management Research Laboratory, 26 West Martin Luther King Drive, Cincinnati, Ohio 45268 Partitioning of volatile organic compounds (VOCs) into surfactant micelles affects the apparent vapor- liquid equilibrium of VOCs in surfactant solutions. This partitioning will complicate removal of VOCs from surfactant solutions by standard separation processes. Headspace experiments were performed to quantify the effect of four anionic surfactants and one nonionic surfactant on the Henry’s law constants of 1,1,1-trichloroethane, trichloroethylene, toluene, and tetrachloroethylene at temperatures ranging from 30 to 60 °C. Although the Henry’s law constant increased markedly with temperature for all solutions, the amount of VOC in micelles relative to that in the extramicellar region was comparatively insensitive to temperature. The effect of adding sodium chloride and isopropyl alcohol as cosolutes also was evaluated. Significant partitioning of VOCs into micelles was observed, with the micellar partitioning coefficient (tendency to partition from water into micelle) increasing according to the following series: trichloroethane < trichloroethylene < toluene < tetrachloroethylene. The addition of surfactant was capable of reversing the normal sequence observed in Henry’s law constants for these four VOCs. Introduction have long taken advantage of the high Hc values for these compounds. In the engineering field, the most common Vast quantities of organic solvents have been disposed method of dealing with chlorinated solvents dissolved in of in a manner which impacts human health and the groundwater is “pump & treat”swithdrawal of ground- environment. -
Solvent Effects on the Thermodynamic Functions of Dissociation of Anilines and Phenols
University of Wollongong Research Online University of Wollongong Thesis Collection 1954-2016 University of Wollongong Thesis Collections 1982 Solvent effects on the thermodynamic functions of dissociation of anilines and phenols Barkat A. Khawaja University of Wollongong Follow this and additional works at: https://ro.uow.edu.au/theses University of Wollongong Copyright Warning You may print or download ONE copy of this document for the purpose of your own research or study. The University does not authorise you to copy, communicate or otherwise make available electronically to any other person any copyright material contained on this site. You are reminded of the following: This work is copyright. Apart from any use permitted under the Copyright Act 1968, no part of this work may be reproduced by any process, nor may any other exclusive right be exercised, without the permission of the author. Copyright owners are entitled to take legal action against persons who infringe their copyright. A reproduction of material that is protected by copyright may be a copyright infringement. A court may impose penalties and award damages in relation to offences and infringements relating to copyright material. Higher penalties may apply, and higher damages may be awarded, for offences and infringements involving the conversion of material into digital or electronic form. Unless otherwise indicated, the views expressed in this thesis are those of the author and do not necessarily represent the views of the University of Wollongong. Recommended Citation Khawaja, Barkat A., Solvent effects on the thermodynamic functions of dissociation of anilines and phenols, Master of Science thesis, Department of Chemistry, University of Wollongong, 1982. -
Partition Coefficients in Mixed Surfactant Systems
Partition coefficients in mixed surfactant systems Application of multicomponent surfactant solutions in separation processes Vom Promotionsausschuss der Technischen Universität Hamburg-Harburg zur Erlangung des akademischen Grades Doktor-Ingenieur genehmigte Dissertation von Tanja Mehling aus Lohr am Main 2013 Gutachter 1. Gutachterin: Prof. Dr.-Ing. Irina Smirnova 2. Gutachterin: Prof. Dr. Gabriele Sadowski Prüfungsausschussvorsitzender Prof. Dr. Raimund Horn Tag der mündlichen Prüfung 20. Dezember 2013 ISBN 978-3-86247-433-2 URN urn:nbn:de:gbv:830-tubdok-12592 Danksagung Diese Arbeit entstand im Rahmen meiner Tätigkeit als wissenschaftliche Mitarbeiterin am Institut für Thermische Verfahrenstechnik an der TU Hamburg-Harburg. Diese Zeit wird mir immer in guter Erinnerung bleiben. Deshalb möchte ich ganz besonders Frau Professor Dr. Irina Smirnova für die unermüdliche Unterstützung danken. Vielen Dank für das entgegengebrachte Vertrauen, die stets offene Tür, die gute Atmosphäre und die angenehme Zusammenarbeit in Erlangen und in Hamburg. Frau Professor Dr. Gabriele Sadowski danke ich für das Interesse an der Arbeit und die Begutachtung der Dissertation, Herrn Professor Horn für die freundliche Übernahme des Prüfungsvorsitzes. Weiterhin geht mein Dank an das Nestlé Research Center, Lausanne, im Besonderen an Herrn Dr. Ulrich Bobe für die ausgezeichnete Zusammenarbeit und der Bereitstellung von LPC. Den Studenten, die im Rahmen ihrer Abschlussarbeit einen wertvollen Beitrag zu dieser Arbeit geleistet haben, möchte ich herzlichst danken. Für den außergewöhnlichen Einsatz und die angenehme Zusammenarbeit bedanke ich mich besonders bei Linda Kloß, Annette Zewuhn, Dierk Claus, Pierre Bräuer, Heike Mushardt, Zaineb Doggaz und Vanya Omaynikova. Für die freundliche Arbeitsatmosphäre, erfrischenden Kaffeepausen und hilfreichen Gespräche am Institut danke ich meinen Kollegen Carlos, Carsten, Christian, Mohammad, Krishan, Pavel, Raman, René und Sucre. -
Estimation of Distribution Coefficients from the Partition Coefficient and Pka Douglas C
Estimation of Distribution Coefficients from the Partition Coefficient and pKa Douglas C. Scott* and Jeffrey W. Clymer he use of partition coefficients has received much atten- tion in the assessment of relative lipophilicity and hy- drophilicity of a compound. Recent advances in com- putational chemistry have enabled scientists to estimate Tpartition coefficients for neutral species very easily. For ioniz- able species, the distribution coefficient is a more relevant pa- rameter; however, less effort has been applied to its assessment. Knowledge of the distribution coefficient and pKa is important The authors discuss for the basic characterization of a compound (1), particularly the relationship when assessing the compound’s potential to penetrate biolog- between the partition ical or lipid barriers (2). In addition, the majority of compounds coefficient and the are passively absorbed and a large number of new chemical en- distribution coefficient tities fail in the development stages because of related phar- and relate the two with the use of equations. macokinetic reasons (3). Assessing a compound’s relative lipophilicity dictates a formulation strategy that will ensure ab- To accurately explain this relationship, the sorption or tissue penetration, which ultimately will lead to de- authors consider the partitioning of both the livery of the drug to the site of action. In recognition of the ionized and un-ionized species.The presence value of knowing the extent of a drug’s gastrointestinal per- of both species in the oil phase necessitates a meation along with other necessary parameters, FDA has is- dissociative equilibrium among these species sued guidance for a waiver of in vivo bioavailability and bio- such as that in the water phase. -
Solvation Structure of Ions in Water
International Journal of Thermophysics, Vol. 28, No. 2, April 2007 (© 2007) DOI: 10.1007/s10765-007-0154-6 Solvation Structure of Ions in Water Raymond D. Mountain1 Molecular dynamics simulations of ions in water are reported for solutions of varying solute concentration at ambient conditions for six cations and four anions in 10 solutes. The solutes were selected to show trends in properties as the size and charge density of the ions change. The emphasis is on how the structure of water is modified by the presence of the ions and how many water molecules are present in the first solvation shell of the ions. KEY WORDS: anion; cation; molecular dynamics; potential functions; solva- tion; water. 1. INTRODUCTION The behavior of aqueous solutions of salts is a topic of continuing interest [1–3]. In this note we examine how the structure of water,as reflected in the oxy- gen–oxygen pair function, is modified as the concentration of ions increases. The method of generating the pair functions is molecular dynamics using the SPC/E model for water [4] and various models for ion–water interactions taken from the literature. The solutes are LiCl, NaCl, KCl, RbCl, NaF, CaCl2, CaSO4,Na2SO4, NaNO3, and guanidinium chloride (GdmCl) [C(NH2)3Cl]. This work is an extension of earlier work [5] to a larger set of ions. The water molecules and ions interact through site–site pair interac- tions consisting of Lennard–Jones potentials and Coulomb interactions so that the interaction between a pair of sites labeled i, j and separated by an interatomic distance r is 12 6 φij (r) = 4ij (σij /r) − (σij /r) + qiqj /r (1) where qi is the charge on site i. -
Affinity of Small-Molecule Solutes to Hydrophobic, Hydrophilic, and Chemically Patterned Interfaces in Aqueous Solution
Affinity of small-molecule solutes to hydrophobic, hydrophilic, and chemically patterned interfaces in aqueous solution Jacob I. Monroea, Sally Jiaoa, R. Justin Davisb, Dennis Robinson Browna, Lynn E. Katzb, and M. Scott Shella,1 aDepartment of Chemical Engineering, University of California, Santa Barbara, CA 93106; and bDepartment of Civil, Architectural and Environmental Engineering, University of Texas at Austin, Austin, TX 78712 Edited by Peter J. Rossky, Rice University, Houston, TX, and approved November 17, 2020 (received for review September 30, 2020) Performance of membranes for water purification is highly influ- However, a molecular understanding that links membrane enced by the interactions of solvated species with membrane surface chemistry to solute affinity and hence membrane func- surfaces, including surface adsorption of solutes upon fouling. tional properties remains incomplete, due in part to the complex Current efforts toward fouling-resistant membranes often pursue interplay among specific interactions (e.g., hydrogen bonds, surface hydrophilization, frequently motivated by macroscopic electrostatics, dispersion) and molecular morphology (e.g., sur- measures of hydrophilicity, because hydrophobicity is thought to face and polymer configurations) that are difficult to disentangle increase solute–surface affinity. While this heuristic has driven di- (11–14). Chemically heterogeneous surfaces are even less un- verse membrane functionalization strategies, here we build on derstood but can affect fouling in complex ways. -
1 Supplementary Material to the Paper “The Temperature and Pressure Dependence of Nickel Partitioning Between Olivine and Sili
SUPPLEMENTARY MATERIAL TO THE PAPER “THE TEMPERATURE AND PRESSURE DEPENDENCE OF NICKEL PARTITIONING BETWEEN OLIVINE AND SILICATE MELT” A. K. Matzen, M. B. Baker, J. R. Beckett, and E. M. Stolper. In this Supplement, we provide seven sections that expand and/or illustrate specific topics presented in the main text. The first section is a sample calculation using our preferred partitioning expression, equation (5), from the main text. Section 2 compares our fitted values of ∆ r HT ,P ∆ r ST ,P − ref ref and ref ref for equation (5) to those calculated using tabulated thermodynamic R R data. In Section 3, we present details of the mass-balance calculations used to evaluate the experiments from both this work and the literature, and in Section 4 we describe in detail the construction of the Filter-B dataset. Section 5 details the construction and fits of the regular solution partitioning models. Section 6 is a comparison of the results of this work and the Beattie-Jones family of models. Finally, Section 7 lists all of the references incorporated into our database on olivine-liquid Ni partitioning. 1. EXAMPLE CALCULATION USING OUR PREFERRED PARTITIONING EXPRESSION (EQUATION 5) FROM THE MAIN TEXT Although one of the simplest equations listed in the text, we think it useful to present a detailed accounting of how to use equation (5) along with the fitted parameters presented in Table 4 to ol /liq ol /liq ol liq predict DNi (where DNi = NiO /NiO , by wt.) given the temperature and compositions of the coexisting olivine and liquid. In our example calculation, we predict the partition coefficient for one of our 1.0 GPa experiments, Run 6. -
The Cloud Point Composition and Flory-Huggins Interaction Parameters of Polyethylene Glycol and Sodium Lignin Sulfonate in Water - Ethanol Mixture
AN ABSTRACT OF THE THESIS OF Luh, Song - Ping for the degree of Master of Science in Chemical Engineering presented on July 22, 1987 Title: The Cloud Point Composition and Flory - Huggins Interaction Parameters of Polyethylene Glycol and Sodium Lignin Sulfonate in Water - Ethanol Mixtures Redacted for Privacy Abstract Approved: Willi J. Frederick/Jr. In designing a solubility based separation process for solvent recovery of an organosolv pulping process, the phase behavior of polymeric lignin molecules in alcohol - water mixed solvent should be known. In this study, sodium lignin sulfonates (NaLS) samples were fractionated into three different molecular weight fractions using a partial dissolution method. The cloud point compositions of each of the three fractions were determined by a cloud point titration method. The experimental data were correlated using the three component Flory - Huggins equation of the Gibbs free energy change of mixing. The binary interaction parameter between water and that between ethanol and NaLSwere found to be a weak function of the NaLS volume fraction, while that between water and ethanol was strongly depend on the solvent composition. The Cloud Point Composition and Flory - Huggins Interaction Parameters of Polyethylene Glycol and Sodium Lignin Sulfonate in Water - Ethanol Mixtures by Luh, Song - Ping A THESIS submitted to Oregon State University in partial fulfillment of the requirements for the degree of Master of Science Completed July 22, 1987 Commencement June 1988 APPROVED: Redacted for Privacy Associate P fessor of Chemi401 Engineering in charge of major Redacted for Privacy Head of Department of dlemical Engineering Redacted for Privacy Dean of Gradu School (I Date thesis is presented July 22, 1987 Typed by Luh, Song - Ping for Luh, Song - Ping TABLE OF CONTENTS Page INTRODUCTION 1 LITERATURE REVIEW 3 1. -
Role of Solvation in Drug Design As Revealed by the Statistical Mechanics Integral Equation Theory of Liquids Norio Yoshida*
Review Cite This: J. Chem. Inf. Model. 2017, 57, 2646-2656 pubs.acs.org/jcim Role of Solvation in Drug Design as Revealed by the Statistical Mechanics Integral Equation Theory of Liquids Norio Yoshida* Department of Chemistry, Graduate School of Science, Kyushu University, 744 Motooka, Nishi-ku, Fukuoka 819-0395 Japan ABSTRACT: Recent developments and applications in theoretical methods focusing on drug design and particularly on the solvent effect in molecular recognition based on the three-dimensional reference interaction site model (3D-RISM) theory are reviewed. Molecular recognition, a fundamental molecular process in living systems, is known to be the functional mechanism of most drugs. Solvents play an essential role in molecular recognition processes as well as in ligand−protein interactions. The 3D-RISM theory is derived from the fundamental statistical mechanics theory, which reproduces all solvation thermodynamics naturally and has some advantages over conventional solvation methods, such as molecular simulation and the continuum model. Here, we review the basics of the 3D-RISM theory and methods of molecular recognition in its applications toward drug design. KEYWORDS: Drug design, Molecular recognition, Solvation, 3D-RISM ■ INTRODUCTION ΔGG=Δconf +Δ G int +Δ G solv (2) Molecular recognition is one of the most important where ΔGconf, ΔGint, and ΔGsolv denote the changes in the fundamental processes in biological systems and is known to 1 conformational energy, the interaction energy between ligand be the functional mechanism of most drugs. This is defined as a molecular process in which a ligand molecule is bound at a and protein, and the solvation free energy, respectively. -
Calculating the Partition Coefficients of Organic Solvents in Octanol/Water and Octanol/Air
Article Cite This: J. Chem. Inf. Model. XXXX, XXX, XXX−XXX pubs.acs.org/jcim Calculating the Partition Coefficients of Organic Solvents in Octanol/ Water and Octanol/Air † ‡ § ∥ Miroslava A. Nedyalkova,*, Sergio Madurga, Marek Tobiszewski, and Vasil Simeonov † Inorganic Chemistry Department, Faculty of Chemistry and Pharmacy, University of Sofia, Sofia 1164, Bulgaria ‡ Departament de Ciencià de Materials i Química Física and Institut de Química Teoricà i Computacional (IQTCUB), Universitat de Barcelona, 08028 Barcelona, Catalonia, Spain § Department of Analytical Chemistry, Faculty of Chemistry, Gdansḱ University of Technology (GUT), 80-233 Gdansk,́ Poland ∥ Analytical Chemistry Department, Faculty of Chemistry and Pharmacy, University of Sofia, Sofia 1164, Bulgaria *S Supporting Information ABSTRACT: Partition coefficients define how a solute is distributed between two immiscible phases at equilibrium. The experimental estimation of partition coefficients in a complex system can be an expensive, difficult, and time-consuming process. Here a computa- tional strategy to predict the distributions of a set of solutes in two relevant phase equilibria is presented. The octanol/water and octanol/air partition coefficients are predicted for a group of polar solvents using density functional theory (DFT) calculations in combination with a solvation model based on density (SMD) and are in excellent agreement with experimental data. Thus, the use of quantum-chemical calculations to predict partition coefficients from free energies should be a valuable alternative for unknown solvents. The obtained results indicate that the SMD continuum model in conjunction with any of the three DFT functionals (B3LYP, M06-2X, and M11) agrees with the observed experimental values. The highest correlation to experimental data for the octanol/water partition coefficients was reached by the M11 functional; for the octanol/air partition coefficient, the M06-2X functional yielded the best performance. -
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.