Thermodynamic Modelling of Surfactant Solutions
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Hydrophilic Surface-Treating Aqueous Solution and Hydrophilic Surface
Europaisches Patentamt (19) European Patent Office Office europeenpeen des brevets EP 0 654 514 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) intci.6: C09D 201/00, C09D 177/04, of the grant of the patent: C09D 5/08, C23C 22/68, 09.12.1998 Bulletin 1998/50 C23C 22/66 (21) Application number: 94307102.7 (22) Date of filing: 28.09.1994 (54) Hydrophilic surface-treating aqueous solution and hydrophilic surface-treating method Hydrophile wassrige Oberflachenbehandlungslosung und hydrophiles Oberflachenbehandlungsverfahren Solution aqueuse hydrophile de traitement de surface, et methode de traitement de surface (84) Designated Contracting States: • Hirasawa, Hidekimi DE FR GB Yokohama-shi, Kanagawa (JP) • Yamasoe, Katsuyoshi (30) Priority: 06.10.1993 JP 250314/93 Yotsukaido-shi, Chiba (JP) (43) Date of publication of application: (74) Representative: Stuart, Ian Alexander et al 24.05.1995 Bulletin 1995/21 MEWBURN ELLIS York House (73) Proprietor: Nippon Paint Co., Ltd. 23 Kingsway Kita-ku, Osaka-shi, Osaka 531 (JP) London WC2B 6HP (GB) (72) Inventors: (56) References cited: • Matsukawa, Masahiko EP-A- 0 413 260 US-A-4 828 616 Kawasaki-shi, Kanagawa (JP) US-A- 4 908 075 US-A- 4 973 359 • Mikami, Fujio Yokohama-shi, Kanagawa (JP) DO ^> lo ^- LO CO Note: Within nine months from the publication of the mention of the grant of the European patent, any person may give notice the Patent Office of the Notice of shall be filed in o to European opposition to European patent granted. opposition a written reasoned statement. It shall not be deemed to have been filed until the opposition fee has been paid. -
(CCC)95-Hydrophile-Lipophile Balance (HLB) Relationship
Minerals 2012, 2, 208-227; doi:10.3390/min2030208 OPEN ACCESS minerals ISSN 2075-163X www.mdpi.com/journal/minerals Article Characterizing Frothers through Critical Coalescence Concentration (CCC)95-Hydrophile-Lipophile Balance (HLB) Relationship Wei Zhang 1, Jan E. Nesset 2, Ramachandra Rao 1 and James A. Finch 1,* 1 Department of Mining and Materials Engineering, McGill University, 3610 Univeristy Street, Wong Building, Montreal, QC H3A 2B2, Canada; E-Mails: [email protected] (W.Z.); [email protected] (R.R.) 2 NesseTech Consulting Services Inc., 17-35 Sculler’s Way, St., Catharines, ON L2N 7S9, Canada; E-Mail: [email protected] * Author to whom correspondence should be addressed; E-Mail: [email protected]; Tel.: +01-514-398-1452; Fax: +01-514-398-4492. Received: 22 June 2012; in revised form: 26 July 2012 / Accepted: 31 July 2012 / Published: 13 August 2012 Abstract: Frothers are surfactants commonly used to reduce bubble size in mineral flotation. This paper describes a methodology to characterize frothers by relating impact on bubble size reduction represented by CCC (critical coalescence concentration) to frother structure represented by HLB (hydrophile-lipophile balance). Thirty-six surfactants were tested from three frother families: Aliphatic Alcohols, Polypropylene Glycol Alkyl Ethers and Polypropylene Glycols, covering a range in alkyl groups (represented by n, the number of carbon atoms) and number of Propylene Oxide groups (represented by m). The Sauter 3 mean size (D32) was derived from bubble size distribution measured in a 0.8 m mechanical flotation cell. The D32 vs. concentration data were fitted to a 3-parameter model to determine CCC95, the concentration giving 95% reduction in bubble size compared to water only. -
Selection of Thermodynamic Methods
P & I Design Ltd Process Instrumentation Consultancy & Design 2 Reed Street, Gladstone Industrial Estate, Thornaby, TS17 7AF, United Kingdom. Tel. +44 (0) 1642 617444 Fax. +44 (0) 1642 616447 Web Site: www.pidesign.co.uk PROCESS MODELLING SELECTION OF THERMODYNAMIC METHODS by John E. Edwards [email protected] MNL031B 10/08 PAGE 1 OF 38 Process Modelling Selection of Thermodynamic Methods Contents 1.0 Introduction 2.0 Thermodynamic Fundamentals 2.1 Thermodynamic Energies 2.2 Gibbs Phase Rule 2.3 Enthalpy 2.4 Thermodynamics of Real Processes 3.0 System Phases 3.1 Single Phase Gas 3.2 Liquid Phase 3.3 Vapour liquid equilibrium 4.0 Chemical Reactions 4.1 Reaction Chemistry 4.2 Reaction Chemistry Applied 5.0 Summary Appendices I Enthalpy Calculations in CHEMCAD II Thermodynamic Model Synopsis – Vapor Liquid Equilibrium III Thermodynamic Model Selection – Application Tables IV K Model – Henry’s Law Review V Inert Gases and Infinitely Dilute Solutions VI Post Combustion Carbon Capture Thermodynamics VII Thermodynamic Guidance Note VIII Prediction of Physical Properties Figures 1 Ideal Solution Txy Diagram 2 Enthalpy Isobar 3 Thermodynamic Phases 4 van der Waals Equation of State 5 Relative Volatility in VLE Diagram 6 Azeotrope γ Value in VLE Diagram 7 VLE Diagram and Convergence Effects 8 CHEMCAD K and H Values Wizard 9 Thermodynamic Model Decision Tree 10 K Value and Enthalpy Models Selection Basis PAGE 2 OF 38 MNL 031B Issued November 2008, Prepared by J.E.Edwards of P & I Design Ltd, Teesside, UK www.pidesign.co.uk Process Modelling Selection of Thermodynamic Methods References 1. -
Evaluation of UNIFAC Group Interaction Parameters Usijng Properties Based on Quantum Mechanical Calculations Hansan Kim New Jersey Institute of Technology
New Jersey Institute of Technology Digital Commons @ NJIT Theses Theses and Dissertations Spring 2005 Evaluation of UNIFAC group interaction parameters usijng properties based on quantum mechanical calculations Hansan Kim New Jersey Institute of Technology Follow this and additional works at: https://digitalcommons.njit.edu/theses Part of the Chemical Engineering Commons Recommended Citation Kim, Hansan, "Evaluation of UNIFAC group interaction parameters usijng properties based on quantum mechanical calculations" (2005). Theses. 479. https://digitalcommons.njit.edu/theses/479 This Thesis is brought to you for free and open access by the Theses and Dissertations at Digital Commons @ NJIT. It has been accepted for inclusion in Theses by an authorized administrator of Digital Commons @ NJIT. For more information, please contact [email protected]. Copyright Warning & Restrictions The copyright law of the United States (Title 17, United States Code) governs the making of photocopies or other reproductions of copyrighted material. Under certain conditions specified in the law, libraries and archives are authorized to furnish a photocopy or other reproduction. One of these specified conditions is that the photocopy or reproduction is not to be “used for any purpose other than private study, scholarship, or research.” If a, user makes a request for, or later uses, a photocopy or reproduction for purposes in excess of “fair use” that user may be liable for copyright infringement, This institution reserves the right to refuse to accept a copying -
Physicochemical Properties and the Gelation Process of Supramolecular Hydrogels: a Review
gels Review Physicochemical Properties and the Gelation Process of Supramolecular Hydrogels: A Review Abdalla H. Karoyo and Lee D. Wilson * Department of Chemistry, University of Saskatchewan, 110 Science Place, Saskatoon, SK S7N 5C9, Canada; [email protected] * Correspondence: [email protected]; Tel.: +1-306-966-2961 Academic Editor: Clemens K. Weiss Received: 10 November 2016; Accepted: 2 December 2016; Published: 1 January 2017 Abstract: Supramolecular polysaccharide-based hydrogels have attracted considerable research interest recently due to their high structural functionality, low toxicity, and potential applications in foods, cosmetics, catalysis, drug delivery, tissue engineering and the environment. Modulation of the stability of hydrogels is of paramount importance, especially in the case of stimuli-responsive systems. This review will update the recent progress related to the rational design of supramolecular hydrogels with the objective of understanding the gelation process and improving their physical gelation properties for tailored applications. Emphasis will be given to supramolecular host–guest systems with reference to conventional gels in describing general aspects of gel formation. A brief account of the structural characterization of various supramolecular hydrogels is also provided in order to gain a better understanding of the design of such materials relevant to the nature of the intermolecular interactions, thermodynamic properties of the gelation process, and the critical concentration values of the precursors and the solvent components. This mini-review contributes to greater knowledge of the rational design of supramolecular hydrogels with tailored applications in diverse fields ranging from the environment to biomedicine. Keywords: gel; sol; aggregation; cyclodextrin; hydration 1. Introduction Polymer gels are generally defined as 3D networks swollen by a large amount of water [1]. -
T8532 Storage Temperature 25°C
TRITON X-100 Product Number X-100, T9284, T8787, T8532 Storage Temperature 25°C CAS #: 9002-93-1 reported in numerous references. It does absorb in the Synonyms: X-100; TRITON X-1001; Octylphenol ultraviolet region of the spectrum, so it can interfere 1 ethylene oxide condensate with protein quantitation by absorption at A280nm. A number of polymeric resins have been used to remove Product Description X-100 from solution, including Amberlite hydrophobic XAD resins6 and Rezorian A161 cartridges.3 The "Triton X" series of detergents are produced from CH3 CH3 octylphenol polymerized with ethylene oxide. The number ("-100") relates only indirectly to the number of H3C C CH2 C (OCH2CH2)xOH ethylene oxide units in the structure. X-100 has an CH CH "average of 9.5" ethylene oxide units per molecule, with 3 3 an average molecular weight of 625.1,3 In addition, lower and higher mole adducts will be present in lesser amounts, varying slightly within supplier's standard manufacturing conditions. A by-product formed during x = 9-10 the reaction is polyethylene glycol, a homopolymer of Appearance: Liquid, clear to slightly hazy, colorless to ethylene oxide. Acid is also added to the product to light yellow neutralize the product after the base catalyzed reaction Specific gravity: 1.065 at 25°C (approx. 1.07 g/mL)1 is completed. No antioxidants are added by Sigma or Approximate Molecular Weight: 6251; the manufacturer, but commercial preparations of Triton 1 X-100 have been found to contain peroxides up to effective molarity =1.7 M for the neat liquid. -
European Patent Specification
(19) TZZ ¥_T (11) EP 2 629 763 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int Cl.: of the grant of the patent: A61K 9/00 (2006.01) A61Q 17/04 (2006.01) 06.12.2017 Bulletin 2017/49 A61K 8/49 (2006.01) A61K 31/353 (2006.01) (21) Application number: 11788238.1 (86) International application number: PCT/US2011/001802 (22) Date of filing: 24.10.2011 (87) International publication number: WO 2012/054090 (26.04.2012 Gazette 2012/17) (54) METHODS OF INCREASING SOLUBILITY OF POORLY SOLUBLE COMPOUNDS AND METHODS OF MAKING AND USING FORMULATIONS OF SUCH COMPOUNDS VERFAHREN ZUR ERHÖHUNG DER LÖSLICHKEIT VON SCHWER LÖSLICHEN VERBINDUNGEN UND VERFAHREN ZUR HERSTELLUNG VON FORMULIERUNGEN DERARTIGER VERBINDUNGEN PROCÉDÉS VISANT À ACCROÎTRE LA SOLUBILITÉ DE COMPOSÉS FAIBLEMENT SOLUBLES, ET PROCÉDÉS DE FABRICATION ET D’UTILISATION DE FORMULATIONS DE TELS COMPOSÉS (84) Designated Contracting States: (74) Representative: Stafford, Jonathan Alan Lewis et AL AT BE BG CH CY CZ DE DK EE ES FI FR GB al GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO Marks & Clerk LLP PL PT RO RS SE SI SK SM TR 1 New York Street Manchester M1 4HD (GB) (30) Priority: 22.10.2010 PCT/US2010/002821 22.04.2011 US 201113064882 (56) References cited: EP-A1- 1 600 143 EP-A1- 1 731 134 (43) Date of publication of application: WO-A2-2007/006497 WO-A2-2010/007252 28.08.2013 Bulletin 2013/35 DE-A1- 10 129 973 DE-A1- 10 260 872 US-A- 4 603 046 (60) Divisional application: 17199056.7 • RODRIGUEZ-TENREIRO ET AL: "Estradiol sustained release from high affinity cyclodextrin (73) Proprietor: Vizuri Health Sciences LLC hydrogels", EUROPEAN JOURNAL OF Fairfax, VA 22033 (US) PHARMACEUTICS AND BIOPHARMACEUTICS, ELSEVIER SCIENCE PUBLISHERS B.V., (72) Inventor: BIRBARA, Philip, J. -
Studies on Surfactants, Cosurfactants, and Oils for Prospective Use in Formulation of Ketorolac Tromethamine Ophthalmic Nanoemulsions
pharmaceutics Article Studies on Surfactants, Cosurfactants, and Oils for Prospective Use in Formulation of Ketorolac Tromethamine Ophthalmic Nanoemulsions Shahla S. Smail 1,2,* , Mowafaq M. Ghareeb 3, Huner K. Omer 2 , Ali A. Al-Kinani 1,* and Raid G. Alany 1,4 1 Drug Discovery, Delivery and Patient Care (DDDPC) Theme, Department of Pharmacy, Kingston University, Kingston upon Thames, London KT1 2EE, UK; [email protected] 2 Department of Pharmaceutics, College of Pharmacy, Hawler Medical University, Kurdistan Region, Erbil 44001, Iraq; [email protected] 3 Department of Pharmaceutics, College of Pharmacy, University of Baghdad, Baghdad 10011, Iraq; [email protected] 4 School of Pharmacy, The University of Auckland, Auckland 1023, New Zealand * Correspondence: [email protected] (S.S.S.); [email protected] (A.A.A.-K.) Abstract: Nanoemulsions (NE) are isotropic, dispersions of oil, water, surfactant(s) and cosurfac- tant(s). A range of components (11 surfactants, nine cosurfactants, and five oils) were investigated as potential excipients for preparation of ketorolac tromethamine (KT) ocular nanoemulsion. Diol cosur- factants were investigated for the effect of their carbon chain length and dielectric constant (DEC), Log P, and HLB on saturation solubility of KT. Hen’s Egg Test—ChorioAllantoic Membrane (HET-CAM) assay was used to evaluate conjunctival irritation of selected excipients. Of the investigated surfac- Citation: Smail, S.S.; Ghareeb, M.M.; Omer, H.K.; Al-Kinani, A.A.; Alany, tants, Tween 60 achieved the highest KT solubility (9.89 ± 0.17 mg/mL), followed by Cremophor RH R.G. Studies on Surfactants, 40 (9.00 ± 0.21 mg/mL); amongst cosurfactants of interest ethylene glycol yielded the highest KT Cosurfactants, and Oils for solubility (36.84 ± 0.40 mg/mL), followed by propylene glycol (26.23 ± 0.82 mg/mL). -
PATENT OFFICE 2,159,312 PROCESS for BREAKING OL-N-WATER, TYPE PETROLEUM EMULSIONS Carles M
Patented May 23, 1939 2,159,312 UNITED STATES PATENT OFFICE 2,159,312 PROCESS FOR BREAKING OL-N-WATER, TYPE PETROLEUM EMULSIONS Carles M. Blair, Jr., Webster Groves, Mo., assign or to fhe Tret-O-Lite Company, Webster Groves, Mc., a corporation of Missouri No orawing. Application December 13, 1937, Serial No. 179,471 1. Claims. (CI. 196-4) This invention relates to the treatment of a tive colioid or equivalent thereof. To this extent, certain peculiar kind of naturally occurring crude although not necessarily due to this factor alone, oil emulsion and has for its main object to provide these particular or peculiar oil field emulsions, a practicable process for separating the water ianiely, the naturally occurring oil-in-water ... and oil contained in said peculiar emulsion. emulsions having a significant proportion of dis 5 The vast majority of petroleum emulsions are of persed phase and a substantially complete absence the Water-in-oil type and comprise fine droplets Of a protective colloid or equivalent substance of naturally occurring waters or brines dispersed appear to be substantially a new type of emulsion in a more or less permanent state throughout the that requires a new method of treatment, in 10. oil, which constitutes the continuous phase of the order to separate them economically and rapidly O emulsion. They are obtained from producing into their component parts, and thus permit the wells and from the botton of oil storage tanks, recovery of dry or merchantable oil, and are commonly referred to as "cut oil', 'roily It is to be emphasized that the external phase oil', 'emulsified oil', and 'bottom settlings'. -
Prediction of Solubility of Amino Acids Based on Cosmo Calculaition
PREDICTION OF SOLUBILITY OF AMINO ACIDS BASED ON COSMO CALCULAITION by Kaiyu Li A dissertation submitted to Johns Hopkins University in conformity with the requirement for the degree of Master of Science in Engineering Baltimore, Maryland October 2019 Abstract In order to maximize the concentration of amino acids in the culture, we need to obtain solubility of amino acid as a function of concentration of other components in the solution. This function can be obtained by calculating the activity coefficient along with solubility model. The activity coefficient of the amino acid can be calculated by UNIFAC. Due to the wide range of applications of UNIFAC, the prediction of the activity coefficient of amino acids is not very accurate. So we want to fit the parameters specific to amino acids based on the UNIFAC framework and existing solubility data. Due to the lack of solubility of amino acids in the multi-system, some interaction parameters are not available. COSMO is a widely used way to describe pairwise interactions in the solutions in the chemical industry. After suitable assumptions COSMO can calculate the pairwise interactions in the solutions, and largely reduce the complexion of quantum chemical calculation. In this paper, a method combining quantum chemistry and COSMO calculation is designed to accurately predict the solubility of amino acids in multi-component solutions in the ii absence of parameters, as a supplement to experimental data. Primary Reader and Advisor: Marc D. Donohue Secondary Reader: Gregory Aranovich iii Contents -
The Molecular Basis of Surface Activity
The Molecular Basis of Surface Activity Dong-Myung Shin Hongik University Department of Chemical Engineering Molecular Basis – Basic Structure for Sur. Act. Stories about surfactants (surface active agents) DM Shin : Hongik University Molecular Basis – Basic Structure for Sur. Act. • BASIC STRUCTURAL REQUIREMENTS FOR SURFACE ACTIVITY • Lyophobic Group - Little attraction to the solvent (Hydrophobic - water repellent) • Lyophilic Group - Strong attraction to the solvent (Hydrophilic- fond of water) • Amphiphilic (“liking both”) - some affinity for two essentially immiscible phases • Lyophobic group and solvent interaction unfavorable distortion of solvent structure Increase in energy (due to entropy) preferential adsorption at interface or undergo low energy system (eg. Micelle formation) DM Shin : Hongik University Molecular Basis – Preferrential Orientation Preferrential Orientation Orientation of Surfactant Molecules Orientation away from the bulk solvent phase change in physical properties DM Shin : Hongik University Molecular Basis – Solubility Solubility Hydrophobic group - Hydrophilic group balance 물을 예를 들면 Hydrophobic: Hydrocarbon, fluorocarbon, siloxane chain을사용할수 있고 Hydrophilic: ionic and polar group 이 용해를 시키는데 유용하다. Hydrocarbon 용매의 경우에는 반대로 생각하면 된다. 온도, 압력, surfactant 주변의 조건이 바뀌면 용해도 및 interfacial properties가변하게된다. DM Shin : Hongik University Molecular Basis – Surfactant Struc. & Sources SURFACTANT STRUCTURES AND SOURCES Building Surfactant Molecules Functional group Modification Alcohol dodecane [CH3(CH2) 10CH3], insoluble in -
Modeling of Activity Coefficients Using Computational
Modelling of activity coefficents by comp. chem. 1 Modelling of activity coefficients using computational chemistry Eirik Falck da Silva Report in DIK 2099 Faselikevekter June 2002 Modelling of activity coefficents by comp. chem. 2 SUMMARY ......................................................................................................3 INTRODUCTION .............................................................................................3 background .............................................................................................................................................3 The use of computational chemistry .....................................................................................................4 REVIEW...........................................................................................................4 Introduction ............................................................................................................................................4 Free energy of solvation .........................................................................................................................5 Cosmo-RS ............................................................................................................................................7 SMx models..........................................................................................................................................7 Application of infinite dilution solvation energy..................................................................................8