ALCOHOL ETHOXYLATES Versatile Alternatives for Technical Applications
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
Enhancing the Efficacy of Antimicrobial Peptide BM2, Against Mono-Species Biofilms, with Detergents
Enhancing the efficacy of Antimicrobial peptide BM2, against mono-species biofilms, by combining with detergents A thesis submitted for the degree of Doctor of Clinical Dentistry (Endodontics) Arpana Arthi Devi Department of Oral Rehabilitation, School of Dentistry, University of Otago, Dunedin, New Zealand 2016 Abstract Title Enhancing the efficacy of antimicrobial peptide BM2, against mono-species biofilms, by combining with detergents. Aim To investigate if a detergent regime could enhance the antimicrobial ability of BM2. Method Strains of Enterococcus faecalis, Streptococcus gordonii, Streptococcus mutans, and Candida albicans were grown from glycerol stocks after confirmation of the strains. After subculturing single colonies were cultured in TSB and CSM liquid media for 24hr to obtain a microbial suspension which was adjusted to OD600nm = 0.5. Dilution series of the peptidomimetic BM2 and detergents were prepared in aqueous solution and minimum inhibitory concentration (MIC) and minimum bactericidal concentration (MBC) were determined using a broth micro-dilution method. Further on planktonic cells and monospecies biofilms were exposed to the detergent and BM2 combinations. The efficacy of BM2 and detergents at causing biofilm detachment was measured using a crystal violet based assay. Results Planktonic cells were easier to kill with some of the detergents in isolation or in combination with BM2. SDS and CTAB in combination with BM2 increased the efficacy of BM2 against the test organisms. Tween 20 did not kill any of the test organisms alone or in combination. Biofilms were harder to eradicate and detergent, BM2 combinations gave varied results for the different species tested. Detergents in combination with BM2 did not increase the efficacy of the antimicrobial peptide in disrupting S. -
Ethoxylation Reactor Modelling and Design
Ethoxylation Reactor Modelling and Design by Yen-ni Chiu Bachelor of Engineering (Chemical) UNSW A thesis submitted in fulfillment of the requirements for the degree of Doctor of Philosophy Facaulty of Engineering and Industrial Sciences Swinburne University of Technology Melbourne, Australia To Mum, Dad, Jess and Ted Abstract The manufacture of nonionic surfactants generally involves ethoxylation via ethylene oxide condensation onto a hydrophobe substrate, mostly in the presence of an alkaline catalyst. Nonionic surfactants are used widely in industrial applications, such as detergents, health and personal care, coatings, and polymers. In Australia, approximately one-third of the annual consumption of nonionic surfactants is imported from offshore manufacturers; the market is highly competitive with the local manufacturer facing increasing competition from imports. Optimisation is a pressing need for the current manufacturing plant of the industrial partner for this research project, Huntsman Corporation Australia Pty Limited, the sole domestic manufacturer of nonionic surfactants in Australia. Therefore, the objectives of this research project were • to gain a better understanding of the various chemical and physical processes occurring simultaneously in an ethoxylation process; • to identify the process limitation in an existing production plant operated by Huntsman Corporation Australia, and • to explore measures for enhancing the asset productivity of the production plant. An ethoxylation process working model, describing the chemical kinetics and the physical transport processes involved, was developed to aid the exploration of optimisation opportunities, which would otherwise be empirical. Accordingly, this research project was structured into a two-stage program. The first stage determined the ethoxylation kinetics experimentally. The second stage investigated the interactions of physical transport processes numerically using a computational fluid dynamics (CFD) technique. -
United States Patent (19) 11 Patent Number: 6,013,801 Köll, Deceased Et Al
US00601 3801A United States Patent (19) 11 Patent Number: 6,013,801 Köll, deceased et al. (45) Date of Patent: Jan. 11, 2000 54 METHOD FOR PRODUCING 4,590,223 5/1986 Arai et al. ........................... 544/401 X AMINOETHYLETHANOLAMINE AND/OR 5,455,352 10/1995 Huellmann et al. .................... 544/401 HYDROXYETHYL PPERAZINE FOREIGN PATENT DOCUMENTS 75 Inventors: Juhan Köll, deceased, late of Stenungsund, by Mall Koll, legal 0 354993 2/1990 European Pat. Off. ...... CO7C 213/06 representative; Magnus Frank, 2013 676 1/1972 Germany ....................... CO7D 51/64 Göteborg, both of Sweden 27 16946 10/1978 Germany ....................... CO7C 89/02 206670 2/1984 Germany. 73 Assignee: Akzo Nobel N.V., Arnhem, Netherlands 1512967 10/1989 Russian Federation ........ CO7C 91/12 21 Appl. No.: 08/875,871 OTHER PUBLICATIONS 22 PCT Filed: Jan. 11, 1996 86 PCT No.: PCT/EP96/00207 Ludwig Knorr und Henry W. Brownadon: Ueber Alkohol basen aus Aethylendiamin und uber das Aethylenbismor S371 Date: Oct. 30, 1998 pholin, Dec. 11, 1902 pp. 4470–4473. S 102(e) Date: Oct. 30, 1998 87 PCT Pub. No.: WO96/24576 Primary Examiner Michael G. Ambrose PCT Pub. Date: Aug. 15, 1996 Attorney, Agent, or Firm-Ralph J. Mancini 30 Foreign Application Priority Data 57 ABSTRACT Feb. 8, 1995 (SE) Sweden .................................. 9500444 A method for preparing aminoethylethanolamine, and/or hydroxyethylpiperazine is described. Reaction of ethylene 51) Int. Cl." ........................ C07D 295/88; CO7C 213/04 oxide with ethylendiamine, piperazine, or a mixture of both 52 U.S. Cl. ............................................. 544/401; 564/503 produces these compounds. The process is integrated into a 58 Field of Search ............................. -
Fatty Acids: Fatty Acid Is a Carboxylic Acid Often with a Long Aliphatic Chain, Which Is Either Saturated Or Unsaturated
Introduction 1 Fatty Acids: Fatty acid is a carboxylic acid often with a long aliphatic chain, which is either saturated or unsaturated. Fatty acids and their derivatives are consumed in a wide variety because they are used as raw materials for a wide variety of industrial products like, paints, surfactant, textiles, plastics, rubber, cosmetics, foods and pharmaceuticals. Industrially, fatty acids are produced by the hydrolysis of triglycerides, with the removal of glycerol moiety. As mentioned before, fatty acids can be classified into two classes, the first is unsaturated fatty acid with one or more double bonds in the alkyl chain and the other is saturated fatty acid. Long chain 3-alkenoic acids are a family of polyunsaturated fatty acids which have in common a carbon–carbon double bond in the position 3. They are used as key precursors for synthesis of many organic compounds. There are many methods for the synthesis of such acids; here we will mention two of these methods. Nucleophilic substitution of allylic substrates with organometallic reagents, treatment of β-vinyl-β-propiolactone with butylmagnesium bromide in the presence of copper(I) iodide in THF at –30 o C, gave 3-nonenoic acid as a major product and 3-butyl-4-pentenoic acid with the ratio 98:2 respectively(1). Knoevenagel condensation of an aldehyde with malonic acid in the presence of organic bases was considerable value for the synthesis of unsaturated fatty acids. This reaction is mainly related to its application for the synthesis of α-β-unsaturated fatty acids. For the synthesis of β-γ-unsaturated fatty acids the Linstead modification (2) of the Knoevenagel condensation, in which triethanolamine or other tertiary amines are used. -
Predicting Distribution of Ethoxylation Homologues With
1 PREDICTING THE DISTRIBUTION OF ETHOXYLATION HOMOLOGUES WITH A PROCESS SIMULATOR Nathan Massey, Chemstations, Inc. Introduction Ethoxylates are generally obtained by additions of ethylene oxide (EO) to compounds containing dissociated protons. Substrates used for ethoxylation are primarily linear and branched C12-C18 alcohols, alkyl phenols, nonyl (propylene trimer) or decyl (propylene tetramer) groups, fatty acids and fatty acid derivatives. The addition of EO to a substrate containing acidic hydrogen is catalyzed by bases or Lewis acids. Amphoteric catalysts, as well as heterogeneous catalysts are also used. The degree of ethoxylation ( the moles of EO added per mole of substrate ) varies over wide ranges, in general between 3 and 40, and is chosen according to the intended use. As an illustration of how this distribution might be predicted using a process simulator, Chemcad was used to simulate the ethoxylation of Nonylphenols. Description of the Ethoxylation Chemistry The reaction mechanisms of base catalyzed and acid catalyzed ethoxylation differ, which affects the composition of the reaction products. In base catalyzed ethoxylation an alcoholate anion, formed initially by reaction with the catalyst ( alkali metal, alkali metal oxide, carbonate, hydroxide, or alkoxide ) nucleophilically attacks EO. The resulting union of the EO addition product can undergo an equilibrium reaction with the alcohol starting material or ethoxylated product, or can react further with EO: Figure 1 O RO- + H2CCH2 - - RO CH2CH2O O ROH H2CCH2 - - RO RO CH2CH2OH RO RO CH2CH2O 2 As Figure 1 illustrates, in alkaline catalyzed ethoxylations several reactions proceed in parallel. The addition of EO to an anion with the formation of an ether bond is irreversible. -
Linear Alpha-Olefins (681.5030)
IHS Chemical Chemical Economics Handbook Linear alpha-Olefins (681.5030) by Elvira O. Camara Greiner with Yoshio Inoguchi Sample Report from 2010 November 2010 ihs.com/chemical November 2010 LINEAR ALPHA-OLEFINS Olefins 681.5030 B Page 2 The information provided in this publication has been obtained from a variety of sources which SRI Consulting believes to be reliable. SRI Consulting makes no warranties as to the accuracy completeness or correctness of the information in this publication. Consequently SRI Consulting will not be liable for any technical inaccuracies typographical errors or omissions contained in this publication. This publication is provided without warranties of any kind either express or implied including but not limited to implied warranties of merchantability fitness for a particular purpose or non-infringement. IN NO EVENT WILL SRI CONSULTING BE LIABLE FOR ANY INCIDENTAL CONSEQUENTIAL OR INDIRECT DAMAGES (INCLUDING BUT NOT LIMITED TO DAMAGES FOR LOSS OF PROFITS BUSINESS INTERRUPTION OR THE LIKE) ARISING OUT OF THE USE OF THIS PUBLICATION EVEN IF IT WAS NOTIFIED ABOUT THE POSSIBILITY OF SUCH DAMAGES. BECAUSE SOME STATES DO NOT ALLOW THE EXCLUSION OR LIMITATION OF LIABILITY FOR CONSEQUENTIAL OR INCIDENTAL DAMAGES THE ABOVE LIMITATION MAY NOT APPLY TO YOU. IN SUCH STATES SRI CONSULTING’S LIABILITY IS LIMITED TO THE MAXIMUM EXTENT PERMITTED BY SUCH LAW. Certain statements in this publication are projections or other forward-looking statements. Any such statements contained herein are based upon SRI Consulting’s current knowledge and assumptions about future events including without limitation anticipated levels of global demand and supply expected costs trade patterns and general economic political and marketing conditions. -
Combined UV-Vis-Absorbance and Reflectance Spectroscopy Study of Dye Transfer Kinetics in Aqueous Mixtures of Surfactants
Noname manuscript No. (will be inserted by the editor) Combined UV-Vis-absorbance and Reflectance Spectroscopy Study of Dye Transfer Kinetics in Aqueous Mixtures of Surfactants Carlos G. Lopez · Anna Manova · Corinna Hoppe · Michael Dreja · Peter Schmiedel · Mareile Job · Walter Richtering · Alexander B¨oker · Larisa Tsarkova Received: date / Accepted: date Abstract We report an analytical approach to study the kinetics of desorp- tion and exhaustion of a hydrophobic dye in a multicomponent washing-model environment. The process of dye transfer between an acceptor textile (white polyamide), detergent micelles and a donor textile (red polyester) was quan- tified by a combination of colorimetric analyses. UV-Vis absorbance and UV- reflectance spectroscopy were used to follow the concentration of the solubilised dye in the micelles and the amount of dyer transferred to the acceptor textile, respectively, as a function of time. Up to ' 10 min of the washing process, the released dye is predominantly solubilised in surfactant micelles. At later times, the adsorption of the dye on the hydrophobic surface of the acceptor textile is energetically favoured. The shift of the desorption equilibrium in the presence of the acceptor textile results in ' 30% increase in the release of the dye. The reported methodology provides insight into the competition between solubili- sation of hydrophobic molecules by amphiphiles and dye adsorption on solid substrates, important for designing novel concepts of dye transfer inhibition. Carlos G. Lopez · Anna Manova · Corinna Hoppe · Walter Richtering Institute of Physical Chemistry, RWTH Aachen University, Landoltweg 2, 52056 Aachen, Germany Anna Manova DWI-Leibniz Institute for Interactive Materials, Forckenbeckstrasse 50, 52056 Aachen. -
Locating and Estimating Sources of Ethylene Oxide
United States Office of Air Quality EPA-450/4-84-007L Environmental Protection Planning And Standards Agency Research Triangle Park, NC 27711 September 1986 AIR EPA LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF ETHYLENE OXIDE L &E EPA- 450/4-84-007L September 1986 LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF ETHYLENE OXIDE U.S. Environmental Protection Agency Office of Air and Radiation Office of Air Quality Planning and Standards Research Triangle Park, North Carolina 27711 This report has been reviewed by the Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, and approved for publication as received from the contractor. Approval does not signify that the contents necessarily reflect the views and policies of the Agency, neither does mention of trade names or commercial products constitute endorsement or recommendation for use. EPA - 450/4-84-007L TABLE OF CONTENTS Section Page 1 Purpose of Document .......................................... 1 2 Overview of Document Contents ................................ 3 3 Background ................................................... 5 Nature of Pollutant .................................... 5 Overview of Production and Use ......................... 7 References for Section 3 .............................. 14 4 Emissions from Ethylene Oxide Production .................... 16 Ethylene Oxide Production ................................... 16 References for Section 4 .................................... 33 5 Emissions from Industries Which Use Ethylene -
Recent Developments in Ziegler-Natta Catalysts for Olefin Polymerization and Their Processes
Indian Journal of Technology Vol. 26, February 1988, pp. 53-82 Recent Developments in Ziegler-Natta Catalysts for Olefin Polymerization and Their Processes V CHANDRASEKHAR, P R SRINIVASAN & S SIVARAM* Research Centre, Indian Petrochemicals Corporation Ltd, P.O. Petrochemicals, Baroda 391346, India The chemistry of Ziegler-Natta catalysts in olefin polymerization is reviewed. Factors determining catalyst activity are identified for the current generation of high activity - high selectivity catalysts. These include the nature of transition metal, its oxidation states and the ligands around it, the nature of alkylaluminium compounds, the physical state ofthe catalyst and its dependence on the method of preparation as well as activation of support and the role ofinternal and external donors. The effect of reaction parameters on catalyst performance as well as effect of nature of catalysts on polymer properties such as molecular weight, molecular weight distribution and stereoregularity are discussed. Current developments in soluble titanium! zirconium, vanadium and magnesium-titanium catalysts are reviewed. Different classes of industrial processes for production of polyethylene and polypropylene, namely slurry phase, gas phase and solution processes are discussed, The nature of contemporary catalysts is exemplified by selected patents from current literature, The various reactor types for polyolefins and salient reactor design aspects are discussed, The dependence of polymer properties on reactor design 11:1 well as kinetic modelling and simulation of polyolefin processes are briefly reviewed. I. Introduction made the dramatic discovery that not only propylene Polyolefins are a group of bulk commodity polymers could be polymerized to high molecular weight pol comprising of polyethylenes, polypropylene, poly ymers by Ziegler catalysts but the polymer so pro (butene-I) and various copolymers ofethylene, propy duced had a highly stereo regular structure (termed lene and higher alpha olefins. -
Surfactant Book 2007
Surfactants: Strategic Personal Care Ingredients Anthony J. O’Lenick, Jr. ISBN 978-1-932633-96-2 Copyright 2014, by Anthony J. O'Lenick, Jr. This book is out of print. The copyright has reverted back to the author. It is being made available free of charge in electronic version. Please feel free to use it, download it or cite it in other publications. Allured Publishing Corporation 362 South Schmale Road, Carol Stream, IL 60188-2787 USA Tel: 630/653-2155 Fax: 630/653-2192 e-mail: [email protected] Table of Contents Preface................................................................................................................... vii About the Author ................................................................................................. viii Acknowledgments .................................................................................................. ix Chapter 1: Raw Materials for Surfactant Preparation Background ............................................................................................................. 1 Triglycerides............................................................................................................ 4 Methyl Esters ........................................................................................................ 20 Fatty Acids ............................................................................................................ 20 Natural Acids .................................................................................................... 20 Guerbet -
United States Patent (19) 11 Patent Number: 5,807,502 Wollenweber Et Al
USOO5807502A United States Patent (19) 11 Patent Number: 5,807,502 Wollenweber et al. (45) Date of Patent: Sep. 15, 1998 54 AQUEOUS FATTY ALCOHOL DISPERSIONS 4,396,524 8/1983 Hempel et al. ......................... 252/321 4,549,002 10/1985 Hoefer et al. ... - - - - - 526/209 4,600,523 7/1986 Priorr et al. ............................ 252/321 75 Inventors: Horst-Werner Wollenweber, Duesseldorf, Rainer Hoefer, Neuss; 4,976,888 12/1990 De Clercq et al. ..................... 252/358 Heinz-Guenther Schulte, Muehlheim, 5,147,412 9/1992 Klinksiek et al. .................... 23/293 R all of Germany 5,346,973 9/1994 Feustel et al. .......................... 526/209 FOREIGN PATENT DOCUMENTS 73 Assignee: Henkel Kommanditgesellschaft Auf Aktien, Duesseldorf, Germany 1297 755 3/1992 Canada. 230 977 8/1987 European Pat. Off.. 21 Appl. No.: 765,752 399 266 11/1990 European Pat. Off.. 11 90 927 4/1965 Germany. 22 PCT Filed: Jun. 12, 1995 29 OO O30 7/1980 Germany. 30 39 393 4/1981 Germany. 86 PCT No.: PCT/EP95/02260 30 O1 387 7/1981 Germany. 36 01929 7/1987 Germany. S371 Date: Dec. 20, 1996 40 06 391 9/1991 Germany. S 102(e) Date: Dec. 20, 1996 OTHER PUBLICATIONS 87 PCT Pub. No.: WO95/35143 Database WPI, Week 8323 London: Derwent Publications Ltd., AN-83–55096K, Class A97, JP58–072000 A (Daiichi PCT Pub. Date: Dec. 28, 1995 Kogyo Seiyaku), abstract. 30 Foreign Application Priority Data Primary Examiner Richard D. Lovering Jun. 20, 1994 DE Germany .......................... 44 21 270.4 ASSistant Examiner-Daniel S. Metzmaier (51) Int. Cl. ............................................... B01D 19/04 Attorney, Agent, or Firm-Ernest G. -
03 Chapter 2.Pdf (3.540Mb)
2. Literature Review 2.1 Flexible Polyurethane Foam Chemistry This section focuses on the basic chemical reactions involved in the formation of flexible polyurethane foams. Since flexible polyurethane foam production requires a variety of chemicals and additives, this section will review specific chemicals and their importance in the foaming process. 2.1.1 General Chemical Reactions Flexible polyurethane foam chemistry particularly features two reactions – the ‘blow’ reaction and the ‘gelation’ reaction. A delicate balance between the two reactions is required in order to achieve a foam with a stable open-celled structure and good physical properties. The commercial success of polyurethane foams can be partially attributed to catalysts which help to precisely control these two reaction schemes. An imbalance between the two reactions can lead to foam collapse, serious imperfections, and cells that open prematurely or not at all. 2.1.1.1 Blow Reaction The first step of the model blow reaction (Figure 2.1) involves the reaction of an isocyanate group with water to yield a thermally unstable carbamic acid which decomposes to give an amine functionality, carbon dioxide, and heat. In the second step (Figure 2.2), the newly O R N CO + HO H R N C O H Ca rbam i c A c id I s oc y a n a te Wat e r H R N H 2 + CO2 + HEA T Am i n e C a r bon Di oxide Figure 2.1 First Step of the Blow Reaction formed amine group reacts with another isocyanate group to give a disubstituted urea and additional heat is generated.