ABSTRACTS 2018 AOCS ANNUAL MEETING and EXPO May 6–9, 2018
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Tailored Microstructure of Colloidal Lipid Particles for Pickering Emulsions with Tunable Properties
Electronic Supplementary Material (ESI) for Soft Matter. This journal is © The Royal Society of Chemistry 2017 Supporting information. Tailored Microstructure of Colloidal Lipid Particles for Pickering Emulsions with Tunable Properties Anja A.J. Schröder1,2, Joris Sprakel2, Karin Schroën1, Claire C. Berton-Carabin1 1. Laboratory of Food Process Engineering, Wageningen University and Research, Bornse Weilanden 9, 6708 WG Wageningen, The Netherlands. 2. Physical Chemistry and Soft Matter, Wageningen University and Research, Stippeneng 4, 6708 WE Wageningen, The Netherlands. Email addresses: [email protected], [email protected], [email protected], [email protected] S1 S1. Tripalmitin CLP dispersions produced with 0.5% w/w (left) and 1% w/w (right) Tween40 in the aqueous phase. S2. Fatty acid composition of palm stearin. Component name Percentage average C14:0 1.16 C16:0 82.18 C18:0 5.12 C18:1 9.03 C18:2 1.83 C18:3 0.02 C20:0 0.32 C22:0 0.25 C22:1 0.04 C24:0 0.05 S3. Hydrodynamic diameter (z-average) measured by dynamic light scattering, and, D[4,3], D[3,2], D10, D50 and D90 measured by static light scattering of CLPs composed of (a) tripalmitin, (b) tripalmitin/tricaprylin 4:1, (c) palm stearin. S2 Type of z-average PdI D[4,3] A D[3,2] D10 D50 D90 lipid (μm) (μm) (μm) (μm) (μm) (μm) Tripalmitin 0.162 ± 0.112 ± 0.130 ± 0.118 ± 0.082 ± 0.124 ± 0.184 ± 0.005 0.02 0.004 0.003 0.002 0.004 0.005 Tripalmitin/ 0.130 ± 0.148 ± 0.131 ± 0.117 ± 0.080 ± 0.124 ± 0.191 ± tricaprylin 0.011 0.02 0.003 0.001 0.004 0.002 0.010 (4:1) Palm 0.158 ± 0.199 ± 0.133 ± 0.119 ± 0.081 ± 0.127 ± 0.195 ± stearin 0.007 0.02 0.002 0.002 0.005 0.000 0.010 A B S4. -
Zahnmedizinische Produkte Und Ihre Inhaltsstoffe
Medikamente Zahnmedizinische Produkte III–8.3 Zahnmedizinische Produkte und ihre Inhaltsstoffe Produktname Anbieter/ Inhaltsstoffe Verwendung Hersteller/ (Elemente in Massen-%, Vertrieb seit x = keine Angabe) Adaptic LC Johnson & John Ba-Glas Kunststoff son AH 26 DeTrey Dentsply Pulver: Silber, Wismutoxid, Methenamin, Wurzelkanal- Titandioxid, Harz: Epoxybisphenolharz Füllungsmasse Alba KF Heraeus/Heraeus/ Pd: 40,0; Ag: 53,0; Sn: x; Zn: 3,5; In: 2,0 Zahnlegierung 1988 Alba Lot 810 Heraeus Kulzer Au: 10,00; Pd: 1,00; Cu: 11,00; Ag: 69,00; Dentallot In: 6,00; Zn: 3,00 Alba Lot 880 Heraeus Kulzer Au: 12,00; Pd: 4,00; Cu: 11,00; Ag: 69,00; Dentallot In: 4,00 Alba SG Heraeus/Heraeus/ Au: 10,0; Pd: 21,0; Ag: 57,0; Cu: 10,0; Zn: Zahnlegierung 1953 2,0 Albabond Heraeus/Heraeus/ Pd: 60,5; Ag: 28,0; Sn: 3,0; In: 7,0; Ga: x Zahnlegierung 1980 Albabond A Heraeus/Heraeus/ Pd: 57,0; Ag: 32,8; Sn: 6,8; In: 3,4 Zahnlegierung 1989 Albabond E Heraeus/Heraeus/ Au: 1,6; Pd: 78,4; Cu: 11,0; Sn: x; In: x; Ga: Zahnlegierung 1983 7,5 Albabond EH Heraeus/Heraeus/ Au: 2,0; Pd: 79,0; Cu: 10,0; Ga: 8,8 Zahnlegierung 1984 Albabond GF Heraeus/Heraeus/ Pd: 60,5; Ag: 19,5; Cu: 7,5; Sn: 3,0; In: 9,5 Zahnlegierung 1987 Albabond U Heraeus/Heraeus/ Au: 2,0; Pd: 75,0; Cu: 9,5; Sn: 3,0; In: 7,0; Zahnlegierung 1982 Ga: 3,5 Albiotic Upjohn Lincomycin Antibiotikum Aleram 2 Allgemeine Gold- Au: x; Pd: 78,5; Cu: 10,5; Sn: x; Ga: 8,0 Zahnlegierung u. -
Esterifikasi Gliserol Dari Produk Samping Biodiesel Menjadi Triasetin Menggunakan Katalis Zeolit Alam
Esterifikasi Gliserol Dari Produk Samping Biodiesel Menjadi Triasetin Menggunakan Katalis Zeolit Alam Nirmala Sari 1, Zuchra Helwani 2, dan Hari Rionaldo3 Laboratorium Teknologi Oleokimia Program Studi Teknik Kimia S1, Fakultas Teknik Universitas Riau Kampus Binawidya Km. 12,5 Simpang Baru Panam, Pekanbaru 28293 *Email : [email protected] ABSTRACT Glycerol is a by-product of biodiesel production from transesterification reaction generated 10% volume product. The increase of biodiesel production is followed by the increase of the glycerol as by product. Glycerol when esterified with acetic acid formed Triacetin. Triacetin has many uses for food, non-food and additives in biofuel feedstock that is renewable and environmentally friendly. In this study will be make Triacetin from reaction esterification of crude glycerol purified with acetic acid glacial and using natural zeolite catalyst has been activated. Making triacetin performed with a three-neck flask equipped with a condenser, heating mantle, thermometer and magnetic stirred at 100 ° C, 100 mesh size catalyst and reaction time for 4 hours. Process of qualitative analysis using FT-IR instrument has detected the exixtence of Triacetin product. The variables are varied ratio reactant of glycerol and acetic acid, and the concentration catalyst. The highest conversion obtained for 90.02% in reactan ratio mol glycerol and acetic acid 1: 7, catalyst concentration of 3% to weight of acetic acid. Comparison of reagents give real effect to the conversion of glycerol into Triacetin, while the catalyst concentration does not give a significant effect on glycerol conversion be Triacetin. Keywords: acetic acid, esterification, glycerol, Triacetin 1. Pendahuluan Gliserol merupakan produk samping gliserol ester maleat resin. -
Triglyceride Transesterification in Heterogeneous Reaction System with Calcium Oxide As Catalyst
Rev. Fac. Ing. Univ. Antioquia N.° 57 pp. 7-13. Enero, 2011 Triglyceride transesterification in heterogeneous reaction system with calcium oxide as catalyst Transesterificación de triglicéridos en el sistema de reacción heterogénea con óxido de calcio como catalizador Mónica Becerra Ortega, Aristóbulo Centeno Hurtado, Sonia Azucena Giraldo Duarte* Centro de Investigaciones en Catálisis (CICAT). Escuela de Ingeniería Química. Universidad Industrial de Santander (UIS). Carrera 27 Calle 9. Bucaramanga. Colombia (Recibido el 03 de febrero de 2010. Aceptado el 15 de octubre de 2010) Abstract In this work, the behavior of the CaO as a potential catalyst for the transesterification of triglyceride towards biodiesel production was studied. The effect of the alcohol type, the ratio of alcohol/triacetin, the amount of catalyst, and the chain length of triglyceride on the catalytic behavior of CaO was analyzed. Total conversion was obtained at room temperature with a 6:1 molar ratio of methanol to triacetin over 1% of CaO, after 1 h. It was demonstrated that the whole reaction occurs in heterogeneous phase. During five reaction cycles the CaO maintained a high catalytic activity, showing its good stability. Additionally, it was established that the length of the triglyceride used influenced the transesterification reaction yield due to the steric hindrances and diffusional limitations in the fluid phase. ----- Keywords: Biodiesel, triacetin, basic catalysis, triolein Resumen En este trabajo se estudió el comportamiento del CaO como potencial catalizador en la transesterificación de trigliceridos para la producción de biodiesel. Se analizó el efecto del tipo de alcohol, la relación molar alcohol/triacetina, la cantidad de catalizador y el tamaño de la cadena del triglicérido sobre su comportamiento catalítico. -
2013 Annual Meeting Abstracts Biotechnology
2013 Annual Meeting Abstracts Biotechnology MONDAY AFTERNOON BIO 1.1/PHO 1: Polar Lipids: Chemistry, Technology, and Applications Chair(s): X. Xu, Wilmar Global R&D Center, China; Aarhus University, Denmark; M. Ahmad, Jina Pharmaceuticals Inc., USA Enzymatic "green" Preparation of Sugar-fatty Acid Esters D. Hayes(1) (1)University of Tennessee, United States of America Saccharide-fatty acid esters are an emerging category of biobased surfactants prepared entirely from renewable resources that are used as emulsifiers in foods, cosmetics, and pharmaceuticals, and possess anticancer and insecticidal properties. Typically, the esters are prepared chemically under harsh condition: temperatures near 200 C, employment of solvents, etc., which can cause undesirable side-reactions and produce waste products. Our group has been investigating the use of lipases and novel bioreactor system design to prepare sugar esters under solvent-free conditions and relatively low temperature: ~65 C. Using a stoichiometric feed of saccharide and fatty acid, our approach achieves 90-95% pure ester on a 10-30 gram scale, which, due to the absence of excess reactants and solvent, will require little or no further downstream purification to achieve industrial specifications. The presentation will provide an overview of our recent work, including an evaluation of its physical properties. Deep Eutectic Solvents: new Opportunities for Lipase-catalyzed Reactions E. DURAND(1), J. LECOMTE(2), B. BAREA(3), P. VILLENEUVE(4) (1)CIRAD, UMR IATE, France (2)CIRAD, UMR IATE, France (3)CIRAD, UMR IATE, France (4)CIRAD, UMR IATE, France In recent years, researchers focused on finding green alternative media to organic solvents for enzyme-catalyzed reactions. -
Chemical Kinetics for Synthesis of Triacetin from Biodiesel Byproduct
www.ccsenet.org/ijc International Journal of Chemistry Vol. 4, No. 2; April 2012 Chemical Kinetics for Synthesis of Triacetin from Biodiesel Byproduct Zahrul Mufrodi Department of Chemical Engineering, Ahmad Dahlan University 9 Kapas Street, Yogyakarta 55166, Indonesia Tel: 62-274-743-6596 E-mail: [email protected] Sutijan, Rochmadi & Arief Budiman Department of Chemical Engineering, Gadjah Mada University 2 Grafika Street, Yogyakarta 55281, Indonesia Received: December 9, 2011 Accepted: January 29, 2012 Published: April 1, 2012 doi:10.5539/ijc.v4n2p101 URL: http://dx.doi.org/10.5539/ijc.v4n2p101 The research is financed by KKP3T department of agriculture and Department of national education Indonesia Abstract The reaction kinetic of the glycerol acetylation with acetic acid catalyzed by sulfuric acid has been studied in the frame of continuous triacetin production. Glycerol, acetic acid and sulfuric acid catalyst were reacted in a batch reactor, in order to get reaction kinetics data. The mole ratio of catalyst to glycerol and temperature were studied during the experience. This study concluded that the selectivity of triacetin increased with increase in mole ratio of catalyst to glycerol. Increasing temperatures lead to increase selectivity of triacetin. It will decreased at the time of acetic acid has begun to evaporate. Triacetin synthesis is an exothermic reaction, a higher reaction temperature will cause in shifting the balance toward formation of reactants. This needs to be anticipated by taking one of the products so that the equilibrium shifting toward product formation. Keywords: Reaction kinetic, Glycerol, Acetylation, Triacetin, Acetic acid 1. Introduction Needs of oil energy sources from fossil fuels are increasing, while inventories are running low. -
PARTIAL CHARACTERIZATION of LIPASE from COCOA BEANS (Theobroma Cacao
448 Indo. J. Chem., 2008, 8 (3), 448 - 453 PARTIAL CHARACTERIZATION OF LIPASE FROM COCOA BEANS (Theobroma cacao. L.) OF CLONE PBC 159 Ratna Agung Samsumaharto Faculty of Biology, Setia Budi University, Jl. Let. Jend. Sutoyo Mojosongo – Surakarta 57127 Received 3 April 2008; Accepted 15 October 2008 ABSTRACT A study was carried out to characterize the cocoa lipase from cocoa beans (Theobroma cacao, L.) of clone PBC 159. The optimum temperature of cocoa lipase was 30-40 °C and the pH optimum was 7.0-8.0. The moleculer weight of the lipase enzyme was in between 45-66 kDa. The results indicate that Km value for cocoa bean lipase was 2.63 mM, when trimyristin was used as a substrate. The incubation of cocoa bean lipase with triolein and tributyrin (as substrate) yielded Km of 11.24 and 35.71 mM, respectively. The Vmax value obtained from the incubation of the lipase with a wide range of substrates, including tributyrin, trimyristin and triolein, are expressed as µmole acid/min/mg protein for cocoa lipase. Vmax values decreased with the increase in the triacylglycerol chain-length, with Vmax values of 27.78, 13.16 and 11.63 µmole acid/min/mg protein when incubated with tributyrin, trimyristin and triolein, respectively. Inhibition of lipase occurred in the presence of diisopropyl flourophosphate, N- bromosuccinimide and 5,5-dithiobis-(-2-nitrobenzoic acid). Keywords: characterization, lipase, cocoa beans INTRODUCTION According to Hassan [8] the lipase showed that the optimum temperature for oil palm mesocarp lipase Lipases are ester hydrolases or esterases since activity range between 20.0 to 32.5 °C. -
A DFT Investigation of Methanolysis and Hydrolysis of Triacetin Abstract 1
A DFT investigation of methanolysis and hydrolysis of triacetin Taweetham Limpanuparba, Kraiwan Punyainb, Yuthana Tantirungrotechaic,d,* aDepartment of Chemistry, Faculty of Science, Mahidol University, Bangkok 10400, Thailand bDepartment of Chemistry, Faculty of Science, Naresuan University, Phitsanulok 65000, Thailand cNational Nanotechnology Center (NANOTEC), National Science and Technology Development Agency, Pathumthani 12120, Thailand dTheoretical Chemistry Laboratory, Faculty of Science, Mahidol University, Salaya, Nakhon Pathom 73170, Thailand * Corresponding author at: Address: National Nanotechnology Center (NANOTEC), National Science and Technology Development Agency, Pathumthani 12120, Thailand. This paper was subsequently accepted for publication in Journal of Molecular Structure: THEOCHEM Volume 955, Issues 1–3, 15 September 2010, Pages 23–32 Refer to http://dx.doi.org/10.1016/j.theochem.2010.05.022 for the final published version. Abstract The thermodynamic and kinetic aspects of the methanolysis and hydrolysis reactions of glycerol triacetate or triacetin, a model triacylglycerol compound, were investigated by using Density Functional Theory (DFT) at the B3LYP/6-31++G(d,p) level of calculation. Twelve elementary steps of triacetin methanolysis were studied under acid-catalyzed and base-catalyzed conditions. The mechanism of acid-catalyzed methanolysis reaction which has not been reported yet for any esters was proposed. The effects of substitution, methanolysis/hydrolysis position, solvent and face of nucleophilic attack on the free energy of reaction and activation energy were examined. The prediction confirmed the facile position at the middle position of glycerol observed by NMR techniques. The calculated activation energy and the trends of those factors agree with existing experimental observations in biodiesel production. 1. Introduction Triacylglyceride (TG) is a major constituent of naturally available oil and fat. -
Food Scientist's Guide to Fats and Oils For
FOOD SCIENTIST’S GUIDE TO FATS AND OILS FOR MARGARINE AND SPREADS DEVELOPMENT by KATHLEEN M. MORLOK B.S., University of Minnesota, 2005 A REPORT submitted in partial fulfillment of the requirements for the degree MASTER OF SCIENCE Food Science KANSAS STATE UNIVERSITY Manhattan, Kansas 2010 Approved by: Major Professor Kelly J.K. Getty Animal Sciences & Industry Abstract Fats and oils are an important topic in the margarine and spreads industry. The selection of these ingredients can be based on many factors including flavor, functionality, cost, and health aspects. In general, fat is an important component of a healthy diet. Fat or oil provides nine calories per gram of energy, transports essential vitamins, and is necessary in cellular structure. Major shifts in consumption of fats and oils through history have been driven by consumer demand. An example is the decline in animal fat consumption due to consumers’ concern over saturated fats. Also, consumers’ concern over the obesity epidemic and coronary heart disease has driven demand for new, lower calorie, nutrient-rich spreads products. Fats and oils can be separated into many different subgroups. “Fats” generally refer to lipids that are solid at room temperature while “oils” refer to those that are liquid. Fatty acids can be either saturated or unsaturated. If they are unsaturated, they can be either mono-, di-, or poly-unsaturated. Also, unsaturated bonds can be in the cis or trans conformation. A triglyceride, which is three fatty acids esterified to a glycerol backbone, can have any combination of saturated and unsaturated fatty acids. Triglycerides are the primary components of animal and vegetable fats and oils. -
Formation of Polyol-Fatty Acid Esters by Lipases in Reverse Micellar Media
Formation of Polyol-Fatty Acid Esters by Lipases in Reverse Micellar Media Douglas G. Hayes* and Erdogan Gulari’ Department of Chemical Engineering, University of Michigan, Ann Arbor, Michigan 48109-2 136 Received July 19, 1991Mccepted January 7, 1992 The synthesis of polyol-fatty acid esters has strong implica- content to shift thermodynamic equilibrium in favor of tions in such industries as foods, cosmetics, and polymers. esterification over hydrolysis, and be heterogeneous or We have investigated these esterification reactions employ- biphasic in nature to accommodate all media compo- ing the polyols ethylene glycol, 2-monoglyceride, and sugars and their derivatives with the biocatalyst lipase in water/ nents and provide lipases with an interface, which in AOT/isooctane reverse micellar media. For the first reaction, most cases enhances the enzymes’ performance. We 50-60% conversion was achieved and product selectivity have employed reverse micellar media composed of toward the monoester over the diester shown possible by nanometer-sized dispersions of aqueous or polar mate- employing lipase from Rhizopus delemar. A simple kinetic rial in a lipophilic organic continuum formed by the ac- model based on the formation of an acyl-enzyme interme- diate accurately predicted the effect of polyol concentra- tion of surfactants/cosurfactants to fulfill these criteria. tion but not the effect of fatty acid or water concentration In addition, compared to alternate types of reaction me- probably due to the model exclusion of partitioning effects. dia, reverse micellar media provide excellent enzyme- The success of this reaction in reverse micellar media is substrate contact due to its dynamic nature, is easy to due greatly to its capacity to solubilize large quantities of prepare, and has a large amount of interfacial area. -
Glycerin and the Market
GLYCERIN AND THE MARKET By Valentine Chijioke Mbamalu Approved: Frank Jones Tricia Thomas Professor of Engineering Assistant Professor of Engineering (Chair) (Committee Member) Neslihan Alp William Sutton Professor of Engineering Dean of the College of Engineering and (Committee Member) Computer Science A. Jerald Ainsworth Dean of the Graduate School GLYCERIN AND THE MARKET By Valentine Chijioke Mbamalu A Thesis Submitted to the Faculty of the University of Tennessee at Chattanooga in Partial Fulfillment of the Requirements of the Degree of Master’s of Engineering The University of Tennessee at Chattanooga Chattanooga, Tennessee May 2013 ii Copyright © 2013 Valentine Chijioke Mbamalu All Rights Reserved iii ABSTRACT Glycerin, a trihydric alcohol, had once enjoyed a good market value but, is now faced with global oversupply and this makes the market volatile. It is a byproduct of biodiesel production thought as an added value to biodiesel operations. It is now faced with an unpredictable market and probably oversupply as an outcome of increased biodiesel production. There are two types of glycerin market; the refined glycerin with its solid price and crude glycerin which is volatile. There are new applications for glycerin being developed or being implemented and it will be a source of strength to the market. This thesis takes an in-depth review of glycerol from its sources to refining and the market. iv ACKNOWLEDGEMENTS First and foremost I thank the Almighty God for the strength and grace He has given me, without which I could not have made it to this point. I express my profound gratitude to my thesis advisor Dr. -
Provisional Peer-Reviewed Toxicity Values for Triacetin (Casrn 102-76-1)
EPA/690/R-12/034F l Final 11-19-2012 Provisional Peer-Reviewed Toxicity Values for Triacetin (CASRN 102-76-1) Superfund Health Risk Technical Support Center National Center for Environmental Assessment Office of Research and Development U.S. Environmental Protection Agency Cincinnati, OH 45268 AUTHORS, CONTRIBUTORS, AND REVIEWERS CHEMICAL MANAGER Jason C. Lambert, PhD, DABT National Center for Environmental Assessment, Cincinnati, OH DRAFT DOCUMENT PREPARED BY ICF International 9300 Lee Highway Fairfax, VA 22031 PRIMARY INTERNAL REVIEWERS Ghazi Dannan, PhD National Center for Environmental Assessment, Washington, DC Zheng (Jenny) Li, PhD, DABT National Center for Environmental Assessment, Washington, DC This document was externally peer reviewed under contract to Eastern Research Group, Inc. 110 Hartwell Avenue Lexington, MA 02421-3136 Questions regarding the contents of this document may be directed to the U.S. EPA Office of Research and Development’s National Center for Environmental Assessment, Superfund Health Risk Technical Support Center (513-569-7300). i Triacetin CONTENTS COMMONLY USED ABBREVIATIONS ................................................................................... iii BACKGROUND ............................................................................................................................ 1 DISCLAIMERS .............................................................................................................................. 1 QUESTIONS REGARDING PPRTVS .........................................................................................