From Pseudomonas Fmgi CRDA 037

Total Page:16

File Type:pdf, Size:1020Kb

From Pseudomonas Fmgi CRDA 037 Characterization of Purified Extracellular Lipase Fractions from Pseudomonas fmgi CRDA 037 by Aliar Abdul Wahrb A thesis submitted to the Faculty of Gnduate Studies and Rtseareh in partial fulîiiment of the rquirements of the degree of Muter of Science O~liaaAbdul Wahab Department of Food Science and Agncultural Chemistry McGill University Montreal, Qu&= National Library Bibliothèque nationale 1+1 ,,nada du Canada Acquisitions and Acquisitions et Bibliographic Services senfices bibliographiques 395 Wellington Street 395, rw Wdlington OttawaON K1AON4 OnawaON K1AW canada canada The author has granted a non- L'auteur a accordé une licence non exclusive licence allowing the exclusive permettant a la National Library of Canada to Bibliothèque nationale du Canada de reproduce, loan, distribute or sell reproduire, prêter, distribuer ou copies of this thesis in microform, vendre des copies de cette thèse sous paper or electronic formats. la foxme de microfiche/fiim, de reproduction sur papier ou sur format électronique. The author retains ownership of the L'auteur conserve la propriété du copyright in ths thesis. Neither the droit d'auteur qui protège cette thèse. thesis nor substantial extracts kom it Ni la thèse ni des extraits substantiels may be printed or othenvise de celle-ci ne doivent être imprimés reproduced without the author's ou autrement reproduits sans son permission. autorisation. SHORT TITLE EXTRACELLULAR LIPASES FROM PSEUDOMONAS FRQGI ABSTRACT M. Sc. Aliar Abdul Wabab The partially purified extracellular lipase fkom Pseudornoms fiagîCRDA 037, obtained by ammonium sulfate prccipitation, was subjected to iùrther purification by successive ion-exchange and sue-exclusion chromatographies using the Fast Protein Liquid Chromatography system. The purification of the partially purified lipase resulted in two enzymatic fiactions, FIVa' and FIVb', with a purification-fold of 169 and 295, respectively. Native electrophoretic analyses revded the presence of three bands for fiaction FIVa', with estimated molecular weights (MW) of 16.2, 25.8 and 38.5 kDa and two bands for FIVb', with estimated MW of 15.2 and 25.8 kDa. The two purified fiactions, FNa' and FM', showed an optimum pH of 9.5 and 10.0, respectively, and an optimum temperature of 80°C. The Km values for FIVa' and FIVb' were 3.85 and 5.49 rnM and the V,, values were 2.78 and 2.09 Ulmg, respectively, using triacetin as a substrate. The purified lipase fiactions retained more than 90% of their activity when stored at room temperature for 36 h. The lipase activity of the purified lipase fiactions was compietely inhibited by 10 mM of FeC12, FeC13 and Eliman's ragent. However, 10 mM of CaCIz and EDTA activated the two purified lipase fiactions by 20 to Both fiactions exhibited high specificity towards short- and long-chain fatty acid esters of triacylglycerols. Fraction FIVa' showed higher specificity towards triacetin, tristearin and tripalmitin, whereas fraction FIVb' exhibited higher activity with triacetin, trimyristin and triolein. In addition, the two purified lipase fractions were able to catalyze, to aimost the same extent, the hydrolysis of butter and olive, canola and fish oils. The gas-liquid chromatography analysis of fke fatty acids, obtained by the hydrolysis of the four edible oils, revealed that fraction FIVa' was more specific for the hydrolysis of fatty acid esters chah lengths of C 12 to C 18 whereas fiaction FIVb' showed a non-specific hydrolyzing activity towards fatty acid esters. RÉSUMÉ M. Sc. AIUt Abdul Wahib La lipase partiellement purifiée de Pseudornoltos Fagi CRDA 037, obtenue par précipitation au sulfate d'ammonium, a été davantage purifiée par chromatographies échangeuses d'ions a de tamisage moléculaire a utilisant le système Fast Protein Liquid Chromatography. Deux fhctions purifiées ont été obtenues, FIVa' et FIVb', avec un facteur de purification de 169 a 195, respectivement. Les analyses d'électrophorèse native ont révélé la présence de trois bandes pour k MonFIVéî', avec des poids moléculaires (MW) estimés de 16,2, 25'8 et 38,s kDa et de deux bandes pour FIVb', avec des MW estimés de 15,2 et 25'8 kDa, respectivement. Les deux nanMns purifiées, FIVa' a Fm', ont montré un pH optimum à 9.5 a 10,0, respectivement, et une température de 80°C. Les valeurs de Km pour FNa' et FIVb' ont été de 3,85 et 5'49 mM et les valeurs de V, ont été de 2-78 et 2,09 Ulrng, respectivement, en utilisant la tracétine comme substrat. Après avoir stockée a température ambiante pour une période de 72 h, les fiactions lipasiques purifiées ont conservé plus de 90 ./. de leur activité pendant 36 h. L'activité lipasique des fiactions purifiées a étt5 compléternent inhibée par FeC12, FeCl3 et le réactif dYEllmanà 10 mM. Cependant, CaC12 a EDTA ont activé l'activité des fiactions purifiées de 20 a 50 %. Les deux fractions ont démontré une forte spécificité vis-à-vis des esters de triglycérides a courtes et a longues chaînes. La fiaction FIVa' a montré une forte spécificité envers la tnacétine, la trimyristine et la trioléine. De plus, les deux &actions purifiées ont catalysé l'hydrolyse de beurre et d'huiles d'olive, de canola et de poisson pratiquement au même degré. Les analyses de chromatographie en phase gazeuse d'acides gras libérés par l'hydrolyse des quatre huiles comestibles ont montré que la fraction FIVa' étaiat spécifique pour les esters d'acides gras a longues chaînes de C12:O à Cl8:O alors que la fraction FIVb' etait non-spécifique, hydroplysant aussi bien les esters d'acides gras à longues chaînes saturées et insaturés. I would like to thank my supervisor, Dr. Seh Kennasha, for the guidance, suppofi and patience he offered throughout my study. 1 would iike to extend my gratitude to Dr. André Morin for his numerous advises and his arrangement for the biomass production at the Agriculture Agri-Food Center, CRDA 1 would aiso like to thank Anwer, Marie-Odile and Tami for their assistance. Also special thanks to Pierre-Yves and Wigdan for their valuable advises and Xavier for writing the résumé. And many thanks to al1 my colleagues for their fnendship and good spirit. 1 would like to thank my husband, Osama, my sister, Dalia, my brother, Qussay, my linle sister, Noor, and especiaily my parents for their moral qqmn. TABLE OF CONTENTS LIST OF FIGURES.................................................................................................. ..VIII... 1, INTRODUCTION ..................................................................................................... 1 2- LITERATURE REVIEW .............m~~o~m~ooa~~~o~~o~~~~~~~~~-~moa~m~~~m~ma~oa~a~~a~o--~~~~~~a~~~~ao~~~oa~oam~~o4 2.1. Flavor Production Biotechnology .............................................................................. 4 2.2. Pseudomonas fiagi .................................................................................................. -6 2.2. I . Physical Features ............................................................................................. 6 2.2.2. FhrPra&ct~on by Pseudomomtsfiagrgr ......................................................... 6 2.2.3. Mechism of Flavor Production by P .fiagrgr ..................................................... 7 2.3. Lipases .................................................................................................................... -8 2.3.1. Nomencluture ................................................................................................... 8 2.3.2. Sources of Lzpes ............... .... ................................................................. 9 2.3.3. Characteristics of Lipes-............................................................................. 10 2.3.4 Production of Microbiai Lipares................. .... ............................................. 12 2.3.5. LipeKinetics ................................................................................................ 13 2.3.6. Lipaw Substrores .............. ... ....................................................................... I5 2.3.7. Assay of Lipaw Activity ................................................................................... 16 2.3.7.1. Titrimetric Method .................................................................................... 16 2.3 .7.2. Spectrophotometric Method ...................................................................... 17 2.3.7.3. Fluorimetric Method .................................................................................. 18 2.3.8. LipeSpecr/ciiq ............................................................................................. 18 2.3 .8.1. Positional Specificity ................................................................................. 19 2.3.8.2. Fatty Acid Specificity .................... .. ..................................................... 19 2.3.8.3. Stereoselectivity ....................................................................................... -20 2.3.9. Punijication of li'es..................................................................................... 21 2-3.10. Industrial Application of Lipes................................................................... 23 3. MATERIALS AND METHODS............................................................................. 25 3.1. Bacterial Strain ....................................................................................................... 25 3.2. Chemicals ............................................................................................................... 25 3.3. Biomass
Recommended publications
  • Calculation of Thermophysical Properties of Oils and Triacylglycerols Using an Extended Constituent Fragments Approach
    CT&F - Ciencia, Tecnología y Futuro - Vol. 5 Num. 1 Dec. 2012 Pag. 67-82 CIBSCOL+ ISSN 0122-5383 CALCULATION OF THERMOPHYSICAL PROPERTIES OF OILS AND TRIACYLGLYCEROLS USING AN EXTENDED CONSTITUENT FRAGMENTS APPROACH CÁLCULO DE PROPIEDADES TERMOFÍSICAS DE ACEITES Y TRIACILGLICEROLES EMPLEANDO UNA METODOLOGÍA EXTENDIDA DE FRAGMENTOS Diana-Carolina Cruz-Forero1, Oscar-Andrés González-Ruiz1 and Luis-Javier López-Giraldo1* 1Universidad Industrial de Santander, Bucaramanga, Santander, Colombia e-mail: [email protected] (Received Jul. 05, 2012; Accepted Nov. 09, 2012) ABSTRACT his paper validates and implements an Extended Constituent Fragments methodology (ECF) for the calculation of thermophysical properties of vegetable oils considering the latter as triglyceride (TAG's) Tmixtures, both homogeneous and heterogeneous. For this purpose, three different vegetables oils were chosen (soybean oil, canola and olive) and their TAG's profiles were estimated using the ECN 42 generalized method. The ECF methodology estimates the properties of TAG's from their fragment composition and spe- cific parameters of each property, which are adjusted using experimental information available in literature. The average relative errors of calculated properties were between 1 and 32% depending on the oil and the property. These errors were significantly lower than those obtained using the Aspen HYSYS commercial software, which oscillates between 70 and 100%. Additionally, by extrapolating the constituent fragments methodology a method for calculating boiling temperatures of TAG's with average relative errors of ~1% was proposed. The calculations of properties for the ECF method were performed using the OIL-CALPROP software developed specifically for this purpose. Keywords: Vegetable oils, Triglycerides, Prediction, Thermodynamic properties, Calorific capacity, Boiling temperature, Simulation, Software.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • Extraction of Trimyristin from Nutmeg
    Extraction of Trimyristin from Nutmeg Note: With consent, your experimental data may be used in a research presentation at the American Chemical Society national meeting. Please consider this when performing the experiment! Read Standard Reflux on page 201 of “The Organic Chem Lab Survival Manual.” Prelab Question 1: Trimyristin is a triglyceride. What are triglycerides? Prelab Question 2: How do microwaves heat? Microwave Procedure: Add approximately 2.5 g of ground nutmeg (record exact mass) and 15 mL of diethyl ether to microwave vessel. Cap microwave vessel as directed. (Monitor vessel capped differently.) Place all microwave vessels into Milestone Ethos laboratory microwave system as directed. (Monitor vessel is equipped with fiber optic temperature probe.) All vessels are heated according to the following temperature profile: Step 1 Ramp from room temperature to 65°C in 1.5 min Step 2 Hold at 65°C for 5.5 min Step 3 Vent (cooling) for 10 min Allow vessels to cool below boiling point of ether before uncapping. (Ice bath can be used to speed up process.) Process microwave extract as directed with conventional extraction method.* Traditional Extraction: Weigh approximately 2.5 g of finely ground nutmeg and combine it with 15 mL of diethyl ether in an appropriate round-bottom flask. Attach a water-cooled condenser to the vial and set the apparatus in an aluminum block on a hot plate. Gently heat the mixture under reflux for 45 minutes or more. *Filter the mixture by gravity. Wash the nutmeg residue in the filter paper with a small amount of ether, saving the filtrate.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • Page 1 of 12Journal Name RSC Advances Dynamic Article Links ►
    RSC Advances This is an Accepted Manuscript, which has been through the Royal Society of Chemistry peer review process and has been accepted for publication. Accepted Manuscripts are published online shortly after acceptance, before technical editing, formatting and proof reading. Using this free service, authors can make their results available to the community, in citable form, before we publish the edited article. This Accepted Manuscript will be replaced by the edited, formatted and paginated article as soon as this is available. You can find more information about Accepted Manuscripts in the Information for Authors. Please note that technical editing may introduce minor changes to the text and/or graphics, which may alter content. The journal’s standard Terms & Conditions and the Ethical guidelines still apply. In no event shall the Royal Society of Chemistry be held responsible for any errors or omissions in this Accepted Manuscript or any consequences arising from the use of any information it contains. www.rsc.org/advances Page 1 of 12Journal Name RSC Advances Dynamic Article Links ► Cite this: DOI: 10.1039/c0xx00000x www.rsc.org/xxxxxx ARTICLE TYPE Trends and demands in solid-liquid equilibrium of lipidic mixtures Guilherme J. Maximo, a,c Mariana C. Costa, b João A. P. Coutinho, c and Antonio J. A. Meirelles a Received (in XXX, XXX) Xth XXXXXXXXX 20XX, Accepted Xth XXXXXXXXX 20XX DOI: 10.1039/b000000x 5 The production of fats and oils presents a remarkable impact in the economy, in particular in developing countries. In order to deal with the upcoming demands of the oil chemistry industry, the study of the solid-liquid equilibrium of fats and oils is highly relevant as it may support the development of new processes and products, as well as improve those already existent.
    [Show full text]
  • 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.
    [Show full text]
  • 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 .........................................................................................
    [Show full text]