DOCSLIB.ORG

Acid Esterification-Alkaline Transesterification Process For

Total Page：16

File Type：pdf, Size：1020Kb

Download full-text PDF Read full-text
Acid Esterification-Alkaline Transesterification Process For Journal of Oleo Science Copyright ©2012 by Japan Oil Chemists’ Society J. Oleo Sci. 61, (2) 81-88 (2012) Acid Esterifi cation-Alkaline Transesterifi cation Process for Methyl Ester Production from Crude Rubber Seed Oil Prachasanti Thaiyasuit, Kulachate Pianthong＊ and Ittipon Worapun Department of Mechanical Engineering, Faculty of Engineering, Ubon Ratchathani University (Ubonratchathani, 34190, THAILAND) Abstract: This study aims to examine methods and the most suitable conditions for producing methyl ester from crude rubber seed oil. An acid esterifi cation-alkaline transesterifi cation process is proposed. In the experiment, the 20% FFA of crude rubber seed oil could be reduced to 3% FFA by acid esterifi cation. The product after esterifi ed was then tranesterifi ed by alkaline transesterifi cation process. By this method, the maximum yield of methyl ester was 90% by mass. The overall consumption of methanol was 10.5:1 by molar ratio. The yielded methyl ester was tested for its fuel properties and met required standards. The major fatty acid methyl ester compositions were analyzed and constituted of methyl linoleate 41.57%, methyl oleate 24.87%, and methyl lonolenate 15.16%. Therefore, the cetane number of methyl ester could be estimated as 47.85, while the tested result of motor cetane number was 51.20. Key words: methyl ester, crude rubber seed oil, esterifi cation, transesterifi cation 1 INTRODUCTION madhas et al.5）had found that the FFA content in the crude Nowadays, the shortage or crisis of fossil fuel lately rubber seed oil was about 17％ and 19％ of FFA in mahua becomes one of the most concerns in automotive industry oil was found by Ghadge and Raheman6）. This FFA value is and world energy sector. This infl uences researchers and significantly high and obstructs the transesterification industries to search for a renewable energy to compensate process in the methyl ester production. It has been con- the fossil fuel. Methyl ester fuel is one of the possible firmed that the ester yield decreases with increasing in choices, because it is renewable and free of sulfur. Methyl FFA significantly. Usually, the alkaline-catalyzed trans- ester contains about 10-11％ oxygen by weight. This char- esterifi cation takes place well only with refi ned oil having acteristic reduces the emissions of CO, HC, and particulate FFA value of less than 2％5－7）. Canakci and Van Gerpen8） matter in the exhaust gas compared with diesel fuel. As it had found that transesterification would not occur if the is obtained mainly from plantation resources, it is able to FFA content in the oil were above 3％. Usually, free car- reduce the lifecycle of carbon dioxide by almost 78％ com- boxylic acids form soaps with alkaline-catalyzed trans- pared to conventional diesel fuel1）, while its fuel properties esterification, hence they impede the separation of the are very closed to diesel. Also, methyl ester can be used in glycerol phase due to the emulsifying effects of soaps and diesel engines with few or no engine modifi cations2）. lower their catalytic activity9, 10）. In extreme cases, of more Usually, methyl ester has been produced from the edible than 5％ FFA oil, Canakci and Van Gerpen11）reported that plant oils such as soybean oil3）and palm oil4）. However, it is the reacted mixture might completely gel after the addition always controversial on using edible oil or food resource as of KOH or NaOH, so that the charge has to be discarded. fuels. Therefore, in recent years, considerable research Therefore, the single step alkaline-catalyzed tranesterifi ca- effort has been directed towards replacing food oils with tion process is not suitable to produce methyl esters from various non-edible, wasted, or low-cost oils. The unrefi ned high FFA crude oil. In order to reduce the FFA, the crude non-edible oils have been considered, however they have oil should be refi ned, but the overall production cost of the high impurities such as free fatty acid（FFA）and phospha- methyl ester will be increased. The single step acid trans- tide. These impurities impede the transesterification esterifi cation is a typical method of producing methyl ester process in the methyl ester production. For instance, Ra- from high FFA oil, however, it requires more methanol, ＊Correspondence to: Kulachate Pianthong, Department of Mechanical Engineering, Faculty of Engineering, Ubon Ratchathani University, Warinchamrab, Ubonratchathani, 34190, THAILAND. E-mail: [email protected] Accepted September 26, 2011 (received for review August 19, 2011) Journal of Oleo Science ISSN 1345-8957 print / ISSN 1347-3352 online http://www.jstage.jst.go.jp/browse/jos/ http://mc.manusriptcentral.com/jjocs 81 P. Thaiyasuit, K. Pianthong and I. Worapun high temperature, and is also time consuming. 600 which is widely growth in Thailand. The rubber seeds Recently, researchers searched for means to produce were cracked and the kernels（52.5％ of seed weight）were methyl ester from high FFA oil such as non-edible crude dried in the oven at 100℃ for 20 h. The CRSO was extract- plant oils, animal oils, and fi sh oils. The reduction of FFA in ed from kernels by hydraulic press machine and was about crude oil before tranesterifi cation process has been exam- 10％ of seed weight as shown in Fig. 1. The extracted ined. This method is also effi cient to produce methyl ester crude rubber seed oil usually contains sediment of kernel from high FFA oils. However, it consumes more methanol, and moisture. The CRSO should be cleared from adulter- as Ghadge and Raheman6）studied the production of methyl ants before the acid esterifi cation process in order to avoid ester from mahua oil having 19％ FFA by pretreatment the imperfection of the process. The dregs of the kernel process and transesterifi cation process. The pretreatment can be removed by the filter fabric. The moisture in the process comprised of double acid-esterifi cation. The 19％ CRSO is in water form. It is found that existence the addi- high FFA level of mahua oil was reduced to less than 1％ tion of 0.5％ water to a mixture of oil, methanol, and sulfu- by this pretreatment process. This process consumed 0.7 ric acid could reduce ester conversion from 95％ to below v/v（16.8:1 molar ratio）methanol-to-oil ratio. Then, the 90％. Also at a water content of 5％, ester conversion de- product of pretreatment process was proceed to trans- creased to only 5.6％11）. Thereby, the fi ltered oil is heated esterifi cation process and consumed methanol 0.25 v/v（6:1 at 120℃ for 5 min to remove the moisture. Then, the free molar ratio）, thus the overall of methanol consumption was fatty acid（FFA）content of CRSO was determined. It was 22.8:1 in molar ratio. Ramadhas et al.5）investigated on the found that the FFA content was increased associate with production of methyl ester from 17％ FFA rubber seed oil the times keeping the rubber seed before extracting crude by two steps transesterifi cation process. The fi rst step was oil as shown in Fig. 2. The CRSO using in this study has acid-esterification and consumed methanol 6:1 in molar FFA content of 20％（Oleic）. The physical properties of ratio. The second step consumed methanol 9:1, thus the CRSO tested by the Research and Technology Institute of overall of methanol consumption was 15:1 in molar ratio. the Petroleum Authority of Thailand（PTT Public Company By this method, over usage of methanol, compare to theo- Limited）are shown in Table 1. The fatty acid compositions retical requirement, is unavoidable. Ei-Mashad et al.12） analysis carried out by the Thailand Institute of Scientifi c found the two steps transesterification was effective and Technological Research（TISTR）with gas chromato- method for producing methyl ester from the acidified graphic method are shown in Table 2. Knowing the fatty salmon oil having 6％ FFA. The 6％ FFA salmon oil was acid composition, the molecular mass of the CRSO can be reduce to 1.5％ by esterifi cation and consumed methanol then estimated. In this research, the molecular mass of about 9:1 in molar ratio. In the second step, the methanol CRSO was determined as 872.4 g/mole. This molecular was used at molar ratio about 5:1 for transesterification. mass is very useful for the calculation of the amount of the The overall methanol consumption of this studied was 14:1. catalyst and methyl alcohol in the esterifi cation and tranes- Even thought the two steps transesterifi cation can be suit- able for produce methyl ester from high FFA crude oils, however it consume too much methanol. Therefore, the aim of this study is to examine the method to reduce the consumption of methanol in methyl ester production from non-edible high FFA crude oil. The non-edible high FFA crude oil in this study was crude rubber seed oil（CRSO）. It was extracted from the rubber seed kernels and then carried out to produce methyl ester by the acid esterification-alkaline transesterification process. The acid esterification process was for reducing FFA content of the CRSO. Then the product of acid esteri- fi cation is transesterifi ed using alkaline catalyst in the alka- line transesterification process. Then fuel properties of methyl ester from rubber seed oil were examined and com- pared with diesel and methyl ester standards. 2 MATERIALS AND METHODS Fresh rubber seeds were collected from the local area called Ubonratchathani, Thailand. The rubber tree is RRIM Fig. 1 Rubber seed and crude rubber seed oil. 82 J. Oleo Sci. 61, (2) 81-88 (2012) Acid Esterifi cation-Alkaline Transesterifi cation Process by the acid esterification-alkaline transesterification process.
Load more

Recommended publications
  • Catalyst in Basic Oleochemicals
    View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Diponegoro University Institutional Repository Bulletin of Chemical Reaction Engineering & Catalysis, 2(2-3), 2007, 22-31 Catalyst in Basic Oleochemicals Eva Suyenty, Herlina Sentosa, Mariani Agustine, Sandy Anwar, Abun Lie, and Erwin Sutanto * Research and Development Department, PT. Ecogreen Oleochemicals Jln. Pelabuhan Kav 1, Kabil, Batam 29435, Telp/Fax: (0778)711374 Presented at Symposium and Congress of MKICS 2007, 18-19 April 2007, Semarang, Indonesia Abstract Currently Indonesia is the world largest palm oil producer with production volume reaching 16 million tones per annum. The high crude oil and ethylene prices in the last 3 – 4 years contribute to the healthy demand growth for basic oleochemicals: fatty acids and fatty alcohols. Oleochemicals are starting to replace crude oil derived products in various applications. As widely practiced in petrochemical industry, catalyst plays a very important role in the production of basic oleochemicals. Catalytic reactions are abound in the production of oleochemicals: Nickel based catalysts are used in the hydrogenation of unsaturated fatty ac- ids; sodium methylate catalyst in the transesterification of triglycerides; sulfonic based polystyrene resin catalyst in esterification of fatty acids; and copper chromite/copper zinc catalyst in the high pressure hydro- genation of methyl esters or fatty acids to produce fatty alcohols. To maintain long catalyst life, it is crucial to ensure the absence of catalyst poisons and inhibitors in the feed. The preparation methods of nickel and copper chromite catalysts are as follows: precipitation, filtration, drying, and calcinations. Sodium methy- late is derived from direct reaction of sodium metal and methanol under inert gas.
    [Show full text]
  • Characterization of the Fatty Acid Composition of Nannochloropsis
    Characterization of the Fatty Acid Composition of Nannochloropsis salina as a Determinant of Biodiesel Properties Nagwa Gamal-ElDin Mohammady Department of Botany and Microbiology, Faculty of Science, Moharam Bey 21511, Alexandria University, Alexandria, Egypt. Fax: +203 3911 794. E-mail: [email protected] Z. Naturforsch. 66 c, 328 – 332 (2011); received November 21, 2010/March 27, 2011 Nannochloropsis salina was cultured batch-wise to evaluate the potential of the alga to produce biodiesel. The cells were harvested at the end of the exponential growth phase when the concentration was 18 · 106 cells/mL culture. The growth estimated as dry weight from this cell number was (3.8 0.7) mg/L. The lipid and triglyceride contents were 40% and 12% on a dry weight basis, respectively. The amount of the ratio triglycerides/total lipids was approximately 0.3. The composition of triglyceride fatty acid methyl esters (biodiesel) was analysed by gas- liquid chromatography and identifi ed as: C14:0, C16:0, C16:1, C18:0, C18:1, C18:2, C18:3, C20:1, and C20:5. The ratio of unsaturated to saturated fatty acid contents was approximate- ly 4.4. Additionally, the characterization of each individual fatty acid ester was discussed with regard to the fuel properties of biodiesel produced by the alga. Key words: Biodiesel, Lipids, Nannochloropsis salina Introduction Depending on species, many microalgae have been described as lipid-rich strains for their hy- The use of biofuels can play an important role drocarbons and other complex oils. However, not in avoiding excessive dependence on fossil fu- all algal oils are satisfactory for the production els and reducing pollution by greenhouse gases of biodiesel (Guschina and Harwood, 2006), due emission (Gouveia and Oliveira, 2009).
    [Show full text]
  • Comparative Study on Properties of Methyl Ester of Cotton Seed Oil and Methyl Ester of Mango Seed Oil with Diesel by K
    Global Journal of Researches in Engineering: B Automotive Engineering Volume 14 Issue 2 Version 1.0 Year 2014 Type: Double Blind Peer Reviewed International Research Journal Publisher: Global Journals Inc. (USA) Online ISSN: 2249-4596 & Print ISSN: 0975-5861 Comparative Study on Properties of Methyl Ester of Cotton Seed Oil and Methyl Ester of Mango Seed Oil with Diesel By K. Vijayaraj & A. P. Sathiyagnanam Annamalai University, India Abstract- The use of fatty acid methyl esters (FAME), often referred to as biodiesel, instead of fossil diesel fuel is under consideration in order to increase the share of fuels from renewable sources and to reduce green house gas emissions. An alternative fuel must be technically feasible, economically competitive, environmentally acceptable and easily available. Fatty acid methyl esters have found to befit all these essential qualities. Fatty acid methyl esters derived from various vegetable oils / animal fats have gained importance as an alternative fuel for diesel engines and almost no modifications are required for using biodiesel. The research on alternative fuels for compression engine has become essential due to depletion of petroleum products and its major contribution for pollution, where vegetable oil promises best alternative fuel. Vegetable oils, due to their agricultural origin are able to reduce net CO2 emissions to the atmosphere. But the major disadvantage of vegetable oil is its viscosity which is higher than diesel. In this study, the Methyl Ester of Cotton Seed oil (MECSO) and Methyl Ester of Mango Seed oil (MEMSO) from non-edible oils of Cotton seed oil and Mango seed oil are prepared, their properties are compared in order to meet EN 14214/ASTM D6751 Standards for biodiesel and with the standards of diesel fuel.
    [Show full text]
  • Epoxidation of Fatty Acid Methyl Esters Derived from Algae Biomass to Develop Sustainable Bio-Based Epoxy Resins
    polymers Article Epoxidation of Fatty Acid Methyl Esters Derived from Algae Biomass to Develop Sustainable Bio-Based Epoxy Resins Pamela Hidalgo 1,*, Simona Álvarez 1, Renato Hunter 2 and Alejandra Sánchez 1 1 Department of Industrial Processes, Faculty of Engineering, Universidad Católica de Temuco, Temuco 4780000, Chile; [email protected] (S.Á.); [email protected] (A.S.) 2 Department of Mechanical Engineering, Universidad de La Frontera, Casilla 54-D, Temuco 4811230, Chile; [email protected] * Correspondence: [email protected]; Tel.: +56-45-222-5672 Received: 15 June 2020; Accepted: 7 September 2020; Published: 10 October 2020 Abstract: The objective of this research was to investigate the development of epoxides from Chlorella vulgaris lipids to obtain a novel bio-based resin. The process involved the production of fatty acid methyl esters (FAMEs) by in situ transesterification of microalgal biomass, followed by epoxidation of the FAMEs to obtain bioresin. During the FAME production process, an assessment was made of the main factors affecting the production of unsaturated fatty acid methyl esters (UFAMEs), such as catalyst dosage and methanol:hexane volume ratio. For step epoxidation, an evaluation of the catalyst concentration, temperature and formic acid:hydrogen peroxide ratio was made. From the results obtained, UFAME production was maximized using 20 wt% of catalyst dosage and a volume ratio of 1:2 (v/v, methanol:hexane). Then, in the epoxidation stage, a higher yield was obtained using 1 wt% of catalyst with a volume ratio of 1:1 and maintaining a temperature of 70 ◦C. The bioresin was blended with neat epoxy resin (DGEBA) and cured with tetraethylenepentamine (TEPA).
    [Show full text]
  • FAME (Fatty Acid Methyl Ester)
    SAFETY DATA SHEET according to Regulation (EC) No. 1907/2006 (REACH) Revision date: 10-Jan-2018 Print date: 10-Jan-2018 Version: 4 Page 1/11 FAME (Fatty Acid Methyl Ester) SECTION 1: Identification of the substance/mixture and of the company/ undertaking 1.1. Product identifier Trade name/designation: FAME (Fatty Acid Methyl Ester) Other means of identification: Biodiesel, RME CAS No.: REACH No.: 68990-52-3 01-2119485821-32-0035 EC No.: 273-606-8 1.2. Relevant identified uses of the substance or mixture and uses advised against Use of the substance/mixture: Fuel, fuel component, solvent, carrier liquid for additives Relevant identified uses: Sector of uses [SU] SU 1: Agriculture, forestry, fishery SU 2a: Mining (without offshore industries) SU 2b: Offshore industries SU 5: Manufacture of textiles, leather, fur SU 6a: Manufacture of wood and wood products SU 6b: Manufacture of pulp, paper and paper products SU 7: Printing and reproduction of recorded media SU 8: Manufacture of bulk, large scale chemicals (including petroleum products) SU 9: Manufacture of fine chemicals SU 11: Manufacture of rubber products SU 12: Manufacture of plastics products, including compounding and conversion SU 13: Manufacture of other non-metallic mineral products, e.g. plasters, cement SU 14: Manufacture of basic metals, including alloys SU 15: Manufacture of fabricated metal products, except machinery and equipment SU 16: Manufacture of computer, electronic and optical products, electrical equipment SU 17: General manufacturing, e.g. machinery, equipment, vehicles, other transport equipment SU 18: Manufacture of furniture Product Categories [PC] PC 1: Adhesives, sealants PC 2: Adsorbents PC 3: Air care products PC 7: Base metals and alloys PC 9a: Coatings and paints, thinners, paint removers PC 9b: Fillers, putties, plasters, modelling clay PC 9c: Finger paints PC 11: Explosives PC 12: Fertilizers PC 13: Fuels PC 14: Metal surface treatment products PC 15: Non-metal surface treatment products PC 16: Heat transfer fluids PC 17: Hydraulic fluids Issued by AGQM Biodiesel e.V.
    [Show full text]
  • Microalgal Species Selection for Biodiesel Production Based on Fuel Properties Derived from Fatty Acid Profiles
    Energies 2013, 6, 5676-5702; doi:10.3390/en6115676 OPEN ACCESS energies ISSN 1996–1073 www.mdpi.com/journal/energies Article Microalgal Species Selection for Biodiesel Production Based on Fuel Properties Derived from Fatty Acid Profiles Muhammad Aminul Islam 1,*, Marie Magnusson 2,3, Richard J. Brown 1, Godwin A. Ayoko 1, Md. Nurun Nabi 1 and Kirsten Heimann 2,3,4,* 1 Biofuel Engine Research facilities, Faculty of Science and Engineering, Queensland University of Technology, Brisbane, Queensland 4000, Australia; E-Mails: [email protected] (R.J.B.); [email protected] (G.A.A.); [email protected] (M.N.N.) 2 School of Marine and Tropical Biology, James Cook University, Townsville, Queensland 4811, Australia; E-Mail: [email protected] 3 Centre for Sustainable Fisheries and Aquaculture, James Cook University, Townsville, Queensland 4811, Australia 4 Centre for Biodiscovery and Molecular Development of Therapeutics, James Cook University, Townsville, Queensland 4811, Australia * Authors to whom correspondence should be addressed; E-Mails: [email protected] (M.A.I.); [email protected] (K.H.); Tel.: +61-4-2381-9870 (M.A.I.); +61-7-4781-5795 (K.H.). Received: 17 August 2013; in revise form: 27 September 2013 / Accepted: 15 October 2013 / Published: 29 October 2013 Abstract: Physical and chemical properties of biodiesel are influenced by structural features of the fatty acids, such as chain length, degree of unsaturation and branching of the carbon chain. This study investigated if microalgal fatty acid profiles are suitable for biodiesel characterization and species selection through Preference Ranking Organisation Method for Enrichment Evaluation (PROMETHEE) and Graphical Analysis for Interactive Assistance (GAIA) analysis.
    [Show full text]
  • Determination of Fatty Acid Methyl Esters Derived from Algae
    View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Cleveland-Marshall College of Law Cleveland State University EngagedScholarship@CSU Chemical & Biomedical Engineering Faculty Chemical & Biomedical Engineering Department Publications 5-2017 Determination of Fatty Acid Methyl Esters Derived from Algae Scenedesmus dimorphus Biomass by GC-MS with One-step Esterification of Free Fatty Acids and Transesterification of Glycerolipids Satya Girish Chandra Avula Cleveland State University Joanne M. Belovich Cleveland State University, [email protected] Yan Xu CFolevlloelawnd thi Stast ea Undni vaerddsitity,ion y.xu@cal wsorkuohios a.etdu: https://engagedscholarship.csuohio.edu/encbe_facpub Part of the Chemical Engineering Commons How does access to this work benefit oy u? Let us know! Publisher's Statement This is the accepted version of the following article: Avula, S. G. C.; Belovich, J. M.; Xu, Y., Determination of fatty acid methyl esters derived from algae Scenedesmus dimorphus biomass by GC–MS with one-step esterification of free fatty acids and transesterification of glycerolipids. Journal of Separation Science 2017, 40, (10), 2214-2227.], which has been published in final form at http://onlinelibrary.wiley.com/doi/10.1002/ jssc.201601336abstract;jsessionid=9C0A6FB5912FD46463D86076A610B8E8.f02t02 Original Citation Avula, S. G. C.; Belovich, J. M.; Xu, Y., Determination of fatty acid methyl esters derived from algae Scenedesmus dimorphus biomass by GC–MS with one-step esterification of free fatty acids and transesterification of glycerolipids. Journal of Separation Science 2017, 40, (10), 2214-2227. Repository Citation Avula, Satya Girish Chandra; Belovich, Joanne M.; and Xu, Yan, "Determination of Fatty Acid Methyl Esters Derived from Algae Scenedesmus dimorphus Biomass by GC-MS with One-step Esterification of Free Fatty Acids and Transesterification of Glycerolipids" (2017).
    [Show full text]
  • A Thesis Entitled the Production of Fatty Acid Methyl Esters in Lewis
    A Thesis entitled The Production of Fatty Acid Methyl Esters in Lewis Acidic Ionic Liquids by Patrick M. Bollin Submitted to the Graduate Faculty as partial fulfillment of the requirements for the Master of Science Degree in Chemical Engineering Dr. Sridhar Viamajala, Committee Chair Dr. Maria Coleman, Committee Member Dr. Sasidhar Varanasi, Committee Member Dr. Patricia R. Komuniecki, Dean College of Graduate Studies The University of Toledo December 2011 Copyright 2011, Patrick M. Bollin This document is copyrighted material. Under copyright law, no parts of this document may be reproduced without the expressed permission of the author. An Abstract of The Production of Fatty Acid Methyl Esters in Lewis Acidic Ionic Liquids by Patrick M. Bollin Submitted to the Graduate Faculty as partial fulfillment of the requirements for the Master of Science Degree in Chemical Engineering The University of Toledo December 2011 Biodiesel is a direct substitute for petroleum derived fules and can be utilized in diesel equipment with few or no modification (Ma, Hanna, 1999). Traditional sources for biodiesel include plant oils (such as soybean or canola) that are also important food sources; biodiesel derived from plants might therefore not result in substantial displacement of petroleum feedstocks. Algae may present itself as an alternate feed- stock for biodiesel production that does not compete with the vital land and water resources needed for traditional agriculture. However, the production of fuels from al- gae is currently economically unviable due to several technological hurdles, including availability of efficient methods of converting cellular lipids to biodiesel. The research described herein describes the in-situ transesterification of soy flour triglycerides (surrogate for algal biomass) with methanol to fatty acid methyl esters using a novel ionic liquid (IL) comprised of 1-Ethyl-3-methylimidazolium chloride (EMIMCl) and the metal halide AlCl3.
    [Show full text]
  • (FAME) Under Different Storage Conditions
    energies Article Functional Properties and Microbiological Stability of Fatty Acid Methyl Esters (FAME) under Different Storage Conditions Małgorzata Hawrot-Paw * , Adam Koniuszy , Paweł S˛edłak and Daria Se ´n Department of Renewable Energy Engineering, West Pomeranian University of Technology in Szczecin, Pawla VI 1, 71-459 Szczecin, Poland; [email protected] (A.K.); [email protected] (P.S.); [email protected] (D.S.) * Correspondence: [email protected] Received: 30 September 2020; Accepted: 26 October 2020; Published: 28 October 2020 Abstract: Biofuels used as biocomponents for transport fuels should meet quality requirements. Their properties have a significant impact on the proper functioning of the engine supply system and the wear of its components. Changes in the performance of biofuel functionality may already occur during storage. Therefore, the present study aimed to evaluate changes in selected rheological and tribological parameters of higher fatty acid esters depending on the time and method of their storage by considering different types of substrates used for their production. The presence of possible microbiological contamination, which may affect the examined parameters of biofuels, was also analyzed. The dynamic viscosity of the biofuels tested changed depending on the substrate used. The biofuel produced from waste oil had the highest viscosity. Tribological studies show that both the linear wear of samples and the friction moment were higher after the storage period. The acid number of the esters did not exceed the permissible value recommended by the standard. The type of raw material used for the production of biodiesel and the conditions of its storage affected biodeterioration, proved by the growth of microorganisms.
    [Show full text]
  • Fatty Acid Methyl Esters in B100 Biodiesel by Gas
    APPLICATION NOTE Gas Chromatography Authors Timothy Ruppel Timon Huybrighs PerkinElmer, Inc. Shelton, CT USA Introduction Fatty Acid Methyl Esters The production and consumption of biofuels continues to increase as more in B100 Biodiesel by attention is paid to the environment and the depletion of fossil-fuel resources. Gas Chromatography Biodiesel, a fuel from natural oils such as (Modified EN 14103) soybean oil, rapeseed oil or animal fats, is a substitute for petroleum-diesel fuel. The quality criteria for the production of biodiesel are specified in EN 14214. Within EN 14214, method EN 14103 specifies the fatty acid methyl ester (FAME) and linolenic acid methyl ester content (Figure 1), which is used to profile the vegetable or animal oil feedstock used in biodiesel production. EN 14103 calls for calibration of all FAME components by relative response to a single compound, methyl heptadecanoate. This requires the measurement of accurate weights for each sample and the addition of an internal standard. The range of FAMEs for which the method is intended lies between C14:0 and C24:1. This application note will discuss the analysis according to method EN 14103. In addition to the methodology specified in EN 14103, a simpler and more accurate method will be presented. The modified method uses commercially-available calibration and test mixtures for precise peak identification and quantitative accuracy, while streamlining the sample preparation and calculations. Reporting is based on area % of all components after the solvent – as a result, the sample weight does not impact the calculations. Figure 1. Linolenic acid. Experimental In order to determine the retention times of the fatty acid The FAME analysis is carried out with a split injection methyl esters, a FAME standard needs to be run.
    [Show full text]
  • SLB-IL111 for Fatty Acid Methyl Ester (FAME) Applications Michael D
    sigma-aldrich.com 595 North Harrison Road, Bellefonte, PA 16823-0048 USA Tel: (800) 247-6628 (814) 359-3441 Fax: (800) 447-3044 (814) 359-3044 Technical Report SLB-IL111 for Fatty Acid Methyl Ester (FAME) Applications Michael D. Buchanan, Katherine K. Stenerson, and Leonard M. Sidisky The extremely polar SLB™-IL111 column Derivatization of Fatty Acids to Methyl Esters exhibits the highest polarity of any GC GC can be used to analyze fatty acids, either as free fatty acids or as fatty phase, allowing it to resolve key cis/trans acid methyl esters. The primary reasons to analyze fatty acids as fatty acid fatty acid methyl ester (FAME) isomers that methyl esters include: cannot be resolved on other columns. It ● also provides an alternative selectivity for In their free, underivatized form, fatty acids may be diffi cult to analyze, FAME applications typically performed on because these highly polar compounds tend to form hydrogen bonds, highly polar cyanopropyl siloxane columns. leading to adsorption issues. Reducing their polarity may make them Its maximum temperature of 270 °C is very more amenable for analysis. impressive for such an extremely polar ● To distinguish between the very slight diff erences exhibited by column. The chromatograms shown here demonstrate the utility of the unsaturated fatty acids, the polar carboxyl functional groups must SLB-IL111 as a great column choice for the analysis of FAMEs. fi rst be neutralized. This then allows column chemistry to perform separations by degree of unsaturation, position of unsaturation, and even the cis vs. trans confi guration of unsaturation. Fatty Acid Chemistry The esterifi cation of fatty acids to FAMEs is performed using an alkylation The most commonly analyzed fatty acids consist of C4-C24+ derivatization reagent.
    [Show full text]
  • Biodiesel by Transesterification of Rapeseed Oil Using
    energies Article Biodiesel by Transesterification of Rapeseed Oil Using Ultrasound: A Kinetic Study of Base-Catalysed Reactions José María Encinar 1,* ID , Ana Pardal 2 ID , Nuria Sánchez 1 and Sergio Nogales 1 ID 1 Department of Chemical Engineering and Physical Chemistry, Extremadura University, Avenida de Elvas s/n., 06071 Badajoz, Spain; [email protected] (N.S.); [email protected] (S.N.) 2 Department of Applied Sciences and Technology, IP Beja, Rua Pedro Soares s/n., 7800 Beja, Portugal; [email protected] * Correspondence: [email protected]; Tel.: +34-924-289-672 Received: 27 July 2018; Accepted: 23 August 2018; Published: 25 August 2018 Abstract: The objective of this work was to study the acceleration that ultrasound causes in the rate of biodiesel transesterification reactions. The effect of different operating variables, such as ultrasound power, catalyst (KOH) concentration and methanol:oil molar ratio, was studied. The evolution of the process was followed by gas chromatography, determining the concentration of methyl esters at different reaction times. The biodiesel was characterized by its density, viscosity, saponification and iodine values, acidity index, water content, flash and combustion points, cetane index and cold filter plugging point (CFPP), according to EN 14214 standard. High methyl ester yield and fast reaction rates were obtained in short reaction times. Ultrasound power and catalyst concentration had a positive effect on the yield and the reaction rate. The methanol:oil molar ratio also increased the yield of the reaction, but negatively influenced the process rate. The reaction followed a pseudo-first order kinetic model and the rate constants at several temperatures were determined.
    [Show full text]