碱性离子液体催化菜籽油制备生物柴油的试验研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
能源是人类社会赖以生存和发展的重要物质基础。随着环境和能源双重压力的不断加大,发展可再生、环保的化石燃料的替代品已经成为世界各国的共识。生物柴油以其良好的性能而展现出来的巨大的潜力和广阔的市场前景逐渐成为人们关注的焦点。
     生物柴油的制备方法有直接混合法、微乳液法、高温热裂解法、酯交换法。而酯交换中的碱催化法因其反应条件温和,催化剂成本低,反应速度快,转化率高,是目前工业生产中使用较为广泛的一种方法。
     离子液体是指在室温或接近室温(<150℃)的条件下呈现液态的、完全由阴阳离子构成的物质。作为一种新型的环境友好溶剂和液体酸碱催化剂,具有其它溶剂和传统催化剂不具备的优点。由于其独特而优良的性能,它被认为是21世纪最有希望的绿色溶剂和催化剂之一,现已应用于催化反应、有机合成、分离科学以及电化学等诸多领域。
     本论文以实验室自制的碱性离子液体氢氧化—丁基三甲基咪唑([Bmim]OH)为催化剂,进行了菜籽油的酯交换反应、超声波辅助下的菜籽油酯交换反应,以及菜籽油的原料特性、菜籽油脂肪酸和菜籽油生物柴油的成份分析等相关试验研究。
     对于[Bmim]OH催化菜籽油的酯交换反应,通过单因素和正交试验的手段,详细研究了醇油摩尔比、反应温度、反应时间和离子液体用量对酯交换反应的影响及离子液体的稳定性。结果表明,在n(甲醇):n(菜籽油)=16:1、反应温度150℃、反应时间4h和催化剂用量为菜籽油质量6%的条件下,生物柴油收率可达96.2%,并且该离子液体的稳定性良好,循环使用五次催化性能没有明显降低。反应动力学的研究显示,该反应的反应级数为0.7075,活化能为43.94kJ/mol,指前因子为96056.32。该反应的动力学模型为-(dcA)/(dt)=96056.32e-(43.93)/(RT)C A0.7075。
     对于超声波辅助下的碱性离子液体[Bmim]OH催化菜籽油制备生物柴油,超声波频率59KHz时得到的最优反应条件是:超声波功率200W、反应温度90℃、反应时间1h、n(甲醇):n(菜籽油)=16:1和催化剂用量为菜籽油质量6%。该条件下,酯交换反应脂肪酸甲酯收率达到90.8%。
     超高效液相色谱测得的菜籽油生物柴油的主要成分为亚麻酸甲酯、亚油酸甲酯、油酸甲酯、芥酸甲酯。菜籽油生物柴油的主要成分是含有18个C的脂肪酸甲酯,其分子结构满足理想的柴油替代品的要求,是合格的燃料替代品。
Energy is an important material base of human society to exist and develop.With the dual increasing pressures of environment and energy, the development of renewable, environmente-friendly fuels to replace fossil fuels has become a world consensus. Biodiesel,for its good performance bring the huge potential and broad market prospects, becomes gradually the focus of attention.
     There are many methods for preparation of biodiesel, direct mixing method, micro-emulsion method, high-temperature thermal cracking method and transesterification. currently,The base catalyzed transesterification,for its mild reaction conditions, low cost of catalyst, fast reaction rate, and high conversion ratio, is one of more widely used methods in industrial.
     Ionic liquid is liquid under the room temperature or near room temperature (<150℃) and entirely composed of the anion and cation. As a new type of environment-friendly solvent and liquid catalyst, Ionic liquid has many unique advantages. Because of unique and excellent performance, it is considered to be one of the most promising green solvent and catalyst in the 21st century.It has been used in catalytic reaction, organic synthesis, separation science and electrochemical and other areas.
     In this paper, using a laboratory-made alkaline ionic liquid [Bmim] OH as catalyst for transesterification of rapeseed oil and ultrasound-assisted transesterification of rapeseed oil.The raw material characteristics of rapeseed oil,and rapeseed oil fatty acids and rapeseed biodiesel component analysis and other related study.
     Through a single factor and orthogonal tests, The author seriously study of many factors which are effect on transesterification, such as molar ratio between methanol to rapeseed oil, reaction temperature, reaction time and amount of ionic liquids, and the ionic liquid stability. The results showed that the optimum reaction conditions were:n(methanol):n(rapeseed oil)=16:1, reaction temperature150℃, reaction time 4h, dosage of catalyst 6% of rapeseed oil weight. Yield of biodiesel was 96.2%. The ionic liquid is stable and without decreasing,which repeatedly used for 5 times.Reaction kinetics studies have shown that the reaction order was 0.7075, the activation energy was 43.94 kJ/mol, preexponential factor was 96,056.32. The reaction kinetic model was.-(dcA)/(dt)=96056.32e-(43.93)/(RT)C A0.7075.
     Rapeseed biodiesel preparation under the ultrasound-assisted alkaline ionic liquid [Bmim] OH, we get the optimal reaction conditions were:ultrasonic frequency 59KHz, ultrasonic power 200W, reaction temperature 90℃, reaction time 1h, n (methanol):n (rapeseed oil)=16:1 and the amount of catalyst for the quality of rapeseed oil 6%. Under these conditions, biodiesel yield was 90.8%.
     The main component of rapeseed oil biodiesel is grease containing C18, its molecular structure meets the requirements of diesel substitute, is an ideal substitute for diesel oil. After measuring rapeseed oil biodiesel with UPLC, its main components were flax acid methyl ester, linoleic acid methyl ester, oil acid methyl ester, and mustard methyl.
引文
[1]王永红.餐饮废油制取生物柴油的研究:[硕士学位论文].天津:天津大学,2004.
    [2]李昌珠,张良波,欧日明,等.生物柴油发展战略研究[J].湖南林业科技,2005,32(6):6-8.
    [3]武彤,张炳烛,李景印,等.生物柴油的研究及发展现状[J].河北工业科技,2008,25(3):156-161.
    [4]Meher L C, Sagar D V, Naik S N. Technical aspects of biodiesel production by transesterification-a review[J].Renewable and Sustainable Energy Reviews,2006,10: 248-268.
    [5]郭卫军,闵恩泽.发展我国生物柴油的初探[J].石油学报,2003,19(2):1-6.
    [6]朱行.植物油制成生物柴油[J].粮食与油脂,2001,(5):50-51.
    [7]李昌珠,蒋丽娟,程树棋.生物柴油——绿色能源[M].北京:化学工业出版社,2005.
    [8]Demirbas A. Biodiesel production via non-catalytic SCF method and biodiesel fuel characteristics[J]. Enery Conversion and Management.2006,47:2271-2282.
    [9]张震宇,方利国.国内外生物柴油技术的研究进展[J].广东化工,2007,34(9):12-16.
    [10]王文魁,包宗宏,王本庭,等.酯交换法生产生物柴油研究进展[J].拖拉机与农用运输车,2008,35(1):3-5.
    [11]黄庆德,黄凤洪,郭萍梅.生物柴油生产技术及其开发意义[J].粮食与油脂,2002,9:8-10.
    [12]薄向利,夏代宽,邱添.超临界流体技术制备生物柴油的研究进展[J].化工时刊,2005,19(12):32-37.
    [13]Freedman B, Pryde E H, Mounts T L. Variables Affecting the Yields of Fatty Esters from Transesterified Vegetable Oils [J].Jaocs,1984,61:1638-1643.
    [14]A.S.Ramadhas, S.Jayaraj,C. Muraleedharan.Biodiesel production from high FFA rubber seed oil[J].Fuel,2005,84:335-340.
    [15]Siti Zullaikah,Chao-chin Lai. A two-step acid-catalyzed process for the production of biodiesel from rice bran oil[J].Bioresource Technology,2005,96:1889-1896.
    [16]林华超.一种生物柴油的生产方法[P].CN:1374370A,2002.
    [17]Satoshi F, Hiromim, Kazushia. Biodiesel Fuel Production with Solid Superacid Catalysis in Fixed Bed Reactor under Atomspheric Pressure [J].Catalysis Communications,2004,5: 721-723.
    [18]王督,苏有勇,王华,等.S04 2--ZrO2固体超强酸催化高酸值原料降酸的研究[J].2009全国生物质能源大会会议论文集,2009,265-270.
    [19]Sanjib kumar Karmee, An ju Chadha. Preparation of biodiesel from crude oil of Pongamia pinnata [J]. Bioresource Technology,2005,96:1425-1429.
    [20]宋吉彬,银建中,张礼鸣,等.碱催化法制备生物柴油工艺研究[J].化工装备技术,2007,28(4):24-26.
    [21]Tinja C, Siegfried P, et al. Biodiesel transesterfication of biological oils with liquid catalysts: Thermodynamic properties oil-methanol-amine[J]. Industrial&Engineering Chemistry.2005, 44(12):9593-9541.
    [22]徐娟,包桂蓉,王华.多相催化剂用于制备生物柴油的研究进展[J].工业加热,2007,6(36):1-4.
    [23]Hak-Joo Kim,Kang Bo-Seung,Kim Min-Ju,et a.Transesterification of Vegetable Oil to Biodiesel Using Heterogeneous Base Catalyst[J].Catalysis Today 2004,93-95:315-320.
    [24]王督,苏有勇,王华,等.Ba02催化菜籽油酯交换制备生物柴油的研究[J].2009全国生物质能源大会会议论文集,2009,205-210.
    [25]Naomi Shibasaki-Kitakawa, Hiroki Honda, Homare Kuribayashi, et al. Biodiesel production using anionic ion-exchange resin as heterogeneous catalyst [J]. Bioresoun Technology,2007, 98(2):416-421.
    [26]Corma A, Iborra S, Miquel S, et al. Catalysts for the production of fine chemicals:production of food emulsifiers,monoglycerides,by glycerolysis of fats with solid base catalysts [J].Journal of Catalysis,1998,173(1):315-321.
    [27]Saka S, Kusdiana D. Biodiesel fuel from rapeseed oil as prepared in Supercritical methanol [J].Fuel,2001,80:225-231.
    [28]Sake S, Kusidiana D. Two-step preparation for catalyst-free biodiesel fuel production[J].Appl Biochem Biotechnol,2004,(115):789-792.
    [29]Eiji M, Shiro S. Kinetics of hydrolysis and methyl esterification for hiodiesel production in two-step supercritical methanol process[J].Fuel,2006,(85):2479-2483.
    [30]孙世尧,王连鸳.超临界甲醇法制备生物柴油的研究现状[J].精细石油化工,2006,23(1):53-57.
    [31]Tateno T,Nilhama-shi E,Sakaki T et al. Process for producing fatty acid esters and Fuels comprising fatty acid ester [P]. CN:1126011,2001.
    [32]Soumanou M M,Bornscheuer U T. Improvement in lipase-catalyzed synthesis of fatty acid methyl esters from sunflower oil [J]. Enzyme and Microbial Technology,2003,33:97-103.
    [33]罗贵民主编,酶工程[M].北京:化学工业出版社,2002.
    [34]蔡志强,邬国英,林西平,等.固定化脂酶催化合成生物柴油的研究[J].中国油脂,2004,29(8):29-33.
    [35]徐圆圆,杜伟,刘德华.非水相脂肪酶催化大豆油脂合成生物柴油的研究[J].现代化工,2003,23:167-169.
    [36]Shimada Y J,Watanbe Y M,Samukawa T,et al. Conversion of vegetable oil to biodiesel using immobilized candida antarctica lipase [J]. Biosci.Bioeng.1999,76(7):789-792.
    [37]李汝雄,王建基.离子液体的合成与应用[J].化学试剂,2001,23(4):211-215.
    [38]Frederique R.Abreu, Melquizedeque B.Alves, et al. New multi-phase catalytic systems based on tin compounds active for vegetable oil transesterificaton reaction [J].Journal of Molecular Catalysis A:Chemical,2005,227:263-267.
    [39]Sung Ho Ha, Mai Ngoc Lan, Sang Hyun Lee, etal. Lipase-catalyzed biodiesel production from soybean oil in ionic liquids [J].Enzyme and Microbial Technology,2007,41:480-483.
    [40]吴芹,陈和,韩明汉等.高活性离子液体催化棉籽油酯交换制备生物柴油[J].催化学报,2006,27(4):294-296.
    [41]吴芹,陈和,韩明汉等.B酸离子液体催化棉籽油酯交换制备生物柴油[J].石油化工,2006,35(6):583-586.
    [42]易伍浪,朝明汉,吴芹等.]Bronsted酸离子液体催化废油脂制备生物柴油[J].过程工程学报,2007,7(6):1144-148.
    [43]张磊,于世涛,刘福胜,等.离子液体催化大豆油制备生物柴油[J].工业催化,2007,15(7):34-37.
    [44]王文魁.包宗宏.氯铝酸离子液体催化大豆油制备生物柴油[J].中国油脂,2007,32(9):51-53.
    [45]Shay E G (1993). Diesel fuel from vegetable oils:status and opportunities[J].Biomass and Bio-energy. (4).227-242.
    [46]Karaosmanoglu F,et.al,Biodiesel from Rapeseed Oil of turkish as An Alternative fules[J].Appl.Biochem and Biotech,1996,61(6):151-164.
    [47]谭天伟,王芳等.生物柴油的生产和应用[J].现代化工.2002,22(2).4-6.
    [48]Biodiesel Magazine,2006,10:86-90.
    [49]闵恩泽,姚志龙.近年生物柴油产业的发展——特色、困境和对策[J].化学进展,2007,19(7):1050-1059.
    [50]夏铭.固体碱催化酯交换反应合成生物柴油研究:[硕士学位论文].南京:南京林业大学,2007.
    [51]蒋剑春,杨凯华,聂小安.生物柴油的研究与应用[J].能源研究与利用,2004,5:22-25.
    [52]Martini W, Schell J. Plant Oils as Fuels:Present State of Science and Future Development[M]. New York:Springer Verlag Berin Heideberg.1998.
    [53]周良虹,黄亚晶.国外生物柴油产业与应用状况[J].可再生能源,2005,4:62-65.
    [54]ShimadaY, WatanabeY, etal. Conversion of Vegetable Oil to Biodiesel Using Immobilized Candida Antarctica Lipase[J]. JAOCS,1999,76:789-793.
    [55]韩德奇,袁旦,王尽涛,刘慧丽.生物柴油的现状与发展前景[J].石油化工技术经济,2002,4:32-37.
    [56]吴谋成.生物柴油[M].北京:化学工业出版社,2008.
    [57]孙毅刚.生物柴油的制取与应用前景分析[J].四川理工学院学报(自然科学版),2005,18(3):55-57.
    [58]包伟良,王治明.离子液体的研究现状与发展趋势[J].中国科协第143次青年科学家论坛——离子液体与绿色化学,2007,3-9.
    [59]乐长高.离子液体及其子有机合成反应中的应用研究[M].上海:华东理工大学出版社,2007.
    [60]李榕.碱性离子液体的合成与应用:[硕士学位论文].广东:华南理工大学,2007.
    [61]Fannin A A, Floreani D A, etal. Properties of 1,3-dialkylimidazolum chloride-aluminum chloride ionic liquids:Phase transitions, densities, electrical conductivities, and viscosities[J]. Phy.Chem.,1984,88:2614-2621.
    [62]Bonhote P, Dias A P, etal. Hydrophobic highly conductive ambient temperature molten salts [J]. Inorg, Chem.,1996,35:1168-1178.
    [63]Gale R J, Gilbert B P, Osteryoung RA. [J]. Inorg Chem,1978,17(10):2728-2732.
    [64]Wilkes J S, Zaworotko M J. Air and water stable 1-ethy-3-methylimidazolium based ionic Liquid[J]. Chem. Soc.,Chem.Commun.,1992 (13):965-967.
    [65]Davis Jr. J.H,Forrester K.J.Thiazolium-ion based Orangic Ionic Liqulds(OILs), novel OILs which Promoe the Benzoin Condensation [J].Tetrahedron lett.1999,40(11):1621-1262.
    [66]Davis J H. Chem.Lett.,2004,33 (9):1072-1077.
    [67]刘伟山,陶国宏,何玲等.功能化的离子液体:手性离子液体的合成与应用[J].有机化学,2006,26(8):1031-1038.
    [68]Jared L. Anderson, Daniel W., Armstrong.[J]. Analytical Chem,2003,75(18):4851-4858.
    [69]李雪辉,郑宾国,赵荆感.离子液体催化丙烯睛氯化合成2,3-二氯丙睛[J].催化学报,2006,27(2):106-108.
    [70]乔煜,邓友全.超强酸性室温离子液体反应介质中烷烃羰化研究[J].化学学报,2002,60(8):1520-1523.
    [71]Namboodiri W. Varma R.S.Novel approach to the synthesis of AZT 5,-O-hydrogenphospholipids[J].Tetrahedron Letter.2002,43:5281—5383.
    [72]李向召,江琦.固体碱催化剂研究进展[J].天然气化工,2005,30(1):42-48.
    [73]Mehnert C P, Dispenziere N C, Cook R A. Preparation of C9-aldehyde via aldol condensation reactions in ionic liquid media[J]. Chem. Commun,2002,2(15):1610-1611.
    [74]Brindaban C. Ranu, Subhash Banerjee. Ionic Liquids Catalyst and Reaction Medium. The Dramatic Influence of a Task-Sepcific Ionic Liqui, [BMIM]OH in Micheal Addention of Active Methylene Comopnuds to Cojnugated Ketones, Carboxylic Eestrs, and Nitriles[J]. Org. Lett.,2005,7(14):3049-3052.
    [75]Ranu, B. C.Jana, R. Ionic liquid as catalyst and reaction medium-a simple, efficient and green procedure for Knoevenagel condensation of aliphatic and aromatic carbonyl compounds using a task-specific basic ionic liquid. Eur. J. Org. Chem.2006,3767-3770.
    [76]Xu J M, Wu W B, Liu B K, Lin X F, Basic Ionic Liquid as Catalysis and Reaction Medium:A Novel and Green Protocol for the Markovnikov Addition of N-heterocycles to Vinyl Esters using a Task-Specific Ionic Liquid, [BmIm]OH, J. Org. Chem.,2006,71(10):3991-3993.
    [77]巩凯,方东,施群荣,刘祖亮.碱性功能化离子液体催化Mannich反应研究.含能材料,2008,16(2):121-124.
    [78]李娟,孙辉,蔡晓晨,戴立益.碱性离子液体[Bmimm]OH在Knoevenagel反应和Perkin反应中的应用.有机化学,2007,27(10):1296-1299.
    [79]Pierre Bonhote,Ana-Paula Dias,Nicholas Papageorgiou.et al. Hydrophobic, highly conductive ambient temperature molten salts[J]. Inorg. Chem.,1996,35:1168-1169.
    [80]李桂华,钱向明,毕艳兰.油料油脂检验与分析[M].北京:化学工业出版社,2006,3:101-103.
    [81]李一哲,包桂蓉,王华.超高效液相色谱法测定生物柴油中的11种脂肪酸及脂肪酸甲酯[J].色谱,2008,26(4):494-498.
    [82]刘文卿.实验设计[M].清华大学出版社,2005.2:103-133.
    [83]李法社.小桐子生物柴油制备的试验研究:[硕士学位论文].云南:昆明理工大学,2008.
    [84]Ernesto Emmanuel Borrero Quintana. Optimization studies for the alkaline transesterifieation biodiesel reaction using ultrasound mixing [D]. Mayaguez:University of Puerto Rico Mayaguez Campus,2002.
    [85]周泉城,王飞.超声波制备生物柴油技术的研究进展[J].可再生能能源,2009,27(1)47-51.
    [86]毕良武,赵振东等.超声波技术在生物质资源加工领域的应用研究进展[J].林产化学与工业,2007,27(增刊):138-142.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700