用户名: 密码: 验证码:
离子液体中脂肪酶催化桐油合成生物柴油的研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
生物柴油以其可再生、环境友好等特性得到公众的认可。生物柴油可以通过物理法、化学法和生物法等方法制得,尤其是生物法,生物酶法合成生物柴油具有反应条件温和,零排放等优点,是最具发展前景的方法。本文采用脂肪酶催化酯交换制备生物柴油,生物酶法的关键是生物催化剂的催化活性和稳定性。
     通过两步法制得的离子液体作为反应的溶剂,通过红外光谱和核磁共振对合成的离子液体进行了表征,结果表明合成的液体就是目标离子液体[BMIM]PF_6;在合成的离子液体中对脂肪酶的耐受性进行了测定,结果固定化脂肪酶在40℃的离子液体中培养24h,酶的活性仍能保持在70%以上。
     本文主要研究了用桐油转化生物柴油,分析评价了桐油的理化性质,陕南桐油的磷脂含量49.65 mg/kg,酸值3.66 mgKOH/g,过氧化值4.43 mol/L,皂化值191.8 mgKOH/g,碘值166.7 g/100g,粘度(27℃)197.3 mpa.s。计算得到桐油平均分子量是894.55g/mol。通过对桐油的色谱分析得出桐油的主要成分为桐酸、亚油酸、油酸、其中桐酸相对含量为78.04%,其次是亚油酸和油酸分别为11.557%和4.167%。
     原料油的预处理实验中,对桐油水化脱胶实验进行了优化,最终得到的优化条件为:水化时间21min,加水量3.9%,水化温度73℃,使桐油中磷脂的含量从最初的49.65mg/Kg到19.52 mg/kg,使得磷脂对反应的影响降到最低。
     以离子液体[BMIM]PF_6为溶剂,在离子液体中合成生物柴油。通过正交实验对在离子液体中合成生物柴油的实验条件进行了优化,最优条件:醇油比为3:1,加酶量为油重的15%,反应温度为45℃,反应24小时。在此条件下,实际实验测得的实际甲酯转化率为76.3%。在反应体系中对脂肪酶的稳定性进行了研究,研究表明在以[BMIM]PF_6为溶剂的反应体系中,经过6次重复使用脂肪酸甲酯转化率仍能维持在50%以上。
People recognize biodiesel as it reproducible and environmental friendly.Biodiesel can be synthesized by physical method or chemical method or biological method.Especially the biological method,the biological enzyme synthesis biodiesel has the response condition to be temperate,merit and so on non-pollutant emission,was the recent years research hot spot.It is the most promising method in the various methods for biodiesel production.In this paper,the biological enzyme synthesis biodiesel has been chosen,and its key point is the activity and stability of the biological enzyme.
     Ionic Liquid[BMIM]PF_6 was chosen as the solvent of the reaction,which was synthesized through a typical two-step way.The FT-IR and MRI were used to make sure that we get the[BMIM]PF_6.The stability of the lipase in[BMIM]PF_6 was investigated,after 24h suspended in[BMIM]PF_6 at 40℃,the lipase retained approximately above 70%of it original activity.
     The aim of this research is to study the preparation method of biodiesel fules from Tung oil.The character of Tung oil were analyzed,the results show that phosphorous content was 49.65 mg/Kg,acid value was 3.66 mgKOH/g,peroxidate value was 4.43 mol/L, saponification value was 191.8 mgKOH/g,iodine value was 166.7 g/100g,viscosity value(27℃) was 197.3 mpa.s,the average molecular weight of Tung oil was 894.55g/mol. GC methods were used to analysis of Tung oil,the main compositions were elaeostearic acid(78.04%),octadecadienoic acid(11.557%),and octadecenoic acid(4.167%)
     In the study of the pretreatment of raw oil,hydration degumming was accepted to optimize the condition of the experiment.The optimization of hydration degumming were: water 3.9%,temperature of 73℃,and the reaction time of 21min,leading to the decrease of phosphorous content from 49.65 mg/Kg to 19.52 mg/kg.After hydration degumming disadvantage of the phosphorus can reduce to minimum.
     We Prepare biodiesel from Tung oil with ionic liquid[BMIM]PF_6,By the orthogonal test of the Tung oil transesterification reaction with[BMIM]PF_6,the optimum conditions for biodiesel preparation were:molar ratio of Tung oil to methanol 3:1,15%w/w(oil) of catalysts, reaction temperature 45℃,reaction time 24h,with the average yield of 76.3%.The stability of the lipase in the reaction was investigated,after 6 times use,the conversion of the fatty acid methyl retained approximately above 50%of it original rate.
引文
[1]谭天伟,王芳,邓立等.生物柴油的生产和应用[J].现代化工,2002,22(2):4-6
    [2]王亮军.中国能源战略及规划要点浅谈.科技情报开发与经济[J].2006,16(6):86-88
    [3]龚志民.基于我国能源缺口模型的能源可持续发展探悉.能源技术与管理[J].2006,1:113-115
    [4]Jose M E,Juan F G,Eduardo S.Preparation and properties of biodiesei from Canary[J].Carbucles Cheese,1999,(38):93-95
    [5]韩德奇,袁旦,王尽涛,刘惠丽.生物柴油的现状与发展前景[J].石油化工技术经济,2004,4(18):32-37
    [6]钱伯章.发展前景广阔的生物柴油产业[J].能源技术,2003:(1)14-16
    [7]袁银南,江清阳,孙平.柴油机燃用生物柴油的排放特性研究[J].内燃机学报,2003,6:423-427
    [8]Dorado M P,Ballesterosb E,Amale J M.Exhaust emissions from a diesel engine fueled with transesterised waste olive oil[J].Fuel,2003,82:1311-1315
    [9]葛蕴珊,信建民,吴思进.增压柴油机燃用生物柴油的排放特性研究[J].燃烧科学与技术,2004,2:125-129
    [10]王忠,袁银南,历宝录等.生物柴油得排放特性实验研究[J].农业工学报,2005,21(7):77-80
    [11]McCormick R L,Graboski M S,Alleman T L,et al.Impact of biodiesel source material and chemical structure on emissions of criteria pollutants from a heavy-duty engine[J].Environ Sci Technol,2001,35(9):1742-1747
    [12]Adams C,Peters J F,Rand,et al.Investigation of soybean oil as a diesel fuel extender[J].JAOCS,1983,60(8):1574-1579
    [13]Ziejewski M,Kaufman K R,Pratt G L.Vegetable Oils as Diesel Fuel[C].Seminar Ⅱ,Northern Regional Research Center,Peoria,Illinois,1983
    [14]Goering C E,Fry B.Engine durability screening test of a diesel oil/soy oil/alcohol microemulsion fuel[J].JAPCS,1984,61(8):1627-1632
    [15]Ziejewski M,Kaufman K R,Pratt G L.Vegetable Oils as Diesel Fuel[C].Seminar Ⅱ,Northern Regional Research Center,Peoria,Illinois,1983
    [16]T.Neuma de Castro Dantas,A.C.da Silva,A.A.D.Neto.New microemulsion systems using diesel and vegetable oils[J].Fuel,2001,80(8):75-81
    [17]宁正祥,赵谋明.食品生物化学[M].广州:华南理工大学出版社,1995,22-23
    [18]Ma F.R.,Hanna M.A.Biodiesel Production:a review[J].Bioresource Technology,1999,70:1-15
    [19]Schwab A.W,Dykstra G.J.,Selke E.,Sorenson S.C.,Pryde E.H.Diesel fuel From thermal decomposition of soybean oil[J].Journal of the American Oil Chemists Society,1988,65:1781-1786
    [20]Zhang Y.,Dube M.A.,McLean D.D.,Kates M.Biodiesel Production from waste cookingoil:1.Process design and technological assessment[J].Bioresource Technology,2003,89:1-16
    [21]Pioch.Biofuels from catalytic of tropical vegetable oil[J].Oleagineux,1993,48:289-291
    [22]王一平,翟怡,张金利.生物柴油制备方法研究进展[J].化工进展,2003,22(1):8-11
    [23]D.Kusdiana,S.Saka.Kinetics of transesterification in rapeseedoil to biodiesel fuel as treated in supercritical methanol[J].Fuel,2001,80:693-698
    [24]S.Saka,D.Kusdiana.Biodiesel fuel from rapeseed oil as Prepared in supercritical methanol[J].Fuel,2001,80:225-231
    [25]Freedman B.,Pryde E.H.,Mounts T.L.Variables affecting the yields of fatty esters from transesterified vegetable oils[J].Journal of the American oil Chemists Society,1984,61:1638-1643
    [26]Freedman B.,Butterfield R.O.,Pryde E.H.Transesterification kinetics of soybean oil[J].Journal of the American Oil Chemists Soeiety,1986,63:1375-1380
    [27]Aleantara R.,Amores J.,Canoira L.,et al.Catalytic Produetion of biodiesel from soybean oil,used frying oil and tallow[J].Biomass and Bioenergy,2000,18:515-527
    [28]盛梅,李为民,部国英.生物柴油研究进展[J].中国油脂,2003,28(4):66-70
    [29]Yasuhisa A,Hideki F,Yuji S,et al.Biofuei production process by novel biocatalysts[J].Journal of Molecular Catalysis,2002,17(3-5):111
    [30]郭璇,贺华阳,王涛等.超临界流体技术制备生物柴油[J].现代化工,2003,23:15-18
    [31]Yuichiro W,Dadan K,Shiro S.Biodiesel fuel from vegetable oil by various supercritical alcohols[J].Applied Biochemistry and Biotechnoiogy,2004,115(1-3):793-802
    [32]Saka S,Kusdiana D.Biodiesel fuel from rapeseed oil as prepared in supercritical methanol[J].Fuel,2001,88(2):225-231
    [33]Manmoru.Production of biodiesel fuel from triglycerides and alchol using immobilized lipase[J].Journal of Molecular Catalyst B:Enzymatic,2001,16:53-58
    [34]Kazuhiro Bana,Masaru Kaiedab.Whole cell biocatalyst of biodiesel fuel Production utilizeing phizopus oryzae cells immobilized within biomass support particles[J].Biochemical Engineering Journal,2001,8:39-43
    [35]Borgstrom B.Erlnason C.Pancreas lipase and colipase,Interaction and effect of bile salt and other detergents[J].Eur.J.Bioehem.1973,37:60-68
    [36]Kamini N R,lefuji H.Lipase Catalyzed Methanolysis of Vegetable Oil in Aqueous Medium by Cryptococcus spp S-2[J].Process Biochemistry,2001,37(4):405-410
    [37]P.Vanessa Lara,Enoch Y.Park.Potential application of waste activated bleaching earth on the Production of fatty acid aikyl esters using Candida cylindracea lipase in organic solvent system[J].Enzyme and Microbial Technology,2004,34:270-277
    [38]章亭洲,杨立荣,朱自强.脂肪酶改性对其在有机相中催化特性的影响[J].浙江大学学报,2001.27(3):237-243
    [39](o|¨)znur K(o|¨)se,Melek T(u|¨)ter,Ayse Aksoy H.Immobilized Candida Antarctica lipase-catalyzed alcoholysis of cotton seed oil in a solvent-free medium.Bioresource Technology,2002,83(2):125-129
    [40]Yuji Shimada,Yomi Watanabe,Akio Ugiharal.Enzymatic alcoholysis for biodiesel fuel produetion and application of there action to oil Processing[J].Journal of Molecular Catalysis B:Enzymatic,2002,79(17):133-142
    [41]聂开立,王芳,邓利等.间歇及连续式固定化酶反应生产生物柴油[J].生物加工过程,2005,2,3(1):58-62
    [42]聂开立,王芳,谭天伟.固定酶法生产生物柴油[J].现代化工,2003,23(9):35-38
    [43]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
    [44]R J Niehols.The Challenge of Change in the Auto Industry:Why Altemative Fuel[J].J.Eng for Gas Thrbine.&power,1994,116(10):727
    [45]F Staat,et al.Vegetable oil Methyl Ester as a Diesel Substitute[J].Chem&Indus,1994,7(11):863
    [46]F Karaosmanoglu,et al.Biodiesel from Rapeseed oil of Turkish as An Alternative Fuels[J].Appl.Biochem.&Bioteeh,1996,61(6):151-164.
    [47]Mohamed M.,Soumanou,Uwe T.,Bornscheuer.Improvement in lipase-catalyzed synthesis of fatty acid methyl esters from sunflower oil[J].Enzyme and Microbial Technology,2003,33(1):97-103
    [48]Boocock D G B,Konar S K,Vinnie Mao.Fast one-phase oil-rich processes for the preparation of vegetable oil methyl esters[J].Biomass and Bioenergy,1996,11(1):43-50
    [49]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
    [50]Hirao M,Sugmoto H.,Ohno H.Novel Room-tmperature Molten Salts by Neutralization of Amines,J.Electro.Chem.Soc.,2000,147(11):4168-4172
    [51]赵敏,王锦堂.离子液体中间体的合成研究,化工时刊,2004,18(7):22-23
    [52]Dzyuba Sergei V.,Bartsch Richard A.,Efficent Synthdsis of 1-Alkyl(aralkyl)-3-methyl(ethyl)imidazolium Halides:Precursors for Room-temperautre Ionic liquids[J].Heterocyclic Chem.,2001,38:265-268
    [53]Schofer S H,Kaftzik N,Wassercheid P,et al.Enzyme catalysis in ionic liquids:Lipase catalysed kinetic resolution of 1-phenylet hanol with improved enantioselectivity[J].Chem Commun,2001,425-426
    [54]Itoh T,Akasaki E,Nishimura Y.Efficient lipase-catalyzed enantioselective acylation under reduced pressure conditions in an ionic liquid solvent system[J].Chem Lett,2002,31(2):154-155
    [55]Kim K W,Songb,Choim Y,et al.Biocatalysis in ionic liquids:Markedly enhanced enantioselectivity of lipase[J].Org Lett,2001,3(10):1507-1509
    [56]Joel L.Kaar,Anita M.Jesionowski,Jason A.Berberich,et al.Impact of Ionic Liquids Physical Properties on Lipase Activity and Stability[J].Journal of the American Chemical Society,2003,125(14):4125-4131
    [57]郭晓熹.国际生物柴油发展状况[J].中国科技财富.2006,(z1):96-97
    [58]倪蓓.生物柴油欧关发展动态及在我国的前景[J].当代石油石化,2005,13(06):21-27
    [59]朱行.植物油制成生物柴油[J].粮食与油脂,2001,30(5):50
    [60]苏畅,赵崇峰,岳莉等.生物柴油技术的进展[J].当代化工,2004,33(2):79-82
    [61]Dieter Boekey.Biodiesel produetion and marketing in Germany[J].UFOP,Germany,2002
    [62]朱建良,张冠杰.生物柴油研究生产现状及发展趋势[J].化工时刊,2004(1):23-28
    [63]蒋剑春,杨凯华,聂小安等.生物柴油的研究与应用[J].新能源与新材料,2004(5):22-25
    [64]罗明典,科技日报,2001,10-22
    [65]谭天伟,王芳,邓利等.能源生物技术[J].生物加工过程,2003(5):1-1
    [66]冀星,王璇.世界各国生物柴油应用情况[J].国际化工信息,2002(9):1-4
    [67]李永善,于佑世.大有作为的“绿色化工”——未来的可再生柴油[J].灾害学,2002,17(2):54-59
    [68]朱明.生物柴油的现在与未来(上)[J].中国石油与化工经济分析,2006(16):41-45
    [69]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(122):62-67
    [70]于文景,于平.油脂制取加工技术、工艺流程、质量检测与生产管理、包装储藏实务全[M],北京:金版电子出版公司,2000:1308-1373,1412-1463
    [71]GB/T 5537-1985,植物油脂检验磷脂测定法[S].国家标准局,1986
    [72]GB/T 5530-1998,动植物油脂 酸价和酸度的测定[S].国家技术质量监督局,1998
    [73]GB/T 5538-1995,油脂过氧化值测定[S].国家技术质量监督局,1996
    [74]GB/T 5534-1995,动植物油脂皂化值的测定[S].国家技术质量监督局,1996
    [75]GB/T 5532-1995,植物油碘价测定[S].国家技术质量监督局,1996
    [76]GB/T 5528-1995,植物油脂水分及挥发物含量测定[S].国家技术质量监督局,1996
    [77]Tsurahide C,Tkaaki T.Process for preoaring dialkyl carbonates[M].US Patent,1994,553-649
    [78]KRAGL U,ECKSTEIN M,KAFTZIK N.Enzyme catalysis in ionic liquids[J].Biotechnology,2002,13:565-571.
    [79]LOU W,ZONG M,WU H,et al.Recent progress on biocatalysis and biot ransformations in ionic liquids[J].Chin J ChemEng,2004,12(4):543-549.
    [80]金学勇,邸学进,张乃强.室温离子液体的制备、性能及应用[J],滨州师专学报,2002,18(4):77-80
    [81]张玉芬,乔聪震,张金吕,李成岳.离子液体-环境友好的溶剂和催化剂[J].化学反应工程与工艺2003,19(2):164-171
    [82]赵东滨,寇元.室温离子液体:合成性质及应用[J],大学化学,2002,17(1):42-46
    [83]Xu D Q,Liu B Y,Luo S P.A novel and eco-friendly method for the preparation of ionic liquids[J].Synthesis-Stuttgart,2003(17):2626-2628
    [84]Huddleston J G,Visser A E,Reichert W M,Characterization and comparison of hydrophobic room temperature ionic liquids incorporating the imidazolium cation[J].Green Chenistry,2001,3:156-164
    [85]Clark S J,Wagner L,Schrock M D.Methyl and ethyl esters as renewable fuels for diesel engines.[J].Am.Chem.Soc,1984,61(10):1632-1638
    [86]李世中.桐油综合开发应用前景广阔[J].经济林研究,1997,15(4):71-72
    [87]Yomi Watanabe,Yuji Shimada,Akio Sugihara.Conversion of Degummed Soyben oil to Biodiesel with Immobilized Candida Antarctica Lipase[J].Journal of Molecula CatalysisB:Enzymatic,2002,17:151-155
    [88]李泽波,杜伟,刘德华.生物柴油制备过程中磷脂及水分含量对脂肪酶的影响[J].化工学报,2007,58(1):233-237
    [89]Ma F,Hanna M A.Biodiesel production:a review.Bioresource Technology,1999,70(1):1-15
    [90]谷克仁.水化脱胶工艺条件对大豆磷脂及油品质量的影响[J].郑州粮食学院学报,1994, 15(4):87-88
    [91]钟海雁,张余权.茶油水化脱胶工艺研究[J].经济林研究,2004,22(1):29-31
    [92]陈永楠.油脂生产技术[M].北京:化学工业出版社,1993.340
    [93]List G.R.,Avellaneda J.M.Effect of Degumming Conditions on Removal and Quality of Soybean Lecithin[J].JAOCS,1981,58:892
    [94]List G.R.,Avellaned,Mounts T.L.Refining of oils and fats for edible purposes[J].JAOCS,1981(10):892
    [95]何东平,油脂精炼与加工工艺学[M],北京:化学工业出版社,2005.4:251,327-328
    [96]JAIN N,KUMAR A,CHAU HAN S,et al.Chemical and biochemical transformations in ionic liquids [J].Tet rahedron,2005,61:1015-1060
    [97]Hideki Fukuda,Akihiko Kond,Hidei Noda.Biodiesel fuel production by transestedfication of oil[J].Journal of Bioscience and Bioengineering,2001,92(5):405-416
    [98]Masaru Kaieda,Taiehi Samukawa,Akihiko Kondo,et al.Effect of methanol and water contents on production of biodiesel fuel from plant oil catalyzed by various lipases in a solvent-free system[J].Journal of Bioscience and Bioengineering,2001,91(1):12-15
    [99]舍珠花,刘大川,潭蓓玉.麻疯树籽油甲酯化工艺的研究[J].中国油脂,2005,30(9):34-36.

© 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