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针对废弃油脂品质差,酸值高,难于采用传统的碱催化酯交换技术加工生产生物柴油,中国石化石油化工科学研究院开展了超/近临界甲醇介质中油脂溶解和反应的基础研究,相继解决了甲醇与油脂的互溶、降低反应条件,三脂肪酸甘油酯和游离脂肪酸的深度转化,以及产品质量等问题,成功开发了近临界醇解生物柴油技术(以下简称SRCA),于2009年建成了6万吨/年工业化示范装置,以酸化油和餐厨废油为原料,生产连续稳定,产品收率高且满足国家生物柴油质量标准(GB/T20828-2007).

参考文献

[1] Atabani A E;Silitong A S;Badruddin I A;Mahlia T M I Masjuki H H Mekhilef S .[J].Renewable & Sustainable Energy Reviews,2012,16:2070.
[2] Ahmad A L;Mat Yasin N H;Derek C J C;Lim J K .[J].Renewable & Sustainable Energy Reviews,2011,15:584.
[3] Lin L;Zhou C Sh;Vittayapadung S;Shen X Q Dong M D .[J].Applied Energy,2011,88:1020.
[4] Ragit, S. S.;Mohapatra, S. K.;Kundu, K.;Prashant Gill .Optimization of neem methyl ester from transesterification process and fuel characterization as a diesel substitute.[J].Biomass & Bioenergy,2011(3):1138-1144.
[5] 闵恩泽,杜泽学.我国生物柴油产业发展的探讨[J].中国工程科学,2010(02):11-15.
[6] 王瑞元.我国食用植物油的产需简况与学习贯彻《粮油加工业“十二五”发展规划》的建议[J].中国油脂,2012(06):1-5.
[7] Bankovic-Ilic I B;Stamenkovic O S;Veljkovic V B .[J].Renewable & Sustainable Energy Reviews,2012,16:3621.
[8] Shin H-Y;Lee S-H;Ryu J-H;Bae S-Y .[J].Journal of Supercritical Fluids,2012,61:134.
[9] Patil P;Deng Sh G;Rhodes J I;Lammers P J .[J].Fuel,2010,89:360.
[10] Math M C;Kumar S P;Chetty S V .[J].Energy Sustain Develop,2010,14:339.
[11] 鲁厚芳,史国强,刘颖颖,梁斌.生物柴油生产及性质研究进展[J].化工进展,2011(01):126-136.
[12] 王涛,谢文磊,李会,王迎宾.废餐饮油酯交换制备生物柴油研究进展[J].中国油脂,2010(05):48-52.
[13] Kawashima A;Matsubara K;Honda K .Development of heterogeneous base catalysts for biodiesel production[J].Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies,2008(9):3439-3443.
[14] Fukuda H;Hama S;Tamalampudi S;Noda H .[J].Trends in Biotechnology,2008,26(12):668.
[15] Sawangkeaw R;Bunyakiat K;Ngamprasertsith S .[J].Journal of Supercritical Fluids,2010,55:1.
[16] 杜泽学,王海京,江雨生,陈艳凤,闵恩泽.采用废弃油脂生产生物柴油的SRCA技术工业应用及其生命周期分析[J].石油学报(石油加工),2012(03):353-361.
[17] 王瑞元.国内外食用油市场的现状与发展趋势[J].中国油脂,2011(06):1-6.
[18] 姚志龙,闵恩泽.废弃食用油脂的危害与资源化利用[J].天然气工业,2010(05):123-128.
[19] 国家统计局 .2011年度统计公报[R].,2012-2-22.
[20] 李慧韫 .[D].天津:天津科技大学,2004.
[21] 吕凡,何品晶,邵立明.废食用油脂作生物柴油原料的可行性分析[J].环境污染治理技术与设备,2006(02):9-15.
[22] 张骥.日本生物柴油的发展[J].可再生能源,2009(01):117-120.
[23] 叶活动;丁以钿 .[P].CN 1 382 762,2002.
[24] 俞建秋;陈德裕;李俊雄;陈自端 .[P].CN 1 473 907,2004.
[25] 李娜,赵华,李会鹏,王福帅.固体酸催化生产生物柴油研究进展[J].工业催化,2012(04):7-10.
[26] Jacobson K;Gopinath R;Meher L C;Dalai A K .[J].Applied Catalysis B:Environmental,2008,85:86.
[27] Tan K T;Lee K T .[J].Renewable & Sustainable Energy Reviews,2011,15:2452.
[28] Tan K T;Lee K T;Mohamed A R .[J].Fuel Processing Technology,2011,92:1905.
[29] Tan K T;Lee K T;Mohamed A R .[J].Journal of Supercritical Fluids,2010,53:88.
[30] Cao W L;Han H W;Zhang J Ch .[J].Fuel,2005,84:347.
[31] Fauzi A H M;Amin N A S .[J].Renewable & Sustainable Energy Reviews,2012,16:5770.
[32] Tang Zh;Du Z X;Min E Z;Gao L Jiang T Han B X .[J].Fluid Phase Equilibria,2006,239:8.
[33] Shimoyama Y;Iwai Y;Jin B S;Hirayama T Arai Y .[J].Fluid Phase Equilibria,2007,257:217.
[34] Fang T;Shimoyama Y;Abeta T;Iwai Y Sasaki M Goto M .[J].Journal of Supercritical Fluids,2008,47:140.
[35] Shimoyama Y;Abeta T;Iwai Y .[J].Journal of Supercritical Fluids,2008,46:4.
[36] Shimoyama, Y;Abeta, T;Zhao, L;Iwai, Y .Measurement and calculation of vapor-liquid equilibria for methanol plus glycerol and ethanol plus glycerol systems at 493-573 K[J].Fluid Phase Equilibria,2009(1):64-69.
[37] Hegel P;Mahe G;Pereda S;Brignole EA .Phase transitions in a biodiesel reactor using Supercritical methanol[J].Industrial & Engineering Chemistry Research,2007(19):6360-6365.
[38] Hegel, P;Andreatta, A;Pereda, S;Bottini, S;Brignole, EA .High pressure phase equilibria of supercritical alcohols with triglycerides, fatty esters and cosolvents[J].Fluid Phase Equilibria,2008(1/2):31-37.
[39] Glisic S;Montoya O;Orlovic A;Skala D .[J].Journal of the Serbian Chemical Society,2007,72:13.
[40] Han H W;Cao W L;Zhang J Ch .[J].Process Biochemistry,2005,40:3148.
[41] Yin J Zh;Xiao M;Song J B .[J].Energy Conversion and Management,2008,49:908.
[42] Sawangkeaw R;Bunyakiata K;Ngamprasertsith S .[J].Journal of Supercritical Fluids,2010,55:1.
[43] Kusdiana D;Saka S .[J].Fuel,2001,80:693.
[44] Anitescu G;Deshpande A;Tavlarides L L .[J].Energy and Fuels,2008,22:1391.
[45] de Boer K;Bahri P A .[J].Biomass and Bioenergy,2011,35:983.
[46] Savage P E;Gopalan S;Mizan T I;Martino C J Brock E E .[J].AICHE Journal,1995,41:1723.
[47] 唐忠 .[D].北京:中国石化石油化工科学研究院,2005.
[48] Noureddini H.;Zhu D. .KINETICS OF TRANSESTERIFICATION OF SOYBEAN OIL[J].Journal of the American Oil Chemists' Society,1997(11):1457-1463.
[49] Madras G;Kolluru C;Kumar R .[J].Fuel,2004,83:2029.
[50] Rathore V;Madras G .[J].Fuel,2007,86:2650.
[51] He HY;Sun SY;Wang T;Zhu SL .Transesterification kinetics of soybean oil for production of biodiesel in supercritical methanol[J].Journal of the American Oil Chemists' Society,2007(4):399-404.
[52] Kusdiana D;Saka S .[J].Journal of Chemical Engineering of Japan,2001,34(03):383.
[53] Kusdiana D.;Saka S. .Effects of water on biodiesel fuel production by supercritical methanol treatment[J].Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies,2004(3):289-295.
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