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以生物质基碳水化合物为原料,以Sn-MCM-41和SnO2/SiO2为催化剂,在亚临界甲醇中制备乳酸甲酯.发现具有高度有序介孔结构的Sn-MCM-41和部分有序介孔结构的SnO2/SiO2-a都有较好的催化活性,在最优反应条件下,乳酸甲酯的收率可达40.3%.采用X射线衍射、N2吸附-脱附、透射电镜、吡啶吸附红外光谱和NH3程序升温脱附等技术对反应前后的催化剂进行了表征.结果表明,乳酸甲酯的收率与反应时间、反应温度以及催化剂的酸量有关.另外,Sn-MCM-41和SnO2/SiO2催化剂循环使用5次后其活性变化不大.结果显示,反应后这两种催化剂的Sn流失量小于0.15%,其结构以及酸性种类也没有明显变化.

参考文献

[1] Vennestrom P N R;Osmundsen C M;Christensen C H;Taarning E .[J].Angewandte Chemie International Edition,2011,50:10502.
[2] Serrano-Ruiz J C;Luque R;Sepulveda-Escribano A .[J].Chemical Society Reviews,2011,40:5266.
[3] 赵天涛,张丽杰,高静,黄志红,全学军.脂肪酶催化乳酸与乙醇合成乳酸乙酯的反应动力学[J].催化学报,2008(02):141-144.
[4] John RP;G.S. A;Nampoothiri KM;Pandey A .Direct lactic acid fermentation: Focus on simultaneous saccharification and lactic acid production[J].Biotechnology Advances: An International Review Journal,2009(2):145-152.
[5] Datta R;Henry M .Lactic acid: recent advances in products, processes and technologies - a review[J].Journal of Chemical Technology & Biotechnology,2006(7):1119-1129.
[6] 刘喆.我国乳酸的生产技术及研发状况[J].河南化工,2010(07):29-31.
[7] Wasewar, KL;Yawalkar, AA;Moulijn, JA;Pangarkar, VG .Fermentation of glucose to lactic acid coupled with reactive extraction: A review[J].Industrial & Engineering Chemistry Research,2004(19):5969-5982.
[8] Aida T M;Tajima K;Watanabe M;Saito Y Kuroda K Nonaka T Hattori H Smith R L Jr Arai K .[J].Journal of Supercritical Fluids,2007,42:110.
[9] Rasrendra C B;Makertihartha I G B N;Adisasmito S;Heeres H J .[J].Topics in Catalysis,2010,53:1241.
[10] Hayashi Y;Sasaki Y.[J].Chemical Communications,2005:2716.
[11] Onda A;Ochi T;Kajiyoshi K;Yanagisawa K .[J].Catalysis Communications,2008,9:1050.
[12] Onda A;Ochi T;Kajiyoshi K;Yanagisawa K .[J].Applied Catalysis A:General,2008,343:49.
[13] Yan X Y;Jin F M;Tohji K;Kishita A Enomoto H .[J].AICHE Journal,2010,56:2727.
[14] Holm M S;Saravanamurugan S;Taarning E .[J].Science,2010,328:602.
[15] Liu Zh;Li W;Pan Ch Y;Chen P Lou H Zheng X M .[J].Catalysis Communications,2011,15:82.
[16] Corma A;Navarro M T;Renz M .[J].Journal of Catalysis,2003,219:242.
[17] Wu P;Li L D;Yu Q;Wu G J Guan N J .[J].Catalysis Today,2010,158:228.
[18] Harrison P G;Lloyd N C;Daniell W;Bailey C Azelee W .[J].Chemistry of Materials,1999,11:896.
[19] Zukal A;Thommes M;Cejka J .[J].Microporous and Mesoporous Materials,2007,104:52.
[20] Alarcon E A;Villa A L;de Correa C M .[J].Microporous and Mesoporous Materials,2009,122:208.
[21] Kovalenko VV;Zhukova AA;Rumyantseva MN;Gaskov AM;Yushchenko VV;Ivanova II;Pagnier T .Surface chemistry of nanocrystalline SnO2: Effect of thermal treatment and additives[J].Sensors and Actuators, B. Chemical,2007(1):52-55.
[22] West, R.M.;Holm, M.S.;Saravanamurugan, S.;Xiong, J.;Beversdorf, Z.;Taarning, E.;Christensen, C.H. .Zeolite H-USY for the production of lactic acid and methyl lactate from C_3-sugars[J].Journal of Catalysis,2010(1):122-130.
[23] Román-Leshkov Y;Moliner M;Labinger J A;Davis M E .[J].Angewandte Chemie International Edition,2010,49:8954.
[24] Matsuoka S;Kawamoto H;Saka S .[J].Journal of Analytical and Applied Pyrolysis,2012,93:24.
[25] Wang J Ch;Masui Y;Onaka M .[J].Applied Catalysis B:Environmental,2011,107:135.
[26] Sasaki M;Goto K;Tajima K;Adschiri T Arai K .[J].Green Chemistry,2002,4:285.
[27] Taarning E;Saravanamurugan S;Spangsberg Holm M;Xiong J M West R M Christensen C H .[J].ChemSusChem,2009,2:625.
[28] Assary, R.S.;Curtiss, L.A. .Theoretical study of 1,2-hydride shift associated with the isomerization of glyceraldehyde to dihydroxy acetone by Lewis acid active site models[J].The journal of physical chemistry, A. Molecules, spectroscopy, kinetics, environment, & general theory,2011(31):8754-8760.
[29] Pescarmona P P;Janssen K P F;Delaet C;Stroobants C Houthoofd K Philippaerts A De Jonghe C Paul J S Jacobs P A Sels B F .[J].Green Chemistry,2010,12:1083.
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