欢迎登录材料期刊网

材料期刊网

高级检索

采用共沉淀法制备了一系列铜基催化剂,在N2中于高压釜中,考察了其催化甘油脱水制备羟基丙酮的反应性能.结果表明,Cu/SiO2催化剂具有较高的催化甘油脱水活性,但目的产物羟基丙酮易与反应产生的H2生成1,2-丙二醇,使得羟基丙酮选择性不高.因此,在固定床反应器上详细考察了在优选的Cu/SiO2催化剂上反应气氛、温度和空速对甘油脱水性能的影响.与纯H2或N2相比,在5%H2~95%N2混合气气氛下反应,Cu/SiO2催化剂表现出较高的活性和羟基丙酮选择性.采用H2-N2混合气作为反应气氛,在一定程度上抑制了N2气氛下催化剂的失活和H2气氛下羟基丙酮的过度加氢.在220℃,常压,5%H2-95%N2混合气气氛和WHSV=0.08 h-1条件下,甘油转化率和羟基丙酮选择性分别高达98.8%和84.6%.

参考文献

[1] 姚日生;金友华 .[J].湖南化工,2000,30(06):32.
[2] 晁自胜;周春娇;章文贵;凡美莲,粱海军,孙成高,黄彩娟 .[P].CN 101 284 234,2008.
[3] 李楠;徐华龙;沈伟;邱建立,刘琼 .[P].CN 101 016 234,2007.
[4] Kinage A K;Upare P P;Kasinathan P;Hwang Y K Chang J S .[J].Catalyst Communication,2010,11:620.
[5] Chin C w;Dasari M A;Suppes G J;SuRedin W R .[J].AICHE Journal,2006,52:3543.
[6] Sato S;Akiyama M;Takahashi R;Hara T Inui K Yokota M .[J].Applied Catalysis A:General,2008,347:186.
[7] 赵静,于维强,李德财,马红,高进,徐杰.常压两步法催化丙三醇脱水-加氢制备1,2-丙二醇[J].催化学报,2010(02):200-204.
[8] Miyazawa T;Kusunoki Y;Kunimori K;Tomishige K .Glycerol conversion in the aqueous solution under hydrogen over Ru/C plus an ion-exchange resin and its reaction mechanism[J].Journal of Catalysis,2006(2):213-221.
[9] Guo L Y;Zhou J X;Mao J B;Guo X W,Zhang S G .[J].Applied Catalysis A,2009,367:93.
[10] Alhanash A;Kozhevnikova E F;Kozhevnikov I V .[J].Catalysis Letters,2008,120:307.
[11] Akiyama M;Sato S;Takahashi R;Inui K Yokota M .[J].Applied Catalysis A:General,2009,371:60.
[12] Huang Z W;Cui F;Kang H X;Chen J,Zhang X Z,Xia C G .[J].Chemistry of Materials,2008,20:5090.
[13] Huang Z W;Cui F;Kang H X;Chen J,Xia C G .[J].Applied Catalysis A:General,2009,366:288.
[14] Sato S;Takahashi R;Sodesawa T;Yuma,K I,Obata Y J .[J].Journal of Catalysis,2000,196:195.
[15] Suprun W;Lutecki M;Haber T;Papp H .[J].Journal of Molecular Catalysis A:Chemical,2009,309:71.
[16] Roy D;Subramaniam B;Chaudhari R V .[J].Catalysis Today,2010,156:3l.
[17] Huang L;Zhu YL;Zheng HY;Li YW;Zeng ZY .Continuous production of 1,2-propanediol by the selective hydrogenolysis of solvent-free glycerol under mild conditions[J].Journal of Chemical Technology & Biotechnology,2008(12):1670-1675.
[18] Wen G D;Xu Y P;Ma H J;Xu Z S Tian Z J .[J].International Journal of Hydrogen Energy,2008,33:6657.
[19] Davda RR;Shabaker JW;Huber GW;Cortright RD;Dumesic JA .A review of catalytic issues and process conditions for renewable hydrogen and alkanes by aqueous-phase reforming of oxygenated hydrocarbons over supported metal catalysts[J].Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications,2005(1/2):171-186.
[20] Yaylayan V A;Harty-Majors S;Ismail A A .[J].Carbohydrate Research,1999,318:20.
[21] Xu Y P;Tian Z J;Wlen G D;Xu Z S Qu W Lin L W .[J].Chemistry Letters,2006,35:216.
[22] Wolfson A;Dlugy C;Shotland Y;Tavor D.Shirai M .[J].Tetrahedron Letters,2009,50:5951.
[23] Nimlos MR;Blanksby SJ;Qian XH;Himmel ME;Johnson DK .Mechanisms of glycerol dehydration[J].The journal of physical chemistry, A. Molecules, spectroscopy, kinetics, environment, & general theory,2006(18):6145-6156.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%