欢迎登录材料期刊网

材料期刊网

高级检索

在常压H_2气氛下催化丙三醇脱水-加氧制备了1,2-丙二醇.首先在220℃和常压H_2条件下,以Cu/Al_2O_3为催化剂催化丙三醇脱水生成中间体内酮醇,其选择性高达86%.考察了Cu负载量、反应温度和反应气氛对催化剂件能的影响.在随后的丙酮醇加氢反应中,Raney Ni催化剂显示出优异的催化性能,在120℃和常压H_2条件下,1,2-丙二醇选择性可达99%以上,催化剂连续使用5h未出现失活现象.考察了反应温度、空速及反应时间对催化剂性能的影响.

The novel technology for synthesis of 1,2-propylene glycol by dehydration-hydrogenation of glycerol at ambient hydrogen pres-sure was reported. Dehydration of glycerol to acetol was catalyzed by Cu/Al_2O_3 catalyst. A 86% selectivity for acetol was achieved at 220 ℃ and ambient hydrogen pressure. The effects of copper loading, reaction temperature, and reaction atmosphere on the catalyst performance were studied. Raney Ni catalyst showed excellent catalytic performance in the hydrogenation of acetol to 1,2-propylene glycol. The selectiv-ity for 1,2-propylene glycol was more than 99% at 120 ℃ and ambient hydrogen pressure, and no appreciable change in the activity was observed over the Raney Ni catalyst after 5 h of time-on-stream. The influence of reaction conditions on the conversion and selectivity was also investigated in the hydrogenation of acetol.

参考文献

[1] 闵恩泽.利用可再生农林生物质资源的炼油厂--推动化学工业迈入"碳水化合物"新时代[J].化学进展,2006(02):131-141.
[2] Huber G W;Iborra S;Corma A .[J].Chemical Reviews,2006,106:4044.
[3] Maris E P;Davis R J .[J].Journal of Catalysis,2007,249:328.
[4] Maris E P;Ketchie W C;Murayama M;Davis R J .[J].Journal of Catalysis,2007,251:281.
[5] Dasari M A;Kiatsimkul P P;Sutterlin W R;Suppes G J .[J].Applied Catalysis A:General,2005,281:225.
[6] Chaminand J;Djakovitch L;Gallezot P;Marion P;Pinel C;Rosier C .Glycerol hydrogenolysis on heterogeneous catalysts[J].Green chemistry,2004(8):359-361.
[7] Furikado I;Miyazawa T;Koso S;Shimao A Kunimori K Tomishige K .[J].Green Chemistry,2007,9:582.
[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] Miyazawa T;Koso S;Kunimori K;Tomishige K .Development of a Ru/C catalyst for glycerol hydrogenolysis in combination with an ion-exchange resin[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2007(0):244-251.
[10] Feng J;Fu H Y;Wang J B;Li R X Chen H Li X J .[J].Catalysis Communications,2008,9:1458.
[11] Feng J;Wang J B;Zhou Y F;Fu H Y Chen H Li X J .[J].Chem Lett,2007,36:1274.
[12] Ma L;He D H;Li Z P .[J].Catalysis Communications,2008,9:2489.
[13] 马兰;贺德华 .[J].催化学撤,2009,30:471.
[14] Wang, S;Liu, HC .Selective hydrogenolysis of glycerol to propylene glycol on Cu-ZnO catalysts[J].Catalysis Letters,2007(1/2):62-67.
[15] Huang Z W;Cui F;Kang H X;Chen J Zhang X Z Xia C G .[J].Chemistry of Materials,2008,20:5090.
[16] Perosa A;Tundo P .[J].Industrial and Engineering Chemistry Research,2005,44:8535.
[17] 赵会吉,张津林,白锐,刘晨光.新型固定床Raney Ni催化剂的苯加氢活性及耐硫性[J].石油化工,2007(07):653-658.
[18] Chiu C W;Tekeei A;Sutterlin W R;Ronco J M Suppes G J .[J].AICHE Journal,2008,54:2456.
[19] Fukuoka A;Dhepe P L .[J].Angewandte Chemie International Edition,2006,45:5161.
[20] Klinsoda I;Piumsomboon P .[J].Energy Conversion and Management,2007,48:1200.
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%