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WO_3/ZrO_2-Cu/ZnO催化剂催化甘油氢解性能

Catalytic performance of Cu/ZnO-WO_3/ZrO_2 catalysts for hydrogenolysis of glycerol
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摘要 采用共沉淀法制备Cu/ZnO催化剂,浸渍焙烧法制备WO3/ZrO2催化剂,将2种催化剂进行物理混合制得Cu/ZnO-WO3/ZrO2混合催化剂。通过H2程序升温还原(H2-TPR)、H2程序升温脱附(H2-TPD)等手段对催化剂的物化性质进行表征,在连续流动固定床反应器中考察Cu/ZnO-WO3/ZrO2催化剂对甘油氢解反应的催化性能。结果表明:添加WO3/ZrO2可改善催化剂的还原性能和氢吸附性能,催化剂的稳定性明显提高。在反应温度190℃、H2压力3 MPa、80%甘油水溶液、甘油质量空速0.6 h-1的反应条件下,3Cu/ZnO-WO3/ZrO2催化剂上能获得77.6%的甘油转化率和95.8%的1,2-丙二醇选择性,且反应200 h内,催化剂的催化性能基本无变化。 The Cu/ZnO catalyst was prepared by a co-precipitation method and the WO3/ZrO: catalyst was prepared by a impregnation calcination method. The Cu/ZnO-WO3/ZrO2catalyst was composed of a physical mixture of Cu/ZnO and WOJZrO2. The physic-chemical properties of the catalysts were charac- terized by H2 temperature programmed reduction (H2-TPR) and H2 temperature programmed desorption ( H2-TPD). The performances of the catalysts for glycerol hydrogenolysis to 1,2-propanediol were inversti- gated in a continuous flow fixed-bed reactor. Results showed that the reduction performances and hydrogen adsorption properties of the catalysts with addition of WO3/ZrO2 were improved. Owing to the presence of WOJZr02 ,the stability of Cu-ZnO catalysts was markedly enhanced. Under the conditions of 190℃ ,3 MPa,80% glycerol solution and weight hourly space velocity 0.6 h-1 ,the conversion of glycerol over 3Cu/ZnO-WO3/ZrO2 was 77.6% and the selectivity for 1,2-propanediol was 95.8%. The performances of the catalyst were stable during 200 h operation.
出处 《南京工业大学学报(自然科学版)》 CAS 北大核心 2013年第6期52-55,共4页 Journal of Nanjing Tech University(Natural Science Edition)
基金 国家高技术研究发展计划(863计划)(2012AA03A606)
关键词 Cu ZnO催化剂 WO3 ZRO2 甘油 氢解 1 2-丙二醇 Cu/ZnO catalyst WOz/ZrO2 glycerol hydrogenolysis 1,2-propanediol
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参考文献16

  • 1Corma A,Lborra S,Velty A,et al.Chemical routes for the transformation of biomass into chemicals[J].Chem Rev,2007,107 (6):2411-2502.
  • 2Pagliaro M,Ciriminna R,Kimura H,et al.From glycerol to valueadded products[J].Angew Chem Int Ed,2007,46(24):4434-4440.
  • 3Behr A,Eilting J,Irawadi K,et al.Improved utilisation of renewable resources:new important derivatives of glycerol[J].Green Chem,2008,10(1):13-30.
  • 4Chaminand J,Djakovitch L A,Gallezot P,et al.Glycerol hydrogenolysis on heterogeneous catalysts[J].Green Chem,2004,6 (8):359-361.
  • 5Dasari M A,Kiatsimkul P-P,Sutterlin W R,et al.Low-pressure hydrogenolysis of glycerol to propylene glycerol[J].Appl Catal A:General,2005,281 (1/2):225-231.
  • 6Guo X,Li Y,Shi R,et al.Co/MgO catalysts for hydrogenolysis of glycerol to 1,2-propanediol[J].Appl Catal A:General,2009,371(1/2):108-113.
  • 7Maris E P,Ketchie W C,Murayama M,et al.Glycerol hydrogenolysis on carbon-supported PtRu and AuRu bimetallic catalysts[J].J Catal,2007,251 (2):281-294.
  • 8Barbelli M L,Santorri G F,Nichio N N.Aqueous phase hydrogenolysis of glycerol to bio-propylene glycol over Pt-Sn catalysts[J].Bioresour Techno1,2012,111 (12):500-503.
  • 9Zhou J,Zhang J,Guo X,et al.Ag/A12 O3 for glycerol hydrogenolysis to 1,2-propanediol:activity,selectivity and deactivation[J].Green Chem,2012,14(1):156-163.
  • 10Wang S,Liu H.Selective hydrogenolysis of glycerol to propylene glycol on Cu-ZnO catalysts[J].Catal Lett,2007,117(1/2):62-67.

二级参考文献41

  • 1冯建,袁茂林,陈华,李贤均.甘油催化氢解的研究与应用[J].化学进展,2007,19(5):651-658. 被引量:36
  • 2Pagliaro M,Ciriminna R,Kimura H,et al.From glycerol to value-added products[J].Angew Chem Int Ed,2007,46(24):4434-4440.
  • 3Behr A,Eilting J,Irawadi K,et al.Improved utilization of renewable resources:new important derivatives of glycerol[J].Green Chem,2008,10(1):13-30.
  • 4Zhou C,Beltramini J N,Fan Y,et al.Chemoselective catalytic conversion of glycerol as a biorenewable source to valuable commodity chemicals[J].Chem Soc Rev,2008,37(3):527-549.
  • 5Chaminand J,Djakovitch L,Gallezot P,et al.Glycerol hydrogenoly-sis on heterogeneous catalysts[J].Green Chem,2004,6(8):359-361.
  • 6Miyazawa T,Kusunoki Y,Kunimori K,et al.Glycerol conversion in the aqueous solution under hydrogen over Ru/C +an ion-exchange resin and its reaction mechanism[J].J Catal,2006,240 (2):213-221.
  • 7Maris E P,Davis R J.Hydrogenolysis of glycerol over carbon-supported Ru and Pt catalysts[J].J Catal,2007,249(2):328-337.
  • 8Furikado I,Miyazawa T,Koso S,et al.Catalytic performance of Rh/SiO2 in glycerol reaction under hydrogen[J].Green Chem,2007,9:582-588.
  • 9Alhanash A,Kozhevnikova E F,Kozhevnikov I V.Hydrogenolysis of glycerol to propanediol over Ru:polyoxometalate bifunctional catalyst[J].Catal Lett,2008,120(3/4):307-311.
  • 10Feng J,Fu H,Wang J,et al.Hydrogenolysis of glycerol to glycols over ruthenium catalysts:effect of support and catalyst reduction temperature[J].Catal Commun,2008,9(6):1458-1464.

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