The factors influencing stability of Ca-Al mixed oxides as a possible catalyst for biodiesel production

被引:23
作者
Kocik, Jaroslav [1 ]
Hajek, Martin [1 ]
Troppova, Ivana [1 ]
机构
[1] Univ Pardubice, Fac Chem Technol, Dept Phys Chem, Pardubice 53210, Czech Republic
关键词
Hydrocalumites; Ca-Al mixed oxides; Transesterification; Stability; LAYERED DOUBLE HYDROXIDE; SOLID BASE CATALYST; ACID METHYL-ESTERS; RAPESEED OIL; HYDROCALUMITE-TYPE; SOYBEAN OIL; TRANSESTERIFICATION; ESTERIFICATION; METHANOL; ALKALI;
D O I
10.1016/j.fuproc.2015.02.013
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The Ca-Al mixed oxides with a constant molar ratio of Ca/Al and different calcination conditions (temperature from 250 to 950 degrees C and flow - air or nitrogen) were synthetized from hydrocalumite as a precursor. The synthetized mixed oxides were tested in the transesterification of rapeseed oil including the determination of calcium leaching to the liquid products. The leaching was compared with the amount of calcium oxides in the catalyst. The minimum leaching was found for calcination in a flow of nitrogen and 650 degrees C. Moreover, it was found, that the leaching started when the conversion was high and when glycerol was formed. The stability of the catalyst in the reaction components such as oil, methanol, ester and glycerol was determined by diffractograms of the catalyst and by calcium in these components. The highest leaching of calcium was in glycerol and the amount was approximately the same as in transesterification, while in other components it was insignificant. According to the diffractograms (before and after leaching), the phase of mixed oxides was stable during transesterification and leaching was caused by the CaO contained in the catalyst. It was also found, that the significant factor influencing the leaching was water contained in the reaction components. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:297 / 302
页数:6
相关论文
共 33 条
  • [1] [Anonymous], JOINT
  • [2] Al2O3-supported alkali and alkali earth metal oxides for transesterification of palm kernel oil and coconut oil
    Benjapornkulaphong, Sita
    Ngamcharussrivichai, Chawalit
    Bunyakiat, Kunchana
    [J]. CHEMICAL ENGINEERING JOURNAL, 2009, 145 (03) : 468 - 474
  • [3] Alkali metal supported on mesoporous alumina as basic catalysts for fatty acid methyl esters preparation
    Bota, Roxana M.
    Houthoofd, Kristof
    Grobet, Piet J.
    Jacobs, Pierre A.
    [J]. SCIENTIFIC BASES FOR THE PREPARATION OF HETEROGENEOUS CATALYSTS: PROCEEDINGS OF THE 10TH INTERNATIONAL SYMPOSIUM, 2010, 175 : 775 - 778
  • [4] Structure-reactivity correlations in MgAl hydrotalcite catalysts for biodiesel synthesis
    Cantrell, DG
    Gillie, LJ
    Lee, AF
    Wilson, K
    [J]. APPLIED CATALYSIS A-GENERAL, 2005, 287 (02) : 183 - 190
  • [5] HYDROTALCITE-TYPE ANIONIC CLAYS: PREPARATION, PROPERTIES AND APPLICATIONS
    Cavani, F.
    Trifiro, F.
    Vaccari, A.
    [J]. CATALYSIS TODAY, 1991, 11 (02) : 173 - 301
  • [6] Enzymatic biodiesel: Challenges and opportunities
    Christopher, Lew P.
    Kumar, Hemanathan
    Zambare, Vasudeo P.
    [J]. APPLIED ENERGY, 2014, 119 : 497 - 520
  • [7] Used frying oils and fats and their utilization in the production of methyl esters of higher fatty acids
    Cvengros, J
    Cvengrosová, Z
    [J]. BIOMASS & BIOENERGY, 2004, 27 (02) : 173 - 181
  • [8] Exhaust emissions from a Diesel engine fueled with transesterified waste olive oil
    Dorado, MP
    Ballesteros, E
    Arnal, JM
    Gómez, J
    López, FJ
    [J]. FUEL, 2003, 82 (11) : 1311 - 1315
  • [9] A novel kinetic study of H3PW12O40 - catalyzed oleic acid esterification with methanol via 1H NMR spectroscopy
    Fernandes, Sergio Antonio
    Cardoso, Abiney Lemos
    da Silva, Marcio Jose
    [J]. FUEL PROCESSING TECHNOLOGY, 2012, 96 : 98 - 103
  • [10] Biodiesel production by supercritical methanol transesterification: process simulation and potential environmental impact assessment
    Fernando Marulanda, Victor
    [J]. JOURNAL OF CLEANER PRODUCTION, 2012, 33 : 109 - 116