Heterogeneous catalysis of calcium oxide used for transesterification of soybean oil with refluxing methanol

被引:195
作者
Kouzu, Masato [1 ]
Yamanaka, Shin-ya [2 ]
Hidaka, Jyu-suke [2 ]
Tsunomori, Michito [3 ]
机构
[1] Keihanna Interact Plaza Inc, JST KFPT Core Res Ctr, Kyoto 6190237, Japan
[2] Doshisha Univ, Fac Engn Sci, Kyoto 6100321, Japan
[3] Ryoko Lime Ind Co Ltd, Tokyo 1010043, Japan
基金
日本科学技术振兴机构;
关键词
Solid base catalyst; Biodiesel; Calcium oxide; Calcium diglyceroxide; Transesterification; SOLID BASE CATALYSTS; BIODIESEL PRODUCTION; RAPESEED OIL; FUEL;
D O I
10.1016/j.apcata.2008.12.003
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Much interest has been taken in finding a solid base catalyst for a reaction to produce biodiesel. Calcium oxide has the great advantage of the enhanced catalytic activity, but the soluble substance is leached away from the solid base catalyst during the reaction. In this paper, the leaching of solid base catalyst was investigated on the basis of data from the heterogeneous catalytic transesterification of soybean oil at reflux of methanol. When calcium oxide was employed for the reaction, the calcium contents of the produced oil and glycerol were 139 and 4602 ppm, respectively. This data indicated that the amount of the soluble substance corresponded to 10.5 wt% of the employed catalyst. Since calcium oxide was transformed into calcium diglyceroxide at the beginning of the reaction, many of the soluble substances derived from calcium diglyceroxide. Also, the soluble substances were rather active in the soybean oil transesterification. On the other hand, calcium diglyceroxide was employed for the reaction, with the result that the amount of the soluble substance was only 4.0 wt%. In this case, the soluble substance did not catalyze the conversion of soybean oil into its methyl esters. Based on the experimental results, the heterogeneous catalysis of calcium oxide was discussed. Additionally, removal of the soluble substance by cation-exchange resin was tested in order to purify the produced oil. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:94 / 99
页数:6
相关论文
共 19 条
  • [1] New heterogeneous process for biodiesel production: A way to improve the quality and the value of the crude glycerin produced by biodiesel plants
    Bournay, L
    Casanave, D
    Delfort, B
    Hillion, G
    Chodorge, JA
    [J]. CATALYSIS TODAY, 2005, 106 (1-4) : 190 - 192
  • [2] Biodiesel fuel production with solid superacid catalysis in fixed bed reactor under atmospheric pressure
    Furuta, S
    Matsuhashi, H
    Arata, K
    [J]. CATALYSIS COMMUNICATIONS, 2004, 5 (12) : 721 - 723
  • [3] Rapeseed oil methyl esters preparation using heterogeneous catalysts
    Gryglewicz, S
    [J]. BIORESOURCE TECHNOLOGY, 1999, 70 (03) : 249 - 253
  • [4] Solid base catalysts: Generation, characterization, and catalytic behavior of basic sites
    Hattori, H
    [J]. JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2004, 47 (02) : 67 - 81
  • [5] Hattori H., 2000, STUD SURF SCI CATAL, V130, P3507, DOI DOI 10.1016/S0167-2991(00)80566-2
  • [6] Kouzu M., 2006, J F JAPAN I F ENERGY, V85, P135
  • [7] Calcium oxide as a solid base catalyst for transesterification of soybean oil and its application to biodiesel production
    Kouzu, Masato
    Kasuno, Takekazu
    Tajika, Masahiko
    Sugimoto, Yoshikazu
    Yamanaka, Shinya
    Hidaka, Jusuke
    [J]. FUEL, 2008, 87 (12) : 2798 - 2806
  • [8] Active phase of calcium oxide used as solid base catalyst for transesterification of soybean oil with refluxing methanol
    Kouzu, Masato
    Kasuno, Takekazu
    Tajika, Masahiko
    Yamanaka, Shinya
    Hidaka, Jusuke
    [J]. APPLIED CATALYSIS A-GENERAL, 2008, 334 (1-2) : 357 - 365
  • [9] Waste cooking oil-an economical source for biodiesel: A review
    Kulkarni, MG
    Dalai, AK
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (09) : 2901 - 2913
  • [10] Transesterification of soybean oil to biodiesel using CaO as a solid base catalyst
    Liu, Xuejun
    He, Huayang
    Wang, Yujun
    Zhu, Shenlin
    Piao, Xianglan
    [J]. FUEL, 2008, 87 (02) : 216 - 221