Biodiesel Synthesis via Esterification of Feedstock with High Content of Free Fatty Acids

被引:56
作者
Souza, Marcella S. [3 ]
Aguieiras, Erika C. G. [2 ]
da Silva, Monica A. P. [3 ]
Langone, Marta A. P. [1 ]
机构
[1] Univ Estado Rio de Janeiro, Inst Quim, BR-20559900 Rio De Janeiro, Brazil
[2] Univ Estado Rio de Janeiro, Inst Biol Roberto Alcantara Gomes, BR-20559900 Rio De Janeiro, Brazil
[3] Univ Fed Rio de Janeiro, Escola Quim, BR-21949900 Rio De Janeiro, Brazil
关键词
Esterification; SODD; Biodiesel; Ethanol; Immobilized lipase; Zeolite; IMMOBILIZED LIPASE; CATALYSTS; ZIRCONIA; METHANOL; SAPO-34; REACTIVITY; ZEOLITES; TEMPLATE; SYSTEM; OLEATE;
D O I
10.1007/s12010-008-8444-4
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The objective of this work was to study the synthesis of ethyl esters via esterification of soybean oil deodorizer distillate with ethanol, using solid acid catalysts and commercial immobilized lipases, in a solvent-free system. Three commercially immobilized lipases were used, namely, Lipozyme RM-IM, Lipozyme TL-IM, and Novozym 435, all from Novozymes. We aimed for optimum reaction parameters: temperature, enzyme concentration, initial amount of ethanol, and its feeding technique to the reactor (stepwise ethanolysis). Reaction was faster with Novozym 435. The highest conversion (83.5%) was obtained after 90 min using 3 wt.% of Novozym 435 and two-stage stepwise addition of ethanol at 50 C. Four catalysts were also tested: zeolite CBV-780, SAPO-34, niobia, and niobic acid. The highest conversion (30%) was obtained at 100 C, with 3 wt.% of CBV-780 after 2.5 h. The effects of zeolite CBV 780 concentration were studied, resulting in a conversion of 49% using 9 wt.% of catalyst.
引用
收藏
页码:253 / 267
页数:15
相关论文
共 30 条
  • [11] Gomes ACL, 2004, STUD SURF SCI CATAL, V154, P2432
  • [12] Industrial applications of microbial lipases
    Hasan, Fariha
    Shah, Aamer Ali
    Hameed, Abdul
    [J]. ENZYME AND MICROBIAL TECHNOLOGY, 2006, 39 (02) : 235 - 251
  • [13] Analysis of acidic properties of zeolitic and non-zeolitic solid acid catalysts using temperature-programmed desorption of ammonia
    Katada, N
    Niwa, M
    [J]. CATALYSIS SURVEYS FROM ASIA, 2004, 8 (03) : 161 - 170
  • [14] Kinetic studies on the Rhizomucor miehei lipase catalyzed esterification reaction of oleic acid with 1-butanol in a biphasic system
    Kraai, G. N.
    Winkelman, J. G. M.
    de Vries, J. G.
    Heeres, H. J.
    [J]. BIOCHEMICAL ENGINEERING JOURNAL, 2008, 41 (01) : 87 - 94
  • [15] Methanol conversion on SAPO-34 catalysts prepared by mixed template method
    Lee, Yun-Jo
    Baek, Seung-Chan
    Jun, Ki-Won
    [J]. APPLIED CATALYSIS A-GENERAL, 2007, 329 : 130 - 136
  • [16] Technical aspects of biodiesel production by transesterification - a review
    Meher, LC
    Sagar, DV
    Naik, SN
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2006, 10 (03) : 248 - 268
  • [17] SYNTHESIS OF SAPO-34 - HIGH-SILICON INCORPORATION IN THE PRESENCE OF MORPHOLINE AS TEMPLATE
    PRAKASH, AM
    UNNIKRISHNAN, S
    [J]. JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS, 1994, 90 (15): : 2291 - 2296
  • [18] Esterification of palmitic acid with methanol over tungsten oxide supported on zirconia solid acid catalysts: effect of method of preparation of the catalyst on its structural stability and reactivity
    Ramu, S
    Lingaiah, N
    Devi, BLAP
    Prasad, RBN
    Suryanarayana, I
    Prasad, PSS
    [J]. APPLIED CATALYSIS A-GENERAL, 2004, 276 (1-2) : 163 - 168
  • [19] Rocha JMS, 1999, J CHEM TECHNOL BIOT, V74, P607, DOI 10.1002/(SICI)1097-4660(199907)74:7<607::AID-JCTB74>3.0.CO
  • [20] 2-N