Transesterification of Triglycerides by CaO: Increase of the Reaction Rate by Biodiesel Addition

被引：76

作者：

Granados, M. Lopez ^{[1
]}

Alonso, D. Martin ^{[1
]}

Alba-Rubio, A. C. ^{[1
]}

Mariscal, R. ^{[1
]}

Ojeda, M. ^{[1
]}

Brettes, P. ^{[2
]}

机构：

[1] CSIC, Inst Catalisis & Petroleoquim, Madrid 28049, Spain

[2] Ctr Tecnol GAIKER, Zamudio 48170, Bizkaia, Spain

来源：

ENERGY & FUELS | 2009年 / 23卷 / 3-4期

关键词：

SOLID BASE CATALYST; SOYBEAN OIL; CALCIUM-OXIDE; SUNFLOWER OIL; PHASE; AL;

D O I：

10.1021/ef800983m

中图分类号：

TE [石油、天然气工业]; TK [能源与动力工程];

学科分类号：

080707 [能源环境工程]; 082001 [油气井工程];

摘要：

A simple procedure has been found that significantly promotes the transesterification reaction rate catalyzed by CaO and moreover prevents the catalyst poisoning by ambient CO2 and H2O. The presence of a small amount of biodiesel in the initial methanol-triglyceride mixture (3 wt % referred to oil) results in a significant increase of the rate of triglyceride methanolysis carried out in a batch reactor. The biodiesel must be previously mixed with the activated CaO, forming a paste. The formation of such a paste also results in a remarkable protection of the activated CaO against the poisoning by ambient CO2 and H2O that may occur during handling of the activated solid.

引用

页码：2259 / 2263

页数：5

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