Kinetic study of synthesis of bio-fuel additives from glycerol using a hetropolyacid

Sravanthi Veluturla , Archna Narula , Subba Rao D , Suniana P. Shetty
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引用次数: 15

Abstract

Concerns about the ever increasing quantities of glycerol produced as a by-product of the process of manufacture of bio-diesel serve as a fuel for research about the alternative uses of glycerol. The esterification of glycerol with acetic acid over Cesium supported heteropolyacid (CsPWA) serving as the catalyst was carried out. The products obtained were mono, di and tri acetins which have wide application as biofuels. A series of experiments were carried out with CsPWA as catalyst and parameters considered for studies were temperature, molar ratio of reactants (acetic acid:glycerol) and the catalyst loading weight percent. Each parameter was varied keeping the other two constant and the results were recorded. Temperature was varied from 80°C to 110°C; molar ratio of glycerol to acetic acid is between 3:1 and 9:1 and catalyst loading of 3%w/w to 7%w/w. The yield and conversion varied for different conditions, but in general, the yield of diacetin and triacetin increased with time. Optimum parameters were adjudged to be 110°C with a molar ratio of 9:1 of the reactants and catalyst loading being 5% weight of reaction mixture where maximum glycerol conversion of 98% was obtained. The results obtained indicate that the esterification of glycerol with acetic acid is a consecutive reaction and the kinetic model was developed based on homogeneous first order reaction series by optimization method using MATLAB, and rate constants (k1, k2 and k3) were determined. From the rate constants at different temperatures, using Arrhenius equation the activation energies (E1, E2 and E3) were also determined.

用异聚酸从甘油合成生物燃料添加剂的动力学研究
生物柴油生产过程中产生的副产品甘油的数量不断增加,这一问题引起了人们的关注,并为研究甘油的替代用途提供了燃料。以铯负载杂多酸(CsPWA)为催化剂,进行了甘油与乙酸的酯化反应。所得产物为单、二、三乙酰酯,在生物燃料中有广泛的应用。以CsPWA为催化剂,以温度、反应物(乙酸:甘油)的摩尔比和催化剂负载率为研究参数,进行了一系列实验。在保持其他两个参数不变的情况下,改变每个参数并记录结果。温度范围为80 ~ 110℃;甘油与乙酸的摩尔比为3:1 ~ 9:1,催化剂负载为3% ~ 7%w/w。在不同条件下,二乙酸乙酯和三乙酸乙酯的产率和转化率不同,但总的来说,二乙酸乙酯和三乙酸乙酯的产率随时间的增加而增加。最佳反应温度为110℃,反应物摩尔比为9:1,催化剂用量为反应混合物重量的5%,甘油转化率最高可达98%。结果表明,甘油与乙酸的酯化反应为连续反应,采用MATLAB优化方法,基于均相一级反应序列建立了酯化反应动力学模型,确定了反应速率常数k1、k2和k3。根据不同温度下的反应速率常数,利用Arrhenius方程确定了反应的活化能(E1, E2和E3)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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