利用酶法脱胶-反酯化联合工艺从粗豆油中生产乙基生物柴油

IF 5.6 1区 农林科学 Q1 AGRICULTURAL ENGINEERING
Rafaela M. dos Passos , Ramon S.B. Ferreira , Marcelo A. Morgano , Patrícia T. de Souza , Antonio J.A. Meirelles , Eduardo A.C. Batista , Guilherme J. Maximo , Marcela C. Ferreira , Klicia A. Sampaio
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引用次数: 0

摘要

巴西是世界上最大的大豆生产国之一。巴西的生物柴油生产(特别是大豆油生物柴油)逐年增长,需要更有效和可持续的技术,酶法工艺就是其中之一。在生物柴油生产之前,酶法脱胶可以作为提供更高质量产品的一种替代方法,同时也是减少时间和成本的一种建议。因此,这项工作的目的是评估使用磷脂酶鸡尾酒对粗豆油进行酶法脱胶(之前已进行过优化)以及使用黑曲霉的脂肪酶进行酯交换反应以生产乙基生物柴油的情况。为此,通过中央复合可旋转设计(CCRD)对乙醇:油(E:O)比例、水和脂肪酶百分比进行了酯交换优化。最佳条件用于评估两种脱胶-酯交换相关工艺:i) 单锅反应(OPR),即在同一反应器中进行脱胶和酯交换反应;ii) 双锅反应(TPR),即首先对油进行脱胶,然后进行酯交换反应。在 E:O = 4.48:1、水 = 3.41 % 和脂肪酶 = 2.43 % 的条件下,达到了最佳的酯交换条件,获得了 97 % 的脂肪酸乙酯 (FAEE)。OPR 和 TPR 都能提供脂肪酸乙酯含量为 94% 的生物柴油:在生物柴油提纯前后,TPR 的效果最好,分别为 97.5 % 和 99.98 %。矿物元素(包括磷)和其他杂质(阴离子)含量较低,符合质量标准。生产的甘油杂质含量也很低,这一点非常有利。虽然脂肪酶利用原油(对照组)实现了向 FAEE 的良好转化(95.7 ± 0.29 %),但最终生物柴油含有大量杂质(P=80.07 ± 0.1 mg/kg),因此需要后续的生物柴油提纯步骤。此外,高杂质含量产生的生物柴油不符合 ANP 立法标准(P<10 mg/kg)。在生物柴油生产过程中使用酶法脱胶,不仅能产生杂质含量低、最终质量高的生物柴油,还能减少污水排放。酶法脱胶是获得高质量生物柴油的关键,而酶法脱胶与酯交换反应的结合则是减少生物柴油生产时间和成本的最佳选择。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Ethyl biodiesel production from crude soybean oil using enzymatic degumming-transesterification associated process
Brazil is one of the largest soybean producers in the world. Biodiesel production in Brazil (specially soybean oil biodiesel) has been growing every year and demanding more effective and sustainable technologies, which is the case of enzymatic processes. Enzymatic degumming could be an alternative to provide better quality products, before biodiesel production but also, in a one reaction step as a proposal to reduce time and costs. Therefore, this work was aimed at evaluating enzymatic degumming (previously optimized) of crude soybean oil using a phospholipase cocktail associated with transesterification using lipase from Aspergillus oryzae for ethyl biodiesel production. For this, transesterification was optimized for ethanol:oil (E:O) ratio, water and lipase % through a central composite rotatable design (CCRD). Optimal conditions were used to evaluate two degumming-transesterification associated processes: i) a one-pot reaction (OPR) where degumming and transesterification were performed at the same reactor; and ii) a two-pot reaction (TPR) where oil was first degummed, followed by transesterification. The optimal transesterification condition were achieved for E:O = 4.48:1, water = 3.41 % and lipase = 2.43 %, where 97 % fatty acid ethyl esters (FAEE) were obtained. Both OPR and TPR provided biodiesels with FAEE > 94 %: TPR was the best with 97.5 % and 99.98 % before and after biodiesel purification. Mineral elements (including phosphorus) and other impurities (anions) were low, and within quality standards. Glycerol produced also presented very low content of impurities which is quite advantageous. Although lipase achieves good conversion to FAEE (95.7 ± 0.29 %) using crude oil (Control), the final biodiesel carries many impurities (P=80.07 ± 0.1 mg/kg), thus requiring subsequent biodiesel purification steps. In addition, the high impurity content generates a biodiesel that does not comply with ANP legislative standards, P<10 mg/kg. The use of enzymatic degumming in the biodiesel production process generates a biodiesel with low impurities and higher final quality, in addition to being a process that generates less effluent. Enzymatic degumming was essential for obtaining high quality biodiesel and its association with transesterification showed to be a great option for decreasing time and costs for biodiesel production.
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来源期刊
Industrial Crops and Products
Industrial Crops and Products 农林科学-农业工程
CiteScore
9.50
自引率
8.50%
发文量
1518
审稿时长
43 days
期刊介绍: Industrial Crops and Products is an International Journal publishing academic and industrial research on industrial (defined as non-food/non-feed) crops and products. Papers concern both crop-oriented and bio-based materials from crops-oriented research, and should be of interest to an international audience, hypothesis driven, and where comparisons are made statistics performed.
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