首页> 外文期刊>Journal of the American Oil Chemists' Society >Production of low-trans fatty acids edible oil by electrochemical hydrogenation in a diaphragm reactor under controlled conditions.
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Production of low-trans fatty acids edible oil by electrochemical hydrogenation in a diaphragm reactor under controlled conditions.

机译:通过在受控条件下在隔膜反应器中进行电化学加氢来生产低反式脂肪酸食用油。

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摘要

Electrochemical hydrogenation is a novel, alternative process for selective hydrogenation of vegetable oils, because of its high extent of hydrogenation and low trans-isomer formation. Electrochemical hydrogenation of soybean oil in a diaphragm reactor with a formate ion concentration of 0.4 mol/l at pH 5.0 under moderate temperature conditions using a current density of 10 mA/cm2 was investigated to identify the critical conditions affecting the selective hydrogenation reaction and the resulting fatty acid profile. The optimum composition was an oil-to-formate solution ratio of 0.3 (w/w), 2-3 g EDDAB in 100 g soybean oil, and 0.8% Pd-C catalyst loading. The electrochemical hydrogenation reaction of soybean oil was described by first-order kinetics, and the kinetic rate constants and reaction selectivity were determined accordingly. Re-use of the Pd-C catalyst up to five times was found to be acceptable. A comprehensive evaluation revealed that the most significant conditions affecting the extent of hydrogenation and the trans fatty acids content of final products were operating temperature, pH of the formate solution, and catalyst loading.
机译:电化学加氢是植物油选择性加氢的一种新颖的替代方法,因为它具有较高的加氢程度和较低的反式异构体形成。研究了在中等温度条件下,电流密度为10 mA / cm 2 的膜片式反应器中,在pH 5.0下甲酸离子浓度为0.4 mol / l的膜式反应器中大豆油的电化学加氢,以确定临界条件影响选择性氢化反应和所得的脂肪酸分布。最佳组成是油与甲酸酯的溶液比为0.3( w / w ),在100克豆油中的2-3 g EDDAB和0.8%Pd- C催化剂负载量。用一级动力学描述了大豆油的电化学加氢反应,并确定了动力学速率常数和反应选择性。发现重复使用Pd-C催化剂最多5次是可以接受的。全面的评估表明,影响氢化程度和最终产物反式脂肪酸含量的最重要条件是操作温度,甲酸盐溶液的pH值和催化剂负载量。

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