Production of structured lipids by lipase-catalyzed interesterification in a packed bed reactor: effect of reaction parameters on the level of diacylglycerols in the products

H. Mu, Xuebing Xu, J. Adler-Nissen, C. Høy
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引用次数: 22

Abstract

The 1,3-specificity of a lipase was utilized in lipase-catalyzed interesterification to produce specific structured lipids containing long-chain polyunsaturated fatty acids at the sn-2 position and medium-chain fatty acids (MCFAs) at the primary position in a packed-bed reactor. Diacylglycerols (DAGs) are important intermediate products in the production of structured lipids, both with regard to the yields of the products and the content of the by-products, but the levels of DAGs produced in lipase-catalyzed interesterification in a continuous process are not well-known. We examined the effects of the following interesterification parameters on the level of DAGs: reaction temperature, residence time, substrate ratio, and water content. Reaction temperature was the most critical factor, with elevated reactor temperatures (particular those above 60 °C) resulting in a considerable increase in the DAG content of the products. Longer residence times increased the level of DAGs in the products, and favoured the formation of 1,3-DAGs from 1,2-DAGs by acyl migration. Increasing the molar ratio between MCFAs and oil, as well as increasing the water content in the reacting substrate mixture affected the DAG content only slightly. The DAG content in the interesterification products had positive correlation with the migration of MCFAs, implying that a high level of DAGs is an indicator for partial acylglycerols and positional isomers, both are impurities in the products. On the other hand, the content of DAGs correlated positively with the incorporation of MCFAs, suggesting that the DAGs are also important for the production of the structured lipids. Under optimized conditions (temperature, 60°C; water, 0.03%; residence time, 4 h; substrate ratio, 6:1), the level of DAGs produced in the packed-bed reactor was less than 4%, and the incorporation and migration of MCFAs were 47% and 1%, respectively.
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在填充床反应器中用脂肪酶催化的酯化反应生产结构化脂质:反应参数对产物中二酰基甘油含量的影响
在填充床反应器中,利用脂肪酶的1,3特异性在脂肪酶催化的酯化反应中产生了含有sn-2位置的长链多不饱和脂肪酸和主要位置的中链脂肪酸(MCFAs)的特定结构脂质。二酰基甘油(Diacylglycerols, DAGs)是生产结构化脂类的重要中间产物,无论是产品的产率还是副产物的含量,但在脂肪酶催化的连续过程中产生的daags的水平尚不清楚。我们考察了反应温度、停留时间、底物比和水含量对dag含量的影响。反应温度是最关键的因素,反应器温度升高(特别是60°C以上的温度)会导致产物中DAG含量的显著增加。较长的停留时间增加了产物中dag的含量,有利于1,2- dag通过酰基迁移形成1,3- dag。增加MCFAs与油的摩尔比以及增加反应底物混合物中的含水量对DAG含量的影响很小。酯化产物中DAG的含量与mcfa的迁移量呈正相关,表明高水平的DAG是部分酰基甘油和位置异构体的指标,两者都是产物中的杂质。另一方面,dag的含量与mcfa的掺入呈正相关,这表明dag对结构脂质的产生也很重要。在优化条件下(温度:60℃;水、0.03%;停留时间,4小时;底物比为6:1),填充床反应器中产生的dag水平小于4%,mcfa的掺入率和迁移率分别为47%和1%。
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