Separation Process Development Laboratory, Chemical Engineering School, State University of Campinas, 13081970 Campinas, São Paulo, Brazil.
Appl Biochem Biotechnol. 2010 Apr;160(7):1879-87. doi: 10.1007/s12010-009-8822-6. Epub 2009 Oct 28.
Distilled glycerides are obtained through distillation of the system mono-diglycerides which is produced from the esterification reaction between a triglyceride with glycerol. In this work, monoglycerides (MG) and diglycerides (DG) are produced through lipase-catalyzed glycerolysis of soybean oil using Candida antarctica B in a solvent-free system. To separate the products of the reaction in order to obtain essentially MG and an oil of DG, it is necessary to use a suitable process in order to preserve the stability of the components and to keep the products free of inappropriate solvents. So, after 24 h of enzymatic reaction, the mixture of acylglycerols and fatty acids was distilled into a centrifugal molecular distiller, since it provides a free solvent and lower temperature environment to increase the desired product concentration. Starting from a material with 25.06% of triglycerides (TG), 46.63% of DG, 21.72% of MG, 5.38% of free fatty acids (FFA), and 1.21% of glycerol, the MG purity in the distillate stream was 80% at evaporator temperature (T (E)) equal to 250 degrees C and feed flow rate (Q) equal to 10.0 mL/min. At these conditions, the MG recovery was 35%. The material collected in the residue stream presented DG-enriched oil with TG unhydrolyzed, residual MG, and low acidity (29.83% of TG, 53.20% of DG, 15.64% of MG, and 1.33% of FFA), which is suitable to replace TG oil in the human diet.
甘油单酯是通过甘油与三酰甘油的酯化反应生成的单甘酯体系的蒸馏得到的。在这项工作中,通过脂肪酶催化大豆油的甘油解反应,在无溶剂体系中使用南极假丝酵母 B 生产单甘酯 (MG) 和二甘酯 (DG)。为了分离反应产物,以获得基本上是 MG 和 DG 油,有必要使用合适的工艺来保持各组分的稳定性,并使产品不含不合适的溶剂。因此,在酶反应 24 小时后,将酰基甘油和脂肪酸的混合物蒸馏到离心分子蒸馏器中,因为它提供了一个无溶剂和低温的环境,以提高所需产物的浓度。从含有 25.06%三酰甘油 (TG)、46.63% DG、21.72% MG、5.38%游离脂肪酸 (FFA) 和 1.21%甘油的原料开始,在蒸发器温度 (T(E))等于 250°C 和进料流速 (Q)等于 10.0 毫升/分钟的情况下,蒸馏物中 MG 的纯度为 80%。在这些条件下,MG 的回收率为 35%。残留在残渣中的物料为富含 DG 的油,其中 TG 未水解,残余 MG 和低酸度 (29.83% TG、53.20% DG、15.64% MG 和 1.33% FFA),适合替代人类饮食中的 TG 油。