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Concentration of docosahexaenoic acid (DHA) and eicosapentaenoic acid (EPA) of tuna oil by urea complexation: optimization of process parameters

机译:Concentration of docosahexaenoic acid (DHa) and eicosapentaenoic acid (Epa) of tuna oil by urea complexation: optimization of process parameters

摘要

Production of docosahexaenoic acid (DHA) and eicosapentaenoic acid (EPA) concentrates from tuna oil was optimized. In the process, the liquid recovery yield (Y-1) and the total content of DHA and EPA (Y-2) were response variables, respectively. A three-factor central composite rotatable design (CCRD) was used to study the effect of urea-to-fatty acid ratio (XI), crystallization temperature (X-2) and crystallization time (X-3). Second order polynomial regression models for Y-1 and Y2 were employed to generate response surfaces. The total DHA and EPA (85.02%) and the liquid recovery yield (25.10%) from tuna oil were obtained at a urea-to-fatty acid ratio of 15 (mole/mole), a crystallization temperature of -5 degrees C, and a crystallization time of 20 h. (c) 2005 Elsevier Ltd. All rights reserved.
机译:优化了从金枪鱼油生产二十二碳六烯酸(DHA)和二十碳五烯酸(EPA)浓缩物的生产。在此过程中,液体回收率(Y-1)和DHA和EPA的总含量(Y-2)分别是响应变量。采用三因素中心复合材料可旋转设计(CCRD)来研究尿素与脂肪酸之比(XI),结晶温度(X-2)和结晶时间(X-3)的影响。 Y-1和Y2的二阶多项式回归模型用于生成响应面。在尿素与脂肪酸的比率为15(摩尔/摩尔),结晶温度为-5摄氏度,且结晶温度为5摄氏度,温度为5摄氏度,温度为5摄氏度的条件下,从金枪鱼油中获得了DHA和EPA的总含量(85.02%)和液体回收率(25.10%)。结晶时间为20小时。 (c)2005 Elsevier Ltd.保留所有权利。

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