Large-scale purification of γ-linolenic acid by selective esterification using Rhizopus delemar lipase

被引:22
作者
Shimada, Y
Sakai, N
Sugihara, A
Fujita, H
Honda, Y
Tominaga, Y
机构
[1] Osaka Municipal Tech Res Inst, Joto Ku, Osaka 5368553, Japan
[2] Nippon Synthet Chem Ind Co Ltd, Osaka 5670052, Japan
关键词
borage oil; distillation; hydrolysis; gamma-linolenic acid; Pseudomonas sp. lipase; purification; Rhizopus delemar lipase; selective esterification; urea adduct;
D O I
10.1007/s11746-998-0091-y
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
gamma-Linolenic acid (GLA) is a physiologically valuable fatty acid, and is desired as a medicine, but a useful method available for industrial purification has not been established. Thus, large-scale purification was attempted by a combination of enzymatic reactions and distillation. An oil containing 45% GLA (GLA45 oil) produced by selective hydrolysis of borage oil was used as a starting material. GLA45 oil was hydrolyzed at 35 degrees C in a mixture containing 33% water and 250 U/g-reaction mixture of Pseudomonas sp. lipase; 91.5% hydrolysis was attained after 24 h. Film distillation of the dehydrated reaction mixture separated free fatty acids (FFA; acid value 199) with a recovery of 94.5%. The FFA were selectively esterified at 30 degrees C for 16 h with two molar equivalents of lauryl alcohol and 50 U/g of Rhizopus delemar lipase in a mixture containing 20% water. The esterification extent was 52%, and the GLA content in the FFA fraction was raised to 89.5%. FFA and lauryl esters were not separated by film distillation, but the FFA-rich fraction contaminated with 18% lauryl esters was recovered by simple distillation. To further increase the GLA content, the FFA-rich fraction was selectively esterified again under similar conditions. As a result, the CLA content in the FFA fraction was raised to 97.3% at 15.2% esterification. After simple distillation of the reaction mixture, lauryl esters contaminating the FFA-rich fraction were completely eliminated by urea adduct fractionation. When 10 kg of GLA45 oil was used as a starting material, 2.07 kg of FFA with 98.6% GLA was obtained with a recovery of 49.4% of the initial content.
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页码:1539 / 1544
页数:6
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