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固定化假丝酵母脂肪酶催化合成辛酸甘油酯 总被引:2,自引:0,他引:2
以自制固定化假丝酵母脂肪酶作为催化剂,研究了无溶剂体系中辛酸和甘油直接酯化合成辛酸甘油酯的反应条件。考察了酶的种类、底物的物质的量之比、温度、酶量、甘油的初始含水量和反应时间等因素对辛酸转化率和产物组成的影响。结果证明,以纺织物作为载体制备的固定化假丝酵母脂肪酶适宜催化辛酸甘油酯的合成。最优反应条件为:辛酸与甘油的物质的量之比为2∶1,固定化假丝酵母脂肪酶加量为0.5g /0.69g 甘油,温度为40 ℃ ,振荡培养箱转速为190 r/min。最优反应条件下辛酸转化率可以达到94%以上,经过简单处理的固定化酶可以重复使用4批。 相似文献
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响应面优化褶皱假丝酵母脂肪酶催化合成木质甾醇油酸酯 总被引:1,自引:0,他引:1
以木质甾醇转化率为指标,考察了10种常见商业化脂肪酶催化合成木质甾醇油酸酯的效果,确定褶皱假丝酵母脂肪酶(CRL)为优选生物催化剂,进一步筛选出正己烷为优选反应介质.在脂肪酶用量、油酸和木质甾醇的物质的量比、反应温度和反应时间这4个单因素考察基础上,通过响应面分析法对酶催化木质甾醇油酸酯合成工艺条件进行优化,并对优化条件进行验证和放大实验.CRL催化合成木质甾醇油酸酯的优化工艺参数为:CRL添加量为木质甾醇质量的10%,油酸与木质甾醇的物质的量比为3.8:1,反应温度为46℃,反应时间为28 h,木质甾醇的转化率为91.56%±0.25%. 相似文献
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以磁性壳聚糖纳米复合材料共价固定的褶皱假丝酵母脂肪酶为催化剂,以木质甾醇和油酸为原料,对木质甾醇油酸酯的酶法合成工艺条件进行了优化。得到的最佳工艺条件为:催化剂用量12.7%(以底物总质量计),油酸与木质甾醇物质的量比为2∶1,木质甾醇质量浓度为122.9 g/L,反应温度50℃,反应时间24 h。在该条件下,木质甾醇转化率为96.42%。对月桂酸、肉豆蔻酸、棕榈酸不同碳链长度的脂肪酸或混合脂肪酸进行酯化反应,木质甾醇的转化率可达96.67%~98.74%,催化剂使用5次时,转化率仍可达82.45%。 相似文献
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固定化假丝酵母99-125脂肪酶催化酯化脂肪酸低碳醇酯反应条件的研究 总被引:9,自引:2,他引:9
以硅藻土和纺织品为载体 ,采用吸附法制备固定化脂肪酶 ,研究了固定化假丝酵母 99 1 2 5脂肪酶在有机溶剂中催化脂肪酸低碳醇酯酯化合成过程中 ,有机溶剂性质、脂肪酸与低碳醇的结构、pH值、反应温度和体系含水量、低碳醇的抑制作用等因素对酯化过程的影响。试验结果表明 :底物低碳醇需要采用流加方式加入体系 ,石油醚是最适宜的有机溶剂 ,脂肪酸与醇的碳链越长 ,越易于酯化 ;固定化脂肪酶对直链醇的选择性优于支链醇。以石油醚为有机溶剂 ,在反应温度为 40℃、pH值为 7时 ,硬脂酸与甲醇的酯化率达 95 % ;反应后期应除去体系中的水以避免酶失活。固定化酶间歇催化油酸与甲醇的酯化时 ,重复使用 1 5次 (每次 2 4h) ,其操作半衰期约为 360h。 相似文献
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南极假丝酵母脂肪酶发酵条件优化及酶学性质 总被引:7,自引:0,他引:7
分别用摇瓶和15L发酵罐,对南极假丝酵母产胞外脂肪酶的培养基成分和操作条件进行了实验研究。得到最优的培养基组成为:豆粉40g/L,淀粉15g/L,豆油5mL/L,K2HPO4g/L,MgsO4·7H2O1g/L,Tween-800.1%,酵母膏5g/L;操作条件为:温度24℃,初始pH值为6.0,通气量为10.0L/min。在此培养条件下,发酵周期缩短至54h。由15L发酵罐生产的酶液酶活达到19.2U/mL。酶液在pH值为4.0~6.0和7.5~9.0范围内较稳定,其最适宜pH值范围为6~8.5;70℃时酶的催化活性最大.在40~70℃的温度范围内保持1h后残留酶活为60%。 相似文献
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硫酸铵-丙酮协同沉淀法纯化南极假丝酵母产脂肪酶 总被引:2,自引:0,他引:2
采用硫酸铵-丙酮协同沉淀法,对南极假丝酵母产脂肪酶(CALB)进行了分离纯化研究.经正交实验确定纯化工艺为:向酶液中加入硫酸铵至饱和度45%的同时加入0.3倍酶液体积的丙酮;离心后再向上清液中加入硫酸铵至饱和度75%,分相后,相界面处沉淀即为脂肪酶粗品.经分离纯化后,酶活回收率为54%、纯化倍数为2.72. 相似文献
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固定化Candida sp.99-125脂肪酶催化大豆油合成脂肪酸乙酯 总被引:1,自引:0,他引:1
探讨了酶法合成脂肪酸乙酯作为生物柴油的可行性. 以大豆油和乙醇为原料,利用本实验室自制的固定化Candida sp. 99-125脂肪酶催化反应,深入研究水含量、溶剂量、脂肪酶量及反应温度等因素对酶法合成脂肪酸乙酯的影响. 结果表明,以大豆油质量为基准,在水含量为 12.5%(w)、溶剂正己烷为3 mL/g、脂肪酶量为20%(w)、温度40℃的优化反应条件下,3次流加乙醇,170 r/min摇瓶反应,12 h后可以达到96.8%的最高酯得率. 进一步研究表明,在此优化反应条件下,连续使用14批脂肪酶酯得率可保持70%以上. 相似文献
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Wax esters were synthesized in a solvent free system catalyzed by immobilized lipase from Candida sp. 99-125, with oleic acid and cetyl alcohol. The effects of substrate molar ratio, lipase dosage and water removal were investigated in a 50 ml flask incubated in a thermostatic cultivation cabinet. The optimized conditions were: temperature 40 ℃, shaking at 170 r·min-1, acid/alcohol molar ratio 1:0.9, lipase dosage in 10% (by mass) of oleic acid, and open reaction for water removal. As a result, the conversion rate reached 98% for reaction of 8 h. The volume of reactor was scaled up to 1 L three-neck flask. The optimized parameters were: 200 r·min-1 agitation speed, 2.5% (by mass) lipase dosage, others were the same as the parameters described above. The conversion rate reached 95% for reaction of 24 h. The lipase retained 46% conversion rate after reuse for 6, 7 batches. The products were purified by removing remained cetyl alcohol and fatty acids with ethanol and saturated sodium carbonate so-lution, respectively. The purity of the wax ester, cetyl oleate, was 96%. The physical and chemical properties of cetyl oleate were tested and compared with those of jojoba oil. The results show that the product cetyl oleate has great potential to use as the substitute of natural jojoba oil. 相似文献
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The stability of the immobilized lipase from Candida sp. 99–125 during biodiesel production was investigated. The lipase was separately incubated in the presence of various reaction components such as soybean oil, oleic acid methyl ester, n‐hexane, water, methanol, and glycerol, or the lipase was stored at 60, 80, 100 and 120 °C. Thereafter the residual lipase activity was determined by methanolysis reaction. The results showed that the lipase was rather stable in the reaction media, except for methanol and glycerol. The stability study performed in a reciprocal shaker indicated that enzyme desorption from the immobilized lipase mainly contributed to the lipase inactivation in the water system. So the methanol and glycerol contents should be controlled more precisely to avoid lipase inactivation, and the immobilization method should be improved with regard to lipase desorption. 相似文献
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传统的酯化或转酯化产品的合成通常需要高温、强酸、强碱等相对苛刻的条件,脂肪酶由于其生物催化过程具有高效、高选择性、条件温和和环境友好等特点,在化学品的合成中越来越受到人们的关注。本课题组开发了一种可以用于酯类合成的新脂肪酶,并且实现了该酶的工业化生产。来源于Candida sp. 99-125的脂肪酶在非水相中对酯化和转酯化反应具有高效的催化活性和稳定性。本文介绍了该脂肪酶的发酵生产及其在中长链脂肪酸酯、二元酸酯、维生素A棕榈酸酯、手性化合物以及生物柴油等多种化学品的合成中的应用。 相似文献
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Donato A. G. Aranda Rafael T. P. Santos Neyda C. O. Tapanes André Luis Dantas Ramos Octavio Auqusto C. Antunes 《Catalysis Letters》2008,122(1-2):20-25
This work deals with esterification of palm fatty acids to produce biodiesel in a batch reactor, using homogeneous acid catalysts,
evaluating the effect of the alcohol used, presence of water, type and concentration of catalysts. Methanesulfonic and sulfuric
acid were the best catalysts. Reaction with methanol showed greater yields. It was showed very clearly that the presence of
water in the reaction medium showed a negative effect in the reaction velocity. Kinetic parameters were estimated and molecular
modeling was performed. Protonation of the carboxylic moiety of the fatty acid were defined as rate determinant step for the
reaction. 相似文献
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Li Deng Tianwei Tan Fang Wang Xuebing Xu 《European Journal of Lipid Science and Technology》2003,105(12):727-734
A lipase preparation developed from Candida sp. 99‐125 was used for fatty acid alkyl ester synthesis by both enzymatic esterification of fatty acids, and transesterification of oils and fats. The lipase preparation was chosen based on screening of lipases from commercial sources as well as those produced in the laboratory. The effects of enzyme dosage, solvent types, water absorbent additions, inhibition of short‐chain alcohols, alcohol and acid types, molar ratio of substrates, and reusability of the lipase preparation in esterification were studied. Degree of esterification between oleic acid and methanol under optimal conditions reached 92%. Purity of the methyl ester after washing with water and distillation was 98%. Half‐life of the lipase preparation was calculated to be approximately 340 h. For transesterification of rapeseed oil with the same lipase preparation, the amount of methanol and mode of methanol addition to the reaction were also conducted. Transesterification of the oil with stepwise methanol addition reached 83% after 36 h reaction time. 相似文献
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The non-edible crude rice bran oil was extracted from white rice bran, and then was catalyzed by immobilized lipase for biodiesel production in this study. The effects of water content, oil/methanol molar ratio, temperature, enzyme amount, solvent,number of methanol added times and two-step methanolysis by using Candida sp. 99-125 as catalyst were investigated. The optimal conditions for processing 1 g rice bran oil were: 0.2 g immobilized lipase, 2 ml n-hexane as solvent, 20% water based on the rice bran oil mass, temperature of 40 °C and two-step addition of methanol. As a result, the fatty acid methyl esters yield was 87.4%. The immobilized lipase was proved to be stable when it was used repeatedly for 7 cycles. 相似文献