基于响应面设计脂肪酶Novo435催化合成甘油二酯的工艺优化

以甘油、油酸为原料,优化在无溶剂体系中以固定化脂肪酶Novo435催化合成甘油二酯（diglyceride,DAG）的工艺。系统考察底物摩尔比（油酸／甘油）、反应温度、时间和加酶量等因素对油酸转化率和甘油二酯含量影响的基础上,利用响应面试验设计优化各主效因子,并经回归分析获得最优的工艺条件。所得最优条件：油酸与甘油底物摩尔比2．27、反应温度48．14℃、反应时间6．3h、加酶量1．68％。在此条件下,实验测得油酸转化率为45．42％,甘油二酯质量分数为70．01％,与响应面模型预测值吻合。     

脂肪酶二步法催化鱼油下脚料富集DHA

采用Pseudomonas sp．脂肪酶水解,Geotrichum sp．脂肪酶选择性酯化的两步法显著提高游离脂肪酸（FFA）中二十二碳六烯酸（DHA）的含量。通过筛选合适的底物醇,优化水解和选择性酯化反应条件达到富集DHA的目的。结果表明月桂醇为选择性酯化的最适底物醇。确定的最佳水解条件：4g反应底物,m（水）／m（粗鱼油）=1,1000 U Pseudomonas sp．脂肪酶,40℃,搅拌速度200r／min,反应24h;最佳酯化条件：3g反应底物,n（FFA）／n（醇）=1／2,1000 U固定化Geotrichum sp．脂肪酶,1g正己烷,30℃,200r／min搅拌,反应20h。经过水解和一次选择性酯化反应后,DHA含量从原料粗鱼油中的18．9％提纯到72．8％;经二次选择性酯化后,DHA含量上升到92％。脂肪酶水解-选择性酯化的两步法是富集DHA的有效方法。     

脂肪酶的固定化及其性质研究

采用吸附与交联相结合的方法国定化脂肪酶,研究了脂肪酶固定化的工艺条件,并考察了固定化脂肪酶的催化性能和稳定性。试验结果表明,WA20树脂固定化脂肪酶的最适条件是：酶液pH7．0、给酶量300IU／g树脂、固定时间8h,所得固定化脂肪酶的活力约为165IU／g树脂;固定化酶稳定性较高,在冰箱内贮存6个月活力没有下降,操作半衰期约为750h,而未用戌二醛文联的固定化脂肪酶操作半衰期仅约290h;固定化脂肪酶催化橄榄油水解的最适条件是：PH8．0、温度55℃、底物浓度60％（V／V）、搅拌转速500r／m。     

叔丁醇体系中复合酶催化餐饮废油制备生物柴油工艺优化

以叔丁醇为反应体系,研究固定化Novozym 435 和Lipozyme TLIM 脂肪酶协同催化餐饮废油合成生物柴油.采用5 因素5 水平响应面法优化工艺参数,最佳工艺条件为:复合酶用量4%( wt.)、复合酶配比1:1(w/w),油/醇摩尔比1:5,反应温度50℃,叔丁醇用量50%(油体积比v/v).在此条件下反应10 h,生物柴油转化率为83.65 %.复合酶操作稳定性较高,重复使用10 个批次,生物柴油转化率仍保持在80% 以上.     

蚕丝固定化脂肪酶的研究

研究了蚕丝固定化脂肪酶的工艺条件,并考察了固定化脂肪酶的稳定性。试验结果表明：蚕丝与对-β-硫酸酯乙砜基苯胺(SESA)进行反应的最适条件是PH=10．8,SESA：2．0g／g蚕丝,反应生成的对氨基苯磺酰乙基蚕丝(ABSE-蚕丝)经重氮化后与脂肪酶偶联的最适条件是：pH=7．5,偶联时间>10h。加酶量为168～308u／g蚕丝时,所得固定化脂肪酶活力为106～160u√g蚕丝．此时固定化冀的活力回收率较高(>52％)。固定化脂肪酶稳定性较高．其操作半衰期约为250h。     

离子液体中固定化脂肪酶催化拆分（±）-薄荷醇

以自制的平均粒径为4．5um磁性高分子微球为载体,采用离子交换法固定化Candida rugosa脂肪酶,催化（±）-薄荷醇的酯化反应,以考察反应时间、pH、反应温度、水活度等因素对酶的固定化以及酯化反应的影响。在固定化反应150min、pH5．0、酯化反应温度30℃、固定化酶的水活度为0．78的条件下,所制备的固定化脂肪酶在离子液体[bmim]PF6中催化拆分（±）-薄荷醇的效果最佳,与游离酶相比固定化脂肪酶的立体选择性有很大的提高,对映体过量率可达93％,对映体选择值为35。     

脂肪酶协同催化猪油合成生物柴油工艺研究

探讨了以乙酸甲酯为酰基受体两种脂肪酶协同催化猪油转酯合成生物柴油的工艺条件。首先利用单因子试验确定2种固定化脂肪酶Novozym435、Lipozyme TLIM单独作为催化剂时的最佳酶用量为40％,反应温度为50℃,乙酸甲酯用量为14（相对于油的摩尔比）。在此基础上,采用3因素5水平和3个中心点的中心组分旋转设计法研究了上述2种脂肪酶协同使用时脂肪酶用量（g/g）、混合酶的配比（%/%）以及乙酸甲酯用量诸因素共同作用对转酯反应转化率的影响。优化后的反应条件为：总酶用量为40％,混合酶配比为50/50,乙酸甲酯用量为14,在该条件下甲酯得率可达97.6％,比同质量的Novozym435、Lipozyme TLIM的催化活性分别高出7.6％、22.3％。表明脂肪酶协同催化猪油合成生物柴油工艺可以较好地提高甲酯得率,并且节约生产成本。     

离子液体中固定化脂肪酶催化拆分（±）-薄荷醇

以自制的平均粒径为4．5um磁性高分子微球为载体,采用离子交换法固定化Candida rugosa脂肪酶,催化（±）-薄荷醇的酯化反应,以考察反应时间、pH、反应温度、水活度等因素对酶的固定化以及酯化反应的影响。在固定化反应150min、pH5．0、酯化反应温度30℃、固定化酶的水活度为0．78的条件下,所制备的固定化脂肪酶在离子液体[bmim]PF6中催化拆分（±）-薄荷醇的效果最佳,与游离酶相比固定化脂肪酶的立体选择性有很大的提高,对映体过量率可达93％,对映体选择值为35。     

超声波辅助下脂肪酶催化高酸值废油脂制备生物柴油

探讨了超声波辅助条件下脂肪酶催化高酸值废油脂转化为生物柴油的反应。来源于Aspergillus oryzae和Candida antarctica的固定化脂肪酶,在超声波辅助下,对高酸值废油脂转化为生物柴油具有高的催化活性。以来自于C.antarctica的固定化脂肪酶Novozym435为催化剂,以酸价为157mg KOH/g的高酸值废油脂为原料在超声波辅助下与丙醇反应,在脂肪酶用量为油质量的8%、初始醇油摩尔比为3∶1、反应温度控制在40~45℃、超声波频率和功率分别采用28kHz和100W的条件下,反应50min转化率达到94.86%。在此条件下,不同碳原子数(C1~C5)的直链和支链醇均有较高的转化率,在短链醇的选择上具有宽广的适应性。超声波还减少了反应产物和反应体系中其他黏性杂质在固定化脂肪酶表面的吸附,回收的Novozym435相较单纯机械搅拌条件下回收的外观干净、分散良好无结块现象、易于洗涤和再次利用,具有良好的操作稳定性。     

生物法合成维生素C棕榈酸酯

研究了不同的脂肪酶在有机溶剂体系中催化合成L-维生素C棕榈酸酯的反应。针对维生素C在有机溶剂中溶解度较低这一问题,对催化合成维生素C棕榈酸酯反应的脂肪酶和反应介质进行比较,同时对影响合成维生素C棕榈酸酯反应的因素（温度、底物浓度、底物摩尔比、反应时间和酶量等）进行探讨,优化了反应条件：在10mL的丙酮中,1.094g棕榈酸与0.107g维生素C在酶量为20％（W/W, 固定化酶/维生素C）的固定化脂肪酶催化下,初始含0.4nm分子筛20%,温度为60℃,转速为200r/min,反应48h转化率可以达到80%,产物维生素C棕榈酸酯的浓度可达20g/L。     

Lipase catalyzed methanolysis to produce biodiesel: Optimization of the biodiesel production

A lipase from Candida sp., suitable for transesterification of fats and oils to produce fatty acid methyl ester (FAME), was immobilized on a cheap cotton membrane, in this paper. The conversion ratio of salad oil to biodiesel could reach up to 96% with the optimal reaction conditions. Continuous reaction in a fixed bed reactor was also investigated. A three-step transesterification with methanol (methanolysis) of oil was conducted by using a series of nine columns packed with immobilized Candida sp. 99–125 lipase. As substrate of the first reaction step, plant or waste oil was used together with 1/3 molar equivalent of methanol against total fatty acids in the oil. Mixtures of the first- and second-step eluates and 1/3 molar equivalent of methanol were used for the second- and third-reaction steps. A hydrocyclone was used in order to on-line separate the by-product glycerol after every 1/3 molar equivalent of methanol was added. Petroleum ether was used as solvent (3/2, v/v of oil) and the pump was operated with a flow rate of 15 L/h giving an annual throughput of 100 t. The final conversion ratio of the FAME from plant oil and waste oil under the optimal condition was 90% and 92%, respectively. The life of the immobilized lipase was more than 10 days. This new technique has many strongpoints such as low pollution, environmentally friendly, and low energy costs.     

Characteristics of immobilized lipase-catalyzed hydrolysis of olive oil of high concentration in reverse phase system

Candida rugosa lipase immobilized by adsorption on swollen Sephadex LH-20 could almost completely hydrolyze 60% (v/v) olive oil in isooctane. Kinetic analysis of the lipase-catalyzed hydrolysis reaction was found to be possible in this system. Amount of fatty acids produced was linearly proportional to the enzyme concentration of 720 mug/g wet gel. The specific enzyme activity was 217 units/mg protein at 60% (v/v) olive oil concentration. When the initial rate is plotted versus concentration of olive oil, this system did not follow Michaelis-Menten kinetics. Maximum activity was obtained at pH 7, but optimum temperature shifted towards higher one with the increase of olive oil concentration. Among the various chemical compounds tested, Hg(2+) and Fe(2+) inhibited the lipase seriously. As the concentration of olive oil increased, the rate of the hydrolysis also increased, but degree of the hydrolysis was observed to decrease. The supply of water from the inside of the gel to the surface of the gel was the main factor for the control of the rate of hydrolysis in batch hydrolysis. The immobilized lipase was used to hydrolyze olive oil two times. Achievement of chemical equilibrium took a longer time with the addition of water and the degree of hydrolysis decreased in the second consecutive trial. After the second hydrolysis trial, the gels were regenerated in a packed column first by eluting out both residual fatty acids around the gel particles and the accumulated glycerol with ethanol and then with 0.05M phosphate buffer, pH 7. The immobilized lipase on the regenerated gel showed the same hydrolysis activity as the original one.     

Lipolytic activity of suspended and membrane immobilized lipase originating from indigenous Burkholderia sp. C20

In this work, a simple, inexpensive, and efficient method of preparing immobilized lipase is presented. The lipase originating from a newly isolated indigenous strain Burkholderia sp. C20 was immobilized onto cellulose nitrate (CN) membrane via filtration. The CN-immobilized lipase was able to retain 60% of its original activity after repeated uses for nine times. The thermal stability of the lipase was also slightly improved after immobilization. The optimal reaction conditions of CN-lipase were pH 9.0 and 55 degrees C, which are similar to those for the suspended lipase. Both suspended and immobilized lipase could hydrolyze the six oil substrates examined, while immobilized lipase displayed less specificity over the oil substrates. Kinetic analysis shows that the dependence of lipolytic activity of both suspended and immobilized lipase on oil substrate concentration can be described by Michaelis-Menten model with good agreement. The estimated kinetic constants for suspended lipase (v(max)=243.9 U/mg, K(m)=0.024 mM) and immobilized lipase (v(max)=32.8 U/mg, K(m)=5.61 mM) were quite different. Employment of immobilization seemed to result in a decrease in v(max) and an increase in K(m), most likely due to the mass transfer resistance arising from formation of micelles during the lipase immobilization process.     

Enzymatic coproduction of biodiesel and glycerol carbonate from soybean oil and dimethyl carbonate

The enzymatic coproduction of biodiesel and glycerol carbonate by the transesterification of soybean oil was studied using lipase as catalyst in organic solvent. To produce biodiesel and glycerol carbonate simultaneously, experiments were designed sequentially. Enzyme screening, the molar ratio of dimethyl carbonate (DMC) to soybean oil, reaction temperature and solvent effects were investigated. The results of enzyme screening, at 100 g/L Novozym 435 (immobilized Candida antarctica lipase B), biodiesel and glycerol carbonate showed conversions of 58.7% and 50.7%, respectively. The optimal conditions were 60 °C, 100 g/L Novozym 435, 6.0:1 molar ratio with tert-butanol as solvent: 84.9% biodiesel and 92.0% glycerol carbonate production was achieved.     

Solvent-free synthesis of glyceryl ferulate using a commercial microbial lipase

A process was optimized for the enzymatic synthesis of glyceryl ferulate with a yield of up to 96% using a vacuum-rotary evaporation strategy under following conditions: 15 mmol glycerol, 1.5 mmol ethyl ferulate, 170 mg Candida antarctica lipase, at 60°C for 10 h and under a vacuum of 10 mm Hg. The immobilized lipase can be used 10 times.     

Conversion of acid oil by-produced in vegetable oil refining to biodiesel fuel by immobilized Candida antarctica lipase

Acid oil, which is a by-product in vegetable oil refining, mainly contains free fatty acids (FFAs) and acylglycerols, and is a candidate of materials for production of biodiesel fuel. A mixture (acid oil model) of refined FFAs and vegetable oil was recently reported to be converted to fatty acid methyl esters (FAMEs) at >98% conversion by a two-step reaction system comprising methyl esterification of FFAs and methanolysis of acylglycerols using immobilized Candida antarctica lipase. The two-step system was thus applied to conversion of acid oil by-produced in vegetable oil refining to biodiesel fuel. Under similar conditions that were determined by using acid oil model, however, the lipase was unstable and was not durable for repeated use. The inactivation of the lipase was successfully avoided by addition of excess amounts of methanol (MeOH) in the first-step reaction, and by addition of vegetable oil and glycerol in the second-step reaction. Hence, the first-step reaction was conducted by shaking a mixture of 66 wt% acid oil (77.9 wt% FFAs, 10.8 wt% acylglycerols) and 34 wt% MeOH with 1 wt% immobilized lipase, to convert FFAs to their methyl esters. The second-step reaction was performed by shaking a mixture of 52.3 wt% dehydrated first-step product (79.7 wt% FAMEs, 9.7 wt% acylglycerols), 42.2 wt% rapeseed oil, and 5.5 wt% MeOH using 6 wt% immobilized lipase in the presence of additional 10 wt% glycerol, to convert acylglycerols to FAMEs. The resulting product was composed of 91.1 wt% FAMEs, 0.6 wt% FFAs, 0.8 wt% triacylglycerols, 2.3 wt% diacylglycerols, and 5.2 wt% other compounds. Even though each step of reaction was repeated every 24 h by transferring the immobilized lipase to the fresh substrate mixture, the composition was maintained for >100 cycles.     

Immobilization of Candida rugosa lipase by cross-linking with glutaraldehyde followed by entrapment in alginate beads

Candida rugosa lipase was immobilized by first cross-linking with glutaraldehyde and then entrapping in calcium alginate beads. The presence of 2-propanol during cross-linking markedly improved the enzyme activity and activity recovery. Maximal enzyme activity (2.1?mmol?h^?1?g^?1 immobilized conjugate, wet weight) and activity recovery (117%) were observed at 30% (v/v) 2-propanol for hydrolysis of olive oil, which were 1.7 and 2.0 times higher than those of the immobilized enzyme prepared in the absence of 2-propanol. The half-life of the immobilized lipase prepared by entrapment after cross-linking in 30% 2-propanol was 1.6 times higher than that prepared by entrapment of the native lipase without cross-linking and 2-propanol pretreatment. The enantioselectivity of the former was 11 times higher than that of the latter for hydrolysis of racemic ketoprofen ethyl ester.     

Conversion of Soybean Oil to Biodiesel Fuel Using Lipozyme TL IM in a Solvent-free Medium

The conversion of soybean oil to biodiesel fuel was investigated in the presence of a lipase from Thermomyces lanuginosus (commercially called Lipozyme TL IM) in a solvent-free medium. The lipase was inactivated when more than 1.5 molar equivalent of methanol was added to the oil mixture. To fully convert the oil to its corresponding methyl esters, the reaction was performed successfully by a three-step addition of 1 molar equivalent of methanol and under the optimized conditions (40°C, 150 rpm, 10% enzyme quantity based on oil weight), the maximum methyl ester (ME) yield was 98% after 12 h reaction. By-product glycerol had a negative effect on enzymatic activity and iso-propanol was found to be effective for glycerol removal, in the presence of which lipase expressed relatively high activity and more than 94% of the ME yield was maintained after being used repeatedly for 15 batches.     

Optimization of lipase pretreatment prior to lipase immobilization to prevent loss of activity

In our previous work, a method of pretreating lipase was developed to prevent loss of its activity during covalent immobilization. In this study, Rhizopus oryzae lipase was pretreated before immobilization and then immobilized on a silica gel surface. The effects of the various materials and conditions used in the pretreatment stage on the activity of immobilized lipase were investigated. Immobilized lipase pretreated with 0.1% of soybean oil had better activity than those pretreated with other materials. The optimal temperature, agitation speed, and pretreating time for lipase pretreatment were determined to be 40 degrees C, 200 rpm, and 45 min, respectively. The activity of immobilized soybean oil pretreated lipase was 630 U/g matrix, which is 20 times higher than that of immobilized non-pretreated lipase. In addition, immobilized lipase activity was maintained at levels exceeding 90% of its original activity after 10 reuses.