微水体系中荧光假单胞菌脂肪酶催化合成单甘酯

研究了无溶剂微水体系中荧光假单胞菌脂肪酶 (PFL)催化油脂甘油解合成单甘酯的反应因素以及多温程非均相固液反应对单甘酯产率的影响。以初始体系最低共熔点 (PFL)取代临界温度学说中的油脂初熔点 ,通过考察不同IEP体系的甘油解 ,发现PFL酶促油脂甘油解时存在碳链基质特异性的函数关系 ,即反应物油脂中饱和碳残基的质量百分含量 (C₁₆+C₁₈)与单甘酯产率间符合以下多项式:Y =- 0.0006X³ +0.0592X²-0.8909X+26.753(13%<X<76.5%),式中X为C₁₆+C₁₈,Y为40℃时等温反应条件下的单甘酯产率。IEP为40℃时,最适等温反应条件如下：加水量3%～4.5%,加酶量为500μ/g油酯摩尔比1：2.5-5.0(油酯：甘油)反应温度40℃.实验条件下多步等程序降温反应48h后单甘酯最高产率为81.4%.     

酶法破碎裂殖壶菌提取胞内油脂

采用酶法破碎裂殖壶菌提取胞内油脂,进行单因素实验和正交实验优化酶解反应条件,酶解反应的影响因素主次顺序依次为酶用量、温度、时间、pH,最佳酶解工艺参数:55 ℃、pH 9.5、搅拌反应2.5 h、酶用量为菌体生物量的2%.在该条件下,胞内油脂的提取量高达(81.53±0.33) g/L,过氧化值仅为0.15,酸价为0.24.     

非水溶剂中Rhizopus arrhizus脂肪酶催化合成三种酯的最佳条件(英文)

以少根根霉 (Rhizopusarrhizus)脂肪酶为催化剂 ,有机溶剂为反应介质 ,合成了 3种短链脂肪酸酯 .研究了反应温度、溶剂、底物浓度、底物摩尔比、吸水剂用量等因素对酯化反应的影响 .确定了3种酯的最佳合成条件 :(1)己酸乙酯 :反应温度为 4 0℃ ,环己烷为溶剂 ,0 2 5mol L底物浓度 ,酸醇摩尔比为 1∶1 2 ;(2 )乙酸异丙酯 :5 0℃ ,环己烷为溶剂 ,0 15mol L底物浓度 ,摩尔比为 1∶1;(3)乙酸异戊酯 :5 0℃ ,异辛烷为溶剂 ,0 2 0mol L底物浓度 ,摩尔比为 1∶1.三种酯合成时均需 0 12 5g ml的0 5nm分子筛为吸水剂 ,在 8h后 ,合成酯转化率达到 97%～ 99% .     

Candidasp．99-125脂肪酶催化猪油酸解合成1，3-二油酸-2-棕榈酸甘油三酯

人乳脂是一种在甘油骨架Sn-2位上富含棕榈酸（C16：0）的结构酯。经分析可知,猪油中棕榈酸主要分布在甘油酯的Sn-2位,可作为制备1,3-二油酸-2-棕榈酸甘油三酯（OPO）的原料。以Candidasp．99—125脂肪酶作催化剂,以猪油和油酸为原料,通过正交试验对无溶剂体系中酸解合成OPO的工艺条件进行研究,得到最适反应条件：猪油与油酸的质量比为1：2．0,酶用量为总底物质量的10％,反应温度40℃,反应时间4h。在该反应条件下,经酸解合成的产物三甘酯中,Sn-2C16：0的含量大于70％,占总脂肪酸中棕榈酸含量的93％以上,并合有43％以上的OPO。     

最新专利文摘

CN101608131 一种无副产甘油的生物柴油制备方法 本发明公开了一种无副产甘油的生物柴油制备方法,将酯交换试剂与动植物油脂混合,在催化剂存在下,30～450℃反应2～18h,其中酯交换试剂与动植物油脂的质量比为1：1～30：1,催化剂添加量为动植物油脂质量的1％～30％,反应器内压力为0．05～30MPa;过滤除去催化剂并蒸馏除去过量的酯交换试剂,产品即为生物柴油;反应产物无副产物甘油。     

固定化全细胞催化可再生油脂合成生物柴油的稳定性

酶法合成生物柴油具有反应条件温和、醇用量小、无污染物排放、产物易分离回收等优点,越来越得到关注。全细胞催化剂,无需酶的提取和纯化,减少了酶活损失,有望大幅降低生产成本;Rhizopus oryzae IFO4697全细胞可以有效催化植物油脂合成生物柴油,进一步提高全细胞在催化植物油脂甲醇解制备生物柴油过程中的稳定性,对于工业放大具有重要意义。本实验对固定化全细胞Rhizopus oryzae IFO4697催化植物油脂合成生物柴油的稳定性进行了系统地研究,结果表明:反应体系水含量对于全细胞催化剂的反应活性和催化稳定性有重要影响,5%～15%含水量适宜;研究范围内,载体粒度及干燥方式对稳定性影响不显著;经过戊二醛交联后,全细胞催化油脂甲醇解反应的稳定性显著提高,1200h反应后,仍然可以保持75%的生物柴油得率;真空抽滤直接回用的方式有利于稳定性的保持。在优化条件下,回用20个批次,生物柴油得率可维持在80%。     

多不饱和脂肪酸结构酯酶法合成工艺的研究

运用低温溶剂结晶法富集藻油中多不饱和脂肪酸,最佳结晶条件为-20℃静置结晶72h,丙酮溶剂与藻油的体积质量比30:1(v/wt,m L/g)。在此条件下,藻油sn-2位的脂肪酸组成中PUFA含量从74.8%提高到92.2%。以富集后的藻油和癸酸为底物,合成富含PUFA的结构酯,优化了酸解反应条件:以脂肪酶Ls-20为催化剂,以正己烷为反应介质,底物藻油与癸酸的摩尔比1:10,酶用量10%(占底物藻油的质量百分比),氮气保护,40℃,180rpm反应25h。利用低温溶剂结晶法分离纯化酸解产物,在丙酮与油脂的体积质量比1.6;1(v/wt,m L/g),-20℃下结晶24h,结构酯回收率达到78.7%。     

超声辅助酶促合成丙二酸单对硝基苄酯

为了研究超声对固定化脂肪酶Novozym 435催化合成丙二酸单对硝基苄酯反应的影响。对超声辅助酶促酯化反应条件进行了优化,确定最佳反应条件:以甲苯为溶剂,固定化脂肪酶Novozym 435质量浓度为3.0 g/L,对硝基苄醇质量浓度为4.0 g/L,反应温度为30℃,反应时间为5 h,超声声强为0.8 W/cm2,超声频率为20 k Hz,丙二酸单对硝基苄酯收率为89.7%。与振荡水浴条件相比,超声辅助酶催化反应能强化传质,在反应温度降低15℃,时间缩短3 h和固定化酶浓度减少1.5 g/L的同时,产物收率增加了18.2%。超声作用下,Novozym 435重复使用性能较佳,应用于酯化反应8次后,丙二酸单对硝基苄酯收率为69.3%。     

最新专利文摘

利用废动植物油生产生物柴油的工艺本发明是在酸性催化剂存在的条件下 ,将各种不同酸值的废动植物油脂进行醇解和酯化反应 ;然后再分离出非产品部分的多余成分 ,得粗制产品 ;在粗制产品中加入含纯碱10 %的饱和食盐水进行中和反应 ,得到水洗粗酯 ,最后 ,在水洗粗酯中加入工业纯碱后进行加热蒸馏 ,收集气相温度为2 2～ 32 0℃的馏分 ,得成品生物柴油。本发明具有原料来源广、生产工艺简单、成本低、无污染、使用安全可靠的特点 ,其生产过程中无污水的排放 ,符合目前国内环保要求。采用本发明工艺生产的生物柴油已通过中试验证 ,其使用性能良好…     

酶促反应合成棕榈酸Vc酯

讨论了以黑曲霉脂肪酶为催化剂,以抗坏血酸和棕榈酸甲酯为底物的酯交换反应及其影响因素。考察了在摇床速度为200r/min,叔丁醇为溶剂下,底物的摩尔比、温度、脂肪酶浓度、时间、含水量对转化率的影响。结果表明,底物棕榈酸甲酯与Vc的摩尔比为1.3:1.0、反应温度为36℃、反应时间为24h、脂肪酶浓度为15%、含水量为1%时,Vc的转化率为23%。合成的棕榈酸Vc酯,无需和底物分离,可以直接作为油脂食品的添加剂。     

Continuous enzymatic transesterification of sesame oil and a fully hydrogenated fat: effects of reaction conditions on product characteristics

An immobilized lipase from Thermomyces lanuginosus (TL IM) was employed to mediate the continuous transesterification of sesame oil and fully hydrogenated soybean oil (FHSBO) in a packed-bed reactor operating at 70 degrees C. Reactions between sesame oil (rich in LLL (15.97%), LOL (31.56%), and OLO (21.15%) [L = linoleic; O = oleic]) and the fully hydrogenated fat ((73.7% SSS, 26.3% SPS) [S = stearic; P = palmitic]) produced semi-solid fats. These products are complex mixtures of triacylglycerol (TAG) species whose compositions depend on reaction conditions. The dependence of the steady state product TAG profile on space time was determined for four initial weight ratios of sesame oil to hydrogenated fat (90:10, 80:20, 70:30, and 60:40). Except for the trial involving a weight ratio of sesame oil to FHSBO of 60:40, near equilibrium conditions were achieved at space times of 30 min-1 h. The chemical, physical, and functional properties of the product semi-solid fats were characterized. The predominant TAG species in the quasi-equilibrium products obtained from the mixture initially containing 90% (w/w) sesame oil and 10% FHSBO were LOL (26.22%) and OLO (21.92%). For transesterification of 80% sesame oil and 20% FHSBO, the major product species were OOP (21.27%), LOL (17.46%), and OLO (13.93%). OOP (24.38%) was the major product for reaction of 70% sesame oil with 30% FHSBO. Appropriate choices of reaction conditions and initial ratios of sesame oil to FHSBO lead to TAG with melting profiles and solid fat contents (SFC) similar to those of a variety of commercial products.     

Hydrolysis of crambe oil by enzymatic catalysis: An evaluation of the operational conditions

Abstract

In this work, the enzymatic hydrolysis of the crambe oil by using a commercial immobilized lipase Lipozyme RM IM was evaluated. The effect of the operational conditions, such as temperature, water/oil molar ratio, enzyme/substrate mass ratio and stirring speed were assessed based on the experimental designs. The experiments were performed in a closed and batch system with controlled temperature and stirring speed. In addition, the kinetics of the process was studied in the best operational conditions, wherein the experimental data were obtained and described by a mathematical model. The influence of the operational conditions was assessed based on the measured values of the free fatty acids (FFA) produced by the enzymatic hydrolysis. In 4?h of reaction, a yield of 42.6% was observed and the most significant operational conditions were the enzyme/substrate mass ratio and stirring speed. By the kinetic investigation, an initial reaction rate of 3.5?×?10⁴?mol?mL^?1?h^?1 and a maximum yield of 74% were observed after 40?h of reaction (in the equilibrium condition). The mathematical model was not only able to adequately describe the experimental data of FFA concentrations profiles but also showed predictive capacity to independents assays in different operational conditions. Therefore, based on the simulation analysis of the enzymatic hydrolysis of the crambe oil, the model can be useful for process optimization and phenomenological studies.     

海滨锦葵油制备生物柴油工艺条件优化

以海滨锦葵油为原料制备生物柴油。通过单因素试验及正交试验研究了反应温度、催化剂用量、醇油摩尔比、反应时间、搅拌强度等因素对酯交换率的影响。结果表明,在试验范围内各影响因素对酯交换率作用的大小依次为：搅拌强度＞催化剂用量＞醇油摩尔比＞反应时间＞反应温度。海滨锦葵油制备生物柴油的最佳工艺参数为：搅拌强度为1800r.min-1,催化剂KOH用量为海滨锦葵油质量的1%,醇油摩尔比6/1,反应时间60min,反应温度65℃,在该工艺条件下,酯交换反应三次,酯交换率达到97.8%。     

Direct preparation of biodiesel from rapeseed oil leached by two-phase solvent extraction

A new method which coupled the two-phase solvent extraction (TSE) with the synthesis of biodiesel was studied. Investigations were carried out on transesterification of methanol with oil-hexane solution coming from TSE process in the presence of sodium hydroxide as the catalyst. Biodiesel (fatty acid methyl esters) were the products of transesterification. The influential factors of transesterification, such as reaction time, catalyst concentration, mole ratio of methanol to oil and reaction temperature were optimized. The results showed that the optimal reaction parameters were sodium hydroxide concentration 1.1% by weight of rapeseed oil, mole ratio of methanol to oil 9:1, reaction time 120 min, and reaction temperature 55-60 degrees C. Under these conditions, the TG conversion would rise up to 98.2%. Based on the new method, biodiesel production process could be simplified and the biodiesel cost could be reduced.     

Production of extremely pure diacylglycerol from soybean oil by lipase-catalyzed glycerolysis

Research work was objectively targeted to synthesize highly pure diacylglycerol (DAG) with glycerolysis of soybean oil in a solvent medium of t-butanol. Three commercial immobilized lipases (Lipozyme RM IM, Lipozyme TL IM and Novozym 435) were screened, and Novozym 435 was the best out of three candidates. Batch reaction conditions of the enzymatic glycerolysis, the substrate mass ratio, the reaction temperature and the substrate concentration, were studied. The optimal reaction conditions were achieved as 6.23:1 mass ratio of soybean oil to glycerol, 40% (w/v) of substrate concentration in t-butanol and reaction temperature of 50 °C. A two-stage molecular distillation was employed for purification of DAG from reaction products. Scale-up was attempted based on the optimized reaction conditions, 98.7% (24 h) for the conversion rate of soybean oil, 48.5% of DAG in the glycerolysis products and 96.1% for the content of DAG in the final products were taken in account as the results.     

Optimization of alkali-catalyzed transesterification of Pongamia pinnata oil for production of biodiesel

Studies were carried out on transesterification of Karanja oil with methanol for the production of biodiesel. The reaction parameters such as catalyst concentration, alcohol/oil molar ratio, temperature, and rate of mixing were optimized for production of Karanja oil methyl ester (KOME). The fatty acid methyl esters content in the reaction mixture were quantified by HPLC and 1H NMR method. The yield of methyl esters from Karanja oil under the optimal condition was 97-98%.     

Effects of Temperature,Time and Composition on Food Oil Surface Tension

Equilibrium and time-dependent surface tension properties at the lipid-vapor interface were investigated, due to their importance in many food applications. Common cooking oils and triglycerides, with or without added oil-soluble amphiphiles, were studied as a function of time and temperature. Surface tension was found to decrease linearly as temperature was increased, and this linear dependence was analyzed to yield thermodynamic information on the surface excess energy and entropy. The different types of cooking oils were nearly indistinguishable with regard to their surface entropy and energy, but an effect of acyl chain length was observed from data for different purified triglyceride oils. These results were consistent with separate results on pure fatty acids of different chain lengths and degree of unsaturation. Lipid amphiphiles, natively present or deliberately added at low concentration to oil, did not cause a change in either dynamic or equilibrium surface tension of corn or olive oil. We conclude that such amphiphilic molecules, despite their presence within the food oil, lack significant surface activity at their native concentration when presented with the surface between oil and air. A decrease in tension in corn oil was seen when mixed in solution with the short-chain caprylic acid (octanoate), but the decrease was notable (>4%) only when this short-chain fatty acid was added at high concentration (≥ 1 M). Added sorbitan monooleate (Span 80) or dioctyl sulfosuccinate sodium salt (AOT) surfactants, on the other hand, decreased equilibrium surface tension by up to 12% and 18%, respectively, at low concentrations (<0.125 M).     

帆布固定化脂肪酶及其性能的研究

研究了用高碘酸钠氧化帆布纤维,使其纤维衍生化成为醛基,与脂肪酶交联进行固定化的过程。通过醛基被交联程度来评价交联过程的优劣。首先对纤维的氧化过程进行了简单优化,进而通过反复交联法与酶蛋白交联。以大豆油和橄榄油水解作为固定化酶的性能评价指标。实验结果表明,通过采用反复交联的方法,可提高载体表面酶蛋白质量分数30％左右。酶活力平均达到4U／cm^2,其对温度、pH的耐受性相比游离酶均有不同程度提高。同时利用油脂在固定化酶过程对酶进行保护,使其对温度、pH等的耐受性进一步增强。在维持较高水解率条件下,可在温和条件下连续反应7批,反应半衰期达140h以上。     

Transesterification of soybean oil using combusted oyster shell waste as a catalyst

Transesterification of soybean oil catalyzed by combusted oyster shell, which is waste material from shellfish farms, was examined. Powdered oyster shell combusted at a temperature above 700 degrees C, at which point the calcium carbonate of oyster shell transformed to calcium oxide, acted as a catalyst in the transesterification of soybean oil. On the basis of factorial design, the reaction conditions of catalyst concentration and reaction time were optimized in terms of the fatty acid methyl ester concentration expressed as biodiesel purity. Under the optimized reaction conditions of a catalyst concentration and reaction time of 25wt.%. and 5h, respectively, the biodiesel yield, expressed relative to the amount of soybean oil poured into the reaction vial, was more than 70% with high biodiesel purity. These results indicate oyster shell waste combusted at high temperature can be reused in biodiesel production as a catalyst.     

Resolution of (R,S)‐ibuprofen catalyzed by immobilized Novozym40086 in organic phase

The enantioselective esterification of ibuprofen catalyzed by Novozym40086 was successfully conducted in organic solvent. Removing‐water reagent was added into the reaction mixture to remove water produced in the esterification. The effects of temperature, n‐hexanol concentration, ibuprofen concentration, and loading of enzymes were investigated. Under the condition of equilibrium, the thermodynamic equilibrium constant (K) of 7.697 and enantioselectivity (E) of 8.512 were obtained. The esterification reaction achieved its equilibrium in approximately 30 hours with conversion of 56% and ee_S of 93.78%. The predicted values of X and ee_S were 67.90% and 95.60%, respectively. The experimental value is approximately equal to the theoretical value, which indicates the feasibility of ideal models.