复合脂肪酶催化生物柴油的初步研究

初步探讨了复合脂肪酶催化生物柴油的工艺。优化了复合酶配比条件和叔丁醇反应体系。在无溶剂体系中,Novozym435分别与Lipozyme TLIM和Lipozyme RMIM均以70／30质量比混合时,甲酯得率分别达到94．52％和96．25％,比Novozym435单独催化时的甲酯得率分别提高了9．52％和9．99％。在叔丁醇体系中,当Novozym435与Li-pozyme TLIM和Lipozyme RMIM分别以60／40和80／20的质量比混合时,其甲酯得率分别为85．06％和81．5％,比Novozym435单独催化的效率分别提高了9．89％和7．48％。优化叔丁醇体系中复合酶催化条件后,甲酯得率达92％。     

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%。     

固定化脂肪酶催化毛棉籽油制备生物柴油

研究了固定化脂肪酶Lipozyme TL IM和Novozym435催化毛棉籽油和乙酸甲酯制备生物柴油的过程。通过向反应体系中添加甲醇,可减少乙酸的抑制,明显提高生物柴油得率,确定最佳反应条件为:正己烷作溶剂,乙酸甲酯与油摩尔比9:1,添加油重3%的甲醇、油重10%的LipozymeTLIM和5%的Novozym435复合使用,温度55°C,反应8h,生物柴油得率达到91.83%。最后探索了酶催化毛棉籽油合成生物柴油的动力学,得到动力学方程。     

纳米载体固定化脂肪酶及其在生物柴油转化中的应用进展

随着全球能源需求量的不断上升和日益加剧的环境压力,固定化脂肪酶在可持续生物柴油合成中的应用受到广泛关注.纳米材料,包括纳米粒子(磁性和非磁性)、碳纳米管和纳米静电纺丝,具有比表面积大、结构稳定、易于功能化修饰等优势,是固定化脂肪酶领域的重要载体之一.综述了纳米材料作为载体在脂肪酶固定化中的应用,重点介绍这类生物催化剂在...     

固定化脂肪酶催化毛油合成生物柴油

本研究开发了一种用石油醚提取毛油的工艺,研究了以提取的毛油和甲醇为原料,用固定化Candida sp.99-125脂肪酶催化合成脂肪酸甲酯(FAMEs)的可行性。同时考察了磷脂对固定化酶活性、反应起始速率、固定化酶使用批次的影响以及毛油和精炼油对固定化酶使用批次等的影响。研究结果表明,用磷脂质量分数为1%的石油醚悬液浸泡过的脂肪酶比仅用石油醚浸泡过的脂肪酶初始转酯化速率显著下降。当大豆油中无磷脂时,15min时FAMEs的产率为26.2%;磷脂质量分数为5%时,FAMEs降为12.4%。当大豆油中磷脂质量分数小于1%时,固定化酶使用10个批次,FAMEs产率无明显变化。固定化脂肪酶催化石油醚浸提得到的大豆和小桐子毛油,经过10个批次反应FAMEs产率都保持在70%以上,该固定化酶直接催化毛油生产生物柴油具有良好的工业化前景。     

大孔树脂固定化脂肪酶及在微水相中催化合成生物柴油的研究

以不同大孔树脂吸附法固定化假丝酵母99_125脂肪酶,在微水有机相中的应用表明非极性树脂NKA是最佳的固定化载体。分别以正庚烷及磷酸盐缓冲液作为固定化介质,发现在正庚烷介质中树脂NKA的固定化效率能够达到98.98%,与采用磷酸盐缓冲液作为介质相比,固定化酶的水解活力和表观酶活回收率分别提高了4.07和3.43倍。考察了在微水相中固定化酶催化合成生物柴油的催化性能,结果表明,在给酶量为1.92∶1(初始酶粉与树脂的质量比),pH值为7.4,体系水含量为15%(水与油的质量比),反应温度为40℃条件下,固定化酶具有最佳的催化能力;以正庚烷为介质固定化脂肪酶催化合成生物柴油,采用三次流加甲醇的方式,单批转化率最高达到97.3%,连续反应19批以后转化率仍保持为70.2%。     

固定化脂肪酶催化制备L-薄荷醇

用大孔树脂NKA固定高选择性的脂肪酶,催化有机相中转酯化反应,从而拆分八异构体消旋薄荷醇来制备L-薄荷醇。研究pH、载体与酶比例对固定化酶制备的影响及固定化酶的反应稳定性;考察温度、转酯化过程醇酯比例、及底物醇异构组成变化对拆分效果的影响。结果表明:固定化酶的最适pH为8,载体与酶的比例为5∶1时,所得固定化酶的反应稳定性比游离酶的反应稳定性提高了约50%;转酯化反应的最优温度为40℃,醇酯比例为1.5∶1时最佳,改进八异构体消旋薄荷醇组分比例后,非对映体选择率dep达到了95.1%。     

生物酶法生产生物柴油的研究进展

生物柴油是一种对环境友好的绿色可再生能源,是石油燃料的理想替代品。目前用于制造生物柴油的方法主要有化学法、生物酶法、超临界法。将生物酶法与化学法及超临界法进行了比较,指出了生物酶法具有其他两种方法无法比拟的优势,但酶法也存在着反应效率低、生产成本高的缺点;针对如何提高酶法生产效率及降低生产成本的问题进行了综述,并对生物柴油酶法技术的发展提出了建议。     

生物柴油的制造技术与应用

目前,由可再生油脂原料制造绿色燃料生物柴油的技术成为各国的研究热点,本文重点介绍了生物柴油的酯交换法制备技术,并对生物柴油及其副产品甘油等在国内外的开发应用作了介绍。[编者按]     

脂肪酶催化合成生物柴油的研究

生物柴油是用动植物油脂或长链脂肪酸与甲醇等低碳醇合成的脂肪酸甲酯,是一种替代能源。这里探讨了生物法制备生物柴油的过程,采用脂肪酶酯化和酯交换两条工艺路线进行催化合成。深入研究制备过程中,不同脂肪酶、酶的用量和纯度、有机溶剂、低碳醇的抑制作用、吸水剂的作用、反应时间和进程、底物的特异性和底物摩尔比等参数对酯化过程的影响。试验结果表明,采用最佳酯化反应参数和分批加入甲醇并用硅胶作脱水剂的工艺过程,酯化率可以达到92％,经分离纯化后的产品GC分析的纯度可达98％以上,固定化酶的使用半衰期可达到360h。同时对酯交换制备生物柴油过程中,甲醇的用量和甲醇的加入方式对脂肪酶催化过程的影响作了初步研究,优化后的酯交换率可达到83％。     

Immobilized cell reactors in mineralization of dicarboxylic acid solid waste

Dicarboxylic acid solid waste containing phthalic acid, malic acid, quinone, saturated and unsaturated dicarboxylic esters etc., are discharged in huge quantities during the crackdown of benzene over the catalyst vanadium at temperatures greater than 500 °C in a dicarboxylic acid manufacturing industry. Concern over the biological effects of these compounds underlines the necessity to treat this solid waste. The role of yeast Saccharomyces cerevisiae and anaerobic mixed bacterial cultures immobilized in activated carbon, in sequential two stage anoxic reactors, were investigated for the degradation of dicarboxylic acid solid waste (DASW). In the first stage, DASW was dissolved in water to yield a concentration of 0.5% w/v and was treated in yeast Saccharomyces cerevisiae immobilized reactor at an optimum residence time of 24 h. The yeast fermented samples were further treated in an upflow anaerobic reactor containing mixed culture immobilized in activated carbon at an Hydraulic Retention Time (HRT) of 0.2076 days at an hydraulic flow rate of 14.6×10⁻³ m³/day and Chemical Oxygen Demand (COD) loading rate of 4.3 kg/m³/day. The intermediates that were formed during the yeast fermentation and the anaerobic degradation of DASW were characterized by HPLC, proton NMR, C¹³ NMR and mass spectrometry.     

Biodiesel synthesis in a solvent-free system by recombinant Rhizopus oryzae: comparative study between a stirred tank and a packed-bed batch reactor

A simultaneous synthesis of biodiesel, as fatty acid methyl esters, and monoacylglycerols catalysed by the recombinant Rhizopus oryzae lipase immobilized by adsorption on Relizyme OD/403M is presented. The use of this 1(3)-positional specific lipase prevents the formation of glycerol as a by-product, thus avoiding its drawbacks. The synthesis was carried out in a solvent-free system and it has been studied in two different reactor systems: stirred tank and packed-bed reactor. Stirred tank reactor presented a high-initial reaction rate and achieved a 33.6% yield, which corresponds to a value of 50.4% of the maximum yield that can be achieved with a 1(3)-positional specific lipase. In packed-bed reactor there was a smaller initial reaction rate, but it was achieved a 49.1% yield, which corresponds to a 73.6% of the maximum yield. When a second batch is performed, the yield decreased only 4% when packed-bed reactor is employed whereas a drastic decrease is observed in a stirred tank operation. Therefore, packed-bed reactor showed a best performance and minor damage to the biocatalyst.     

Enzymatic synthesis of terpenyl esters by transesterification with fatty acid vinyl esters as acyl donors by Trichosporon fermentans lipase

Enzymatic synthesis of terpenyl esters by esterification or transesterification with fatty acid vinyl esters as acyl donors by celite-adsorbed lipase of Trichosporon fermentans was investigated. In direct esterification of geraniol, the lipase showed high reactivity toward fatty acids with carbon chains longer than C-8, but little reactivity toward fatty acids with shorter chains. With fatty acid vinyl esters as acyl donors, the lipase catalysed the synthesis of geranyl and citronellyl esters with carbon chains shorter than C-6 in with yields of >90% molar conversion. Time course, effects of added water, temperature and substrate concentration were studied for the synthesis of geranyl acetate. Molar conversion yield reached 97.5% after 5 h incubation at 30–40°C with the addition of 3% water. In this reaction, no inhibition by substrates such as geraniol and vinyl acetate was observed.     

微水相超声波协同固定化脂肪酶催化酯交换过程优化

超声波协同固定化脂肪酶催化制备生物柴油的最佳工艺条件为：超声波功率70W、叔丁醇为反应介质、叔丁醇用量3％（v／v）、醇油比3：1且甲醇分三批加入、反应温度40℃、水含量为2％（v／v）。副产物甘油对固定化脂肪酶使用寿命影响最大,使用后的固定化脂肪酶用丙酮洗去表面的甘油,进行酯交换反应,酶的稳定性大为提高,可连续使用16批次。     

Rapid simultaneous lipid extraction and transesterification for fatty acid analyses

An improved adaptation of the direct transesterification method of Lepage and Roy (J. Lipid Res. 25, 1391–96, 1984) for the preparation of fatty acid methyl esters allows notable saving of time and reagents. The material being analysed is heated for 10 minutes with methanol, acetyl chloride and hexane. © Rapid Science Ltd. 1998     

Lipase-catalysed synthesis of glucose fatty acid esters in tert-butanol

Synthesis of 6-O-acylate--d-glycopyranose from underivatised substrates in anhydrous tert-butanol was achieved using immobilised lipases from Candida antarctica and Mucor miehei. Except for acetic acid, the initial reaction rates with the C. antarctica lipase were independent of acyl donor chain lengths and in a range of 3.9±0.4 mol glucose converted min–1 g enzyme preparation. The catalytic activity of the M. miehei lipase increased with increasing acyl donor chain length with a maximum for stearic acid of 0.45 mol min–1 g. Using maltose as substrate, the catalytic activity decreased by a factor of 48 and 20 with the lipase from C. antarctica and M. miehei, respectively, while with maltotriose no reaction was observed.