Perspectives for biotechnological production of biodiesel and impacts

In recent years, biological ways for biodiesel production have drawn an increasing attention and compared to chemical approaches, lipase-mediated alcoholysis for biodiesel production has many advantages. Currently, there are extensive reports about enzyme-mediated alcoholysis for biodiesel production, and based on the application forms of biocatalyst, the related research can be classified into immobilized lipase, whole cell catalyst, and liquid lipase-mediated alcoholysis for biodiesel production, respectively. This mini-review is focusing on the study of the aforementioned three forms of biocatalyst for biodiesel production, as well as its impacts and prospects.     

豆粕水解液为氮源发酵产脂肪酶的研究

研究了以豆粕水解液作为氮源,假丝酵母Candida sp．99—125发酵生产脂肪酶的过程。分析水解时间对于产酶的影响,对比豆粕水解前后作为氮源发酵时的产酶规律。在30L发酵罐中批次发酵酶活最高可达6000IU／mL,采用豆油反馈流加之后,发酵脂肪酶活力可达8500IU／mL。     

Optimization of extracellular lipase production from the biocontrol fungus Nomuraea rileyi

Lipases are important cuticle-degrading enzymes that hydrolyze the ester bonds of waxes, fats and lipoproteins during the infection of insects by the fungus Nomuraea rileyi. Lipase production by the N. rileyi strain MJ was optimized by varying environmental and nutritional conditions in culture medium containing different vegetable oils at various concentrations with shaking at 150 rpm for 8 days at 25°C. The maximum lipase production was obtained using castor oil (30.5±0.6 U mL^?1), followed in order by coconut oil (20.8±0.4 U mL^?1), olive oil (20.8±0.4 U mL^?1) and cottonseed oil (20.6±0.4 U mL^?1). The highest lipase activity (37.7±0.4 U mL^?1) was obtained when castor oil was used at a concentration of 4% (v/v) of basal medium. When the surfactant Tween 80 was added at the fourth day rather than at the beginning of incubation, a maximum lipase activity of 44.9±3.5 U mL^?1 was obtained. The optimal temperature and pH for lipase production were 25°C and pH 8.0, respectively. This is the first report on lipase production by the biocontrol fungus N. rileyi.     

Biodiesel production with immobilized lipase: A review

Fatty acid alkyl esters, also called biodiesel, are environmentally friendly and show great potential as an alternative liquid fuel. Biodiesel is produced by transesterification of oils or fats with chemical catalysts or lipase. Immobilized lipase as the biocatalyst draws high attention because that process is “greener”. This article reviews the current status of biodiesel production with immobilized lipase, including various lipases, immobilization methods, various feedstocks, lipase inactivation caused by short chain alcohols and large scale industrialization. Adsorption is still the most widely employed method for lipase immobilization. There are two kinds of lipase used most frequently especially for large scale industrialization. One is Candida antartica lipase immobilized on acrylic resin, and the other is Candida sp. 99–125 lipase immobilized on inexpensive textile membranes. However, to further reduce the cost of biodiesel production, new immobilization techniques with higher activity and stability still need to be explored.     

华根霉产脂肪酶发酵培养基的研究

我对摇瓶培养基存在的豆饼粉含量较高,发酵过程中产生大量泡沫,放大困难的问题,在用华根霉发酵生产脂肪酶中,以豆饼粉－蛋白胨培养基为出发培养基,经优化后的培养基组成为：工业蛋白胨６％,豆饼粉２％,卵磷脂１％,葡萄糖１％,磷酸氢二 酸镁０．０５％。与优化前相比,不仅减少了发酵过程中产生的泡沫,有利于大罐发罐,而且减少了豆饼粉残留,酶活提高１０％。     

脂肪酶催化合成生物柴油的瓶颈问题及其对策研究进展

生物柴油,一种新型的清洁能源燃料,具有可再生、可生物降解、环境友好等优良的品性,可部分或全部替代石化柴油。碱催化法、脂肪酶催化法及超临界法是合成生物柴油的主要工艺,其中脂肪酶催化法是一种节能型、环保型工艺,在节能和环保方面,有着碱催化法无可比拟的优越性,具有良好的工业应用前景。但目前在实现产业化的进程中仍存在如酶成本高、稳定性较差、甲醇对酶的失活效应及反应时间长等瓶颈问题。通过固定化技术和全细胞催化剂的采用、甲醇流加方式的改进、溶剂工程的改善及酰基受体和耐醇酶的开发等技术手段,结合固定床生物反应器,较好地解决了这些瓶颈问题,从而推进了酶催化法合成生物柴油的工业化进程。本文主要对酶法合成生物柴油工艺存在的主要问题及相应对策研究进展进行概括介绍,并对其工业化发展前景进行讨论。     

粗壮假丝酵母(Candida valida 20231)产脂肪酶发酵条件的研究

对粗壮假丝酵母(Candida valida 20231)产脂肪酶所需的培养基成分和发酵条件进行了优化。结果表明,粗壮假丝酵母在接种后3 h即进入对数期,18 h后转入稳定期,66 h后进入衰退期;发酵36 h达到最大酶活,至72 h仍然无明显下降趋势。最适合的培养基成分为:4.0%大豆粉,2.0%菜籽油,0.3%葡萄糖,0.3%NH_4NO_3,1.2%K_2HPO_4,0.42%NaH_2PO_4,0.4%MgSO_4·7H_2O。使用优化的培养基,最佳产酶的条件为:装液量80 mL(250 mL摇瓶),初始pH 6,接种量为2.0%,种子菌龄为12 h。在最佳产酶条件下,脂肪酶活力达到32.6 U/mL。     

Optimization of novel halophilic lipase production by Fusarium solani strain NFCCL 4084 using palm oil mill effluent

Among different sources of lipases, fungal lipases have continued to attract a wide range of applications. Further, halophilic lipases are highly desirable for biodiesel production due to the need to mitigate environmental pollution caused as result of extensive use of fossil fuels. However, currently, the high production cost limits the industrial application of lipases. In order to address this issue, we have attempted to optimize lipase production by Fusarium solani NFCCL 4084 and using palm oil mill effluent (POME) based medium. The production was optimized using a combinatory approach of Plackett-Burman (PB) design, one factor at a time (OFAT) design and face centred central composite design (FCCCD). The variables (malt extract, (NH₄)₂SO₄, CaCl₂, MgSO₄, olive oil, peptone, K₂HPO₄, NaNO₃, Tween-80, POME and pH) were analyzed using PB design and the variables with positive contrast coefficient were found to be K₂HPO₄, NaNO₃, Tween-80, POME and pH. The significant variables selected were further analyzed for possible optimum range by using OFAT approach and the findings revealed that K₂HPO₄, NaNO₃, and Tween-80 as the most significant medium components, and thus were further optimized by using FCCCD. The optimum medium yielded a lipase with an activity of 7.8 U/ml, a significant 3.2-fold increase compared to un-optimized medium. The present findings revealed that POME is an alternative and suitable substrate for halophilic lipase production at low cost. Also, it is clearly evident that the combinatory approach employed here proved to be very effective in producing high activity halophilic lipases, in general.     

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.     

提高微生物脂肪酶产量、活性和稳定性的方法研究

微生物脂肪酶是一类广泛应用于诸多工业领域的生物催化剂。提高微生物脂肪酶的产量、活性和稳定性,增强产品的市场竞争力,一直是微生物脂肪酶研究的重点和热点。本文从产脂肪酶菌株的改造、脂肪酶基因的改良、脂肪酶发酵工程和脂肪酶后期处理等四个方面概述了提高微生物脂肪酶产量、活性和稳定性的方法,以期为微生物脂肪酶的规模化工业生产提供方法性指导。     

Yarrowia lipolytica lipase production enhanced by increased air pressure

Aims: To study the cellular growth and morphology of Yarrowia lipolytica W29 and its lipase and protease production under increased air pressures. Methods and Results: Batch cultures of the yeast were conducted in a pressurized bioreactor at 4 and 8 bar of air pressure and the cellular behaviour was compared with cultures at atmospheric pressure. No inhibition of cellular growth was observed by the increase of pressure. Moreover, the improvement of the oxygen transfer rate (OTR) from the gas to the culture medium by pressurization enhanced the extracellular lipase activity from 96·6 U l^?1 at 1 bar to 533·5 U l^?1 at 8 bar. The extracellular protease activity was reduced by the air pressure increase, thereby eliciting further lipase productivity. Cell morphology was slightly affected by pressure, particularly at 8 bar, where cells kept the predominant oval form but decreased in size. Conclusions: OTR improvement by total air pressure rise up to 8 bar in a bioreactor can be applied to the enhancement of lipase production by Y. lipolytica. Significance and Impact of the Study: Hyperbaric bioreactors can be successfully applied for yeast cells cultivation, particularly in high‐density cultures used for enzymes production, preventing oxygen limitation and consequently increasing overall productivity.     

Isolation of a novel lipase producing fungal isolate Aspergillus fumigatus and production optimization of enzyme

Abstract

Fungal lipases occupy a place of prominence among biocatalysts owing to their novel, multifold applications and resistance to high temperature and other operational conditions. In the present study, Aspergillus fumigatus isolated from oil-contaminated soil produced good amount of lipase activity with galactose (1%) as carbon source and peptone (0.1%) as nitrogen source after 72?h of incubation in the production medium at 45?°C and pH 10.0. The isolated enzyme was found to give its optimum reaction temperature at 40?°C and pH 9.0 with the substrate used as p-nitrophenyl benzoate. The activity of lipase was inhibited by the presence of metal ions. A 6.68-fold increase for lipase production was obtained by one variable at a time. Based on the findings of present study, lipase of A. fumigatus is a potential lipase and a candidate for industrial applications such as bioremediation, detergent, leather and pharmaceutical industries.     

脂肪酶发酵过程中的油脂利用

对假丝酵母Candidasp．99—125发酵生产脂肪酶的过程中油脂代谢情况进行了研究。分析了发酵过程中甘油酯、油酸、棕榈酸等物质浓度随发酵时间的变化趋势,以及它们与菌体生长和产酶之间相互影响关系,结果发现油酸的消耗能够显著地促进脂肪酶的合成（油酸质量浓度从30g／L降低到10g／L）,并且细胞对油酸和棕榈酸的利用没有选择性,最终发酵脂肪酶活力可达8000U／mL。     

Green enzymatic production of glyceryl monoundecylenate using immobilized Candida antarctica lipase B

Enzymatic synthesis of glyceryl monoundecylenate (GMU) was performed using indigenously immobilized Candida anatarctica lipase B preparation (named as PyCal) using glycerol and undecylenic acid as substrates. The effect of molar ratio, enzyme load, reaction time, and organic solvent on the reaction conversion was determined. Both batch and continuous processes for GMU synthesis with shortened reaction time were developed. Under optimized batch reaction conditions such as 1:5 molar ratio of undecylenic acid and glycerol, 2?h of reaction time at 30% substrate concentration in tert-butyl alcohol, conversion of 82% in the absence of molecular sieve, and conversion of 93% in the presence of molecular sieve were achieved. Packed bed reactor studies resulted in high conversion of 86% in 10-min residence time. Characterization of formed GMU was performed by FTIR, MS/MS. Enzymatic process resulted in GMU as a predominant product in high yield and shorter reaction time periods with GMU content of 92% and DAG content of 8%. Optimized GMU synthesis in the present study can be used as a useful reference for industrial synthesis of fatty acid esters of glycerol by the enzymatic route.     

Lipase-catalyzed transesterification of rapeseed oils for biodiesel production with a novel organic solvent as the reaction medium

tert-Butanol, as a novel reaction medium, has been adopted for lipase-catalyzed transesterification of rapeseed oil for biodiesel production, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. Combined use of Lipozyme TL IM and Novozym 435 was proposed further to catalyze the methanolysis and the highest biodiesel yield of 95% could be achieved under the optimum conditions (tert-butanol/oil volume ratio 1:1; methanol/oil molar ratio 4:1; 3% Lipozyme TL IM and 1% Novozym 435 based on the oil weight; temperature 35 °C; 130 rpm, 12 h). There was no obvious loss in lipase activity even after being repeatedly used for 200 cycles with tert-butanol as the reaction medium. Furthermore, waste oil was also explored for biodiesel production and it has been found that lipase also showed good stability in this novel system.     

复合脂肪酶协同催化制备生物柴油的研究

【目的】探讨复合酶协同催化体系在含水量较高的体系中催化油脂制备生物柴油的工艺条件。【方法】通过基因工程手段在毕赤酵母中分别高效分泌表达南极假丝酵母脂肪酶(CALB)和米根霉脂肪酶(ROL),构建CALB和ROL复合酶协同催化体系制备生物柴油,利用单因素实验优化工艺条件,以甲酯化得率作为复合酶协同催化体系效能的评价标准。【结果】优化工艺条件为:CALB?ROL最佳复合酶配比为7?3,每克大豆油中加入16 U的复合脂肪酶,甲醇与大豆油摩尔比为4?1,并按0 h时2?1醇油摩尔比,12 h和24 h时以1?1醇油摩尔比分批加入甲醇,含水量为30%-60%之间,40°C反应29-34 h,甲酯得率达到93%。【结论】该复合酶协同催化体系对环境友好,与常规酶法制备生物柴油工艺相比对酶的使用量和催化时间减少幅度都在50%以上,本复合酶协同催化体系能有效降低生物柴油制备成本,具有较好的工业化应用前景。     

酶法合成生物柴油工业化研究进展

介绍了北京化工大学近年来酶法合成生物柴油工业化研究的结果。主要内容包括以下几个方面:高产脂肪酶菌株的选育、脂肪酶发酵工艺优化及放大、脂肪酶固定化方法、酶反应器放大、生物柴油分离精制及副产物甘油综合利用。该脂肪酶假丝酵母Candida sp.99-125在5 m3罐发酵活力不低于8 000 IU/mL,然后将该脂肪酶吸附固定在织物膜上并进行表面改性,用于搅拌罐式反应器生产每吨甲酯的需酶量仅为4.2 kg,产品经分离精制调质后,其各项指标完全符合德国生物柴油生产标准。副产物甘油可用于1,3-丙二醇发酵,30 L发酵罐中1,3-丙二醇的产量可达到76.1 g/L。     

Options for biochemical production of 4-hydroxybutyrate and its lactone as a substitute for petrochemical production

Options are discussed for biochemical production of 4-hydroxybutyrate (4-HB) and its lactone, gamma-butyrolactone (GBL), from renewable sources. In the first part of the study, the thermodynamic feasibility of four potential metabolic pathways from glucose to 4-HB are analyzed. The calculations reveal that when the pathways are NAD(+) dependent the intermediate succinate semialdehyde (SSA) accumulates leading to low 4-HB yields at equilibrium. For NADP(+) dependent pathways the calculated yield of 4-HB improves, up to almost 100%. In the second part of this study, continuous removal of 4-HB from the solution is considered to shift SSA conversion into 4-HB so that SSA accumulation is minimized. One option is the enzymatic production of GBL from 4-HB. Candida antarctica Lipase B shows good lactonization rates at pH 4, but unfortunately this conversion cannot be performed in-vivo during 4-HB production because of the neutral intracellular pH.