Study on the effect of cultivation parameters and pretreatment on Rhizopus oryzae cell-catalyzed transesterification of vegetable oils for biodiesel production

Enzymatic methanolysis of vegetable oils for biodiesel production has become a hot point recently, in which study on whole cell as catalyst is an important field. In this paper, whole cell (Rhizopus oryzae IFO 4697) was adopted directly as biocatalyst for biodiesel production. Effects of carbon source on cell growth and whole cell-catalyzed methanolysis of vegetable oils for biodiesel production were studied. The results showed that different oils contained in the cultivation medium had varied effects on the whole cell-catalyzed methanolysis of oils; with some specified oil as the carbon source for cell cultivation, those cells expressed higher catalytic activity in catalyzing the transesterification of the same oil for biodiesel production. The initial reaction rate was increased notably (204%) with oil pretreatment on the cells before catalyzing the reaction, which was possibly due to the improved mass transferring of substrates. Under the optimized conditions, the maximum methyl ester yield could reach 86%.     

Study on the effect of cultivation parameters and pretreatment on Rhizopus oryzae cell-catalyzed transesterification of vegetable oils for biodiesel production

Enzymatic methanolysis of vegetable oils for biodiesel production has become a hot point recently, in which study on whole cell as catalyst is an important field. In this paper, whole cell (Rhizopus oryzae IFO 4697) was adopted directly as biocatalyst for biodiesel production. Effects of carbon source on cell growth and whole cell-catalyzed methanolysis of vegetable oils for biodiesel production were studied. The results showed that different oils contained in the cultivation medium had varied effects on the whole cell-catalyzed methanolysis of oils; with some specified oil as the carbon source for cell cultivation, those cells expressed higher catalytic activity in catalyzing the transesterification of the same oil for biodiesel production. The initial reaction rate was increased notably (204%) with oil pretreatment on the cells before catalyzing the reaction, which was possibly due to the improved mass transferring of substrates. Under the optimized conditions, the maximum methyl ester yield could reach 86%.     

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.     

Improved catalytic performance of GA cross-linking treated Rhizopus oryzae IFO 4697 whole cell for biodiesel production

Whole cell-mediated methanolysis of renewable oils for biodiesel production has drawn much attention in recent years since it can avoid the complex procedures of isolation, purification and immobilization required for the preparation of immobilized lipase. It has been demonstrated that Rhizopus oryzae IFO 4697 whole cell could catalyze the methanolysis of renewable oils for biodiesel production effectively and glutaraldehyde (GA) cross-linking treatment on whole cell catalyst could improve its stability in the repeated uses. The catalytic performance of cells with GA cross-linking treatment was studied systematically in this paper. The results showed that the treated cells expressed higher methanol tolerance, and high catalytic activity could be maintained with higher ratio of methanol to oil; the operational stability of whole cell catalyst and methanol utilization rate were also considered in optimization of methanol addition strategy. A novel methanol addition strategy was proposed, with which the reaction time could be shortened significantly and a biodiesel yield of 94.1% could be obtained within 24 h reaction; it was also found that with this methanol addition strategy, GA cross-linked whole cell expressed rather good operational stability; the reason for stability improvement was also investigated and should be attributed to less lipase leakage.     

Immobilization of steapsin lipase on macroporous immobead-350 for biodiesel production in solvent free system

Commercially available steapsin lipase was immobilized on macroporous polymer beads (IB-350) and further investigated for biodiesel production under solvent free conditions. The fatty acid methyl ester (biodiesel) synthesis was carried out by the methanolysis of fresh and used cooking sunflower oil. The enzymatic reaction for biodiesel synthesis was optimized with various reaction parameters and the obtained reaction conditions were 1: 6 molar ratio (oil: methanol), 50 mg biocatalyst and 20% water content at 45°C for 48 h under solvent free conditions. It was observed that 94% of biodiesel was produced under the optimized reaction conditions. The four step addition of methanol at the interval of 12 h was found to be more effective. Moreover the biocatalyst was effectively reused for four consecutive recycles and was appreciably stable for 90 days. The results obtained highlight potential of immobilized steapsin lipase for biodiesel production.     

Mechanism study on NS81006-mediated methanolysis of triglyceride in oil/water biphasic system for biodiesel production

Compared to immobilized lipase, soluble lipase has the merits of lower cost and faster reaction rate, thus much attention has been paid to soluble lipase-mediated methanolysis for biodiesel (fatty acid methyl ester, FAME) production in recent years. Our previous study showed that soluble lipase NS81006 could effectively catalyze the methanolysis of soybean oil (triglyceride, TG) for FAME preparation in oil/water biphasic system. Study on the related mechanism of soluble lipase NS81006-mediated methanolysis of TG was carried out in this paper. Based on the analysis of substances change in the reaction process, mechanism model was hypothesized and the model parameters were simulated by Matlab. The simulated model was validated further. The results showed that in the reaction process of soluble lipase NS81006-mediated methanolysis of TG in oil/water biphasic system, TG proceeded three-step hydrolysis to generate FFA (free fatty acid), and then FFA transformed into FAME by esterification with methanol. During the whole process, FFA is mainly generated through the hydrolysis of TG and intermediate DG (diglyceride), while the hydrolysis of FAME could be ignored.     

Process engineering and optimization of glycerol separation in a packed-bed reactor for enzymatic biodiesel production

A process model for efficient glycerol separation during methanolysis in an enzymatic packed-bed reactor (PBR) was developed. A theoretical glycerol removal efficiency from the reaction mixture containing over 30% methyl esters was achieved at a high flow rate of 540 ml/h. To facilitate a stable operation of the PBR system, a batch reaction prior to continuous methanolysis was conducted using oils with different acid values and immobilized lipases pretreated with methyl esters. The reaction system successfully attained the methyl ester content of over 30% along with reduced viscosity and water content. Furthermore, to obtain a high methyl ester content above 96% continuously, long-term lipase stability was confirmed by operating a bench-scale PBR system for 550 h, in which the intermediates containing methyl esters and residual glycerides were fed into the enzyme-packed columns connected in series. Therefore, the developed process model is considered useful for industrial biodiesel production.     

Dynamic modeling of biodiesel production from simulated waste cooking oil using immobilized lipase

The effectiveness of lipase immobilized on ceramic beads, in the production of biodiesel from simulated waste cooking oil in organic solvent system, was compared to that of free lipase. Experimental determination of the effect of concentrations of methanol on the rate of the enzymatic transesterification was experimentally determined. In addition, the effectiveness of lipases from bacterial and yeast sources for biodiesel production from simulated waste cooking oil was compared. A kinetic model was developed to describe the system, taking into consideration the mass transfer resistances of the reactants. Inhibition effects by both substrates on the interfacial reaction were also considered. The experimental results were used to determine the kinetic parameters of the proposed model and to determine the effect of mass transfer. On the other hand, it was shown that biodieasel can be produced in considerable amounts, with yield reaching 40%, in absence of organic solvent using immobilized lipase from P. cepacia on ceramic beads.     

Effect of water on lipase NS81006-catalyzed alcoholysis for biodiesel production

Biodiesel production catalyzed by free lipase has been drawing attention for its lower cost and faster reaction rate compared to immobilized lipase. It has been found that free lipase NS81006 could efficiently catalyze alkyl esters production and a certain amount of water is demonstrated to be necessary for the catalytic process. The effect of water content on liquid lipase NS81006-mediated methanolysis and ethanolysis for biodiesel production was first explored respectively in this paper. It was found that with water content ranging from 3% to 10% (based on oil weight), there was no significant difference in the final alkyl ester yield either in NS81006-mediated methanolysis or ethanolysis process, while the quality of biodiesel varied obviously. The acid value as well as the contents of monoglyceride and diglyceride were much lower in the lower water-containing system. With the water content decreasing from 10% to 3%, the acid value reduced from 8.24 to 4.89 mg KOH/g oil, and the content of MAG and DAG dropped to 0.31 and 0.22, from 0.62 and 0.74, respectively. Lipase could maintain rather good stability with proper alcohol adding strategy and the gradual reduction in biodiesel yield in the repeated uses resulted from the accumulation of by-product glycerol. The continuous running of lipase-mediated methanolysis of waste cooking oil was successfully realized at 30L reactor and a final methyl ester yield of over 90% could be obtained.     

Lipase catalyzed transesterification of soybean oil using ethyl acetate,an alternative acyl acceptor

Methanol, the acyl acceptor usually used in the commercial process of biodiesel production, is associated with some problems such as immiscibility with oils and lipase deactivation. To overcome these barriers, ethyl acetate was proposed as an alternative acyl acceptor for the production of biodiesel from soybean oil using an immobilized lipase, Novozym 435, Ethyl acetate mixed well with soybean oil, and only slightly inhibited the lipase activity by 5%. The effects of various environmental parameters, such as the composition of soybean oil and ethyl acetate, lipase content, and reaction temperature, were investigated to determine the optimal conditions for biodiesel production. As a result, the highest biodiesel production yield, 63.3 (±0.6)%, was obtained by using an ethyl acetate and soybean oil mixture with a 6∶1 molar ratio, with 8% of the immobilized lipase based on the weight of oil added at 70°C and 600 rpm.     

Enzymatic production of biodiesel from cotton seed oil using t-butanol as a solvent

The enzymatic production of biodiesel by methanolysis of cottonseed oil was studied using immobilized Candida antarctica lipase as catalyst in t-butanol solvent. Methyl ester production and triacylglycerol disappearance were followed by HPLC chromatography. It was found, using a batch system, that enzyme inhibition caused by undissolved methanol was eliminated by adding t-butanol to the reaction medium, which also gave a noticeable increase of reaction rate and ester yield. The effect of t-butanol, methanol concentration and temperature on this system was determined. A methanolysis yield of 97% was observed after 24h at 50 degrees C with a reaction mixture containing 32.5% t-butanol, 13.5% methanol, 54% oil and 0.017 g enzyme (g oil)(-1). With the same mixture, a 95% ester yield was obtained using a one step fixed bed continuous reactor with a flow rate of 9.6 mlh(-1) (g enzyme)(-1). Experiments with the continuous reactor over 500 h did not show any appreciable decrease in ester yields.     

Whole cell biocatalyst for biodiesel fuel production utilizing Rhizopus oryzae cells immobilized within biomass support particles

As part of a research program aimed at producing biodiesel fuel from plant oils enzymatically cells of Rhizopus oryzae (R. oryzae) IFO4697 (with a 1,3-positional specificity lipase) immobilized within biomass support particles (BSPs) were investigated for the methanolysis of soybean oil. The R. oryzae cells easily became immobilized within the BSPs during batch operation. To enhance the methanolysis activity of the immobilized cells under the culture conditions used, various substrate-related compounds were added to the culture medium. Among the compounds tested, olive oil or oleic acid was significantly effective. In contrast, no glucose was necessary. Immobilized cells were treated with several organic solvents, but none gave higher activity than untreated cells. When methanolysis was carried out with stepwise additions of methanol using BSP-immobilized cells, in the presence of 15% water the methyl esters (MEs) content in the reaction mixture reached 90% - the same level as that using the extracellular lipase. The process presented here, using a whole cell biocatalyst, is considered to be promising for biodiesel fuel production in industrial applications.     

Lipase-catalyzed methanolysis of palm oil in presence and absence of organic solvent for production of biodiesel

Enzymatic production of methyl esters (biodiesel) by methanolysis of palm oil in presence and absence of organic solvent was investigated using Candida antarctica lipase immobilized on acrylic resin as a biocatalyst. Although, at least molar equivalent of methanol (methanol-palm oil ratio 3:1) is required for the complete conversion of palm oil to methyl esters, lipase catalyzed methanolysis of palm oil in absence of organic solvent was poisoned by adding more than 1/3 molar equivalent of methanol. The use of polar organic solvents prevented the lipase to be poisoned in methanolysis with a molar equivalent of methanol, and tetrahydrofuran (THF) was found to be the most effective. The presence of water in methanolysis of palm oil both in presence and absence of THF inhibited the reaction rate but this inhibition was considerably low in THF containing system. The palm oil-lipase (w/w) ratio significantly influenced the activity of lipase and the optimal ratio in presence and absence of THF was 100 and 50, respectively.     

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％。     

Study on acyl migration in immobilized lipozyme TL-catalyzed transesterification of soybean oil for biodiesel production

During enzymatic transesterification of soybean oils with methanol for biodiesel production, it was supposed that the maximum biodiesel yield was only 66% since lipozyme TL was a typical lipase with a strict 1,3-positional specificity. However, it has been observed that over 90% biodiesel yield could be obtained. It was therefore assumed, and subsequently demonstrated, that acyl migration occurred during the reaction process. Different factors which may influence the acyl migration were explored further and it has been found that the silica gel acting as the immobilized material contributes significantly to the promotion of acyl migration in the transesterification process. The final biodiesel yield was only 66% when 4% lipozyme TL used, while about 90% biodiesel yield could be achieved when combining 6% silica gel with 4% lipozyme TL, almost as high as that of 10% immobilized lipase used for the reaction.     

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.     

Rhizopus oryzae IFO 4697 whole cell catalyzed methanolysis of crude and acidified rapeseed oils for biodiesel production in tert-butanol system

Whole cell Rhizopus oryzae (R. oryzae) IFO4697 immobilized within biomass support particles (BSPs) was used as catalyst for biodiesel production in tert-butanol, in which the stability of the catalyst could be enhanced significantly. Different feedstocks (refined, crude and acidified rapeseed oils) were adopted further for biodiesel production in tert-butanol system and it was found that when acidified rapeseed oil was used as feedstocks, the reaction rate and final methyl ester (ME) yield were significantly higher than that of refined and crude rapeseed oil. Major differences among the aforementioned oils were found to be the contents of free fatty acid (FFA), water and phospholipids, which showed varied influences on whole cell mediated methanolysis for biodiesel production. The reaction rate increased with the increase of free fatty acid content in oils; water content had varied influence on reaction rate and biodiesel yield; using adsorbent to remove excessive water could increase biodiesel yield significantly (from 73 to 84%); it was also found interestingly that phospholipids contained in oils could increase the reaction rate to a certain extent.     

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.     

Biodiesel-fuel production in a packed-bed reactor using lipase-producing Rhizopus oryzae cells immobilized within biomass support particles

A packed-bed reactor (PBR) system using fungus whole-cell biocatalyst was developed for biodiesel fuel production by plant oil methanolysis. Lipase-producing Rhizopus oryzae cells were immobilized within 6 mm × 6 mm × 3 mm cuboidal polyurethane foam biomass support particles (BSPs) during batch cultivation in a 20-l air-lift bioreactor. Emulsification of the reaction mixture containing soybean oils and water improved the methanolysis reaction rate. Using a high flow rate for the reaction mixture in the PBR caused exfoliation of the immobilized cells from the BSPs, while the inefficient mixing of the reaction mixture at low flow rates allowed the BSPs to be covered with a hydrophilic layer of high methanol concentration, leading to a significant decrease in lipase activity. A high methyl ester content of over 90% was achieved at a flow rate of 25 l/h in the first cycle of repeated batch methanolysis and a high value of around 80% was maintained even after the tenth cycle. Comparison with methanolysis reaction in a shaken bottle suggested that the PBR enhances repeated batch methanolysis by protecting immobilized cells from physical damage and excess amounts of methanol. The process presented here is therefore considered to be promising for industrial biodiesel-fuel production.     

Transesterification using the cross-linked enzyme aggregate of Photobacterium lipolyticum lipase M37

Biodiesel is methyl and ethyl esters of long-chain fatty acids produced from vegetable oils or animal fats. Lipase enzymes have occasionally been used for the production of this biofuel. Recently, biodiesel production using immobilized lipase has received increased attention. Through enhanced stability and reusability, immobilized lipase can contribute to the reduction of the costs inherent to biodiesel production. In this study, methanol-tolerant lipase M37 from Photobacterium lipolyticum was immobilized using the cross-linked enzyme aggregate (CLEA) method. Lipase M37 has a high lysine content (9.7%) in its protein sequence. Most lysine residues are located evenly over the surface of the protein, except for the lid structure region, which makes the CLEA preparation yield quite high (~93%). CLEA M37 evidences an optimal temperature of 30oC, and an optimal pH of 9-10. It was stable up to 50°C and in a pH range of 4.0-11.0. Both soluble M37 and CLEA M37 were stable in the presence of high concentrations of methanol, ethanol, 1-propanol, and nbutanol. That is, their activities were maintained at solvent concentrations above 10% (v/v). CLEA M37 could produce biodiesel from olive oil and alcohols such as methanol and ethanol. Additionally, CLEA M37 generated biodiesel via both 2-step methanol feeding procedures. Considering its physical stability and reusability, CLEA M37 may potentially be used as a catalyst in organic synthesis, including the biodiesel production reaction.