Production of flavor esters by immobilized lipase

Summary Candida cylindracea lipase adsorbed to silica gel produced a variety of flavor esters when hydrated and shaken in n-heptane containing substrates. Scale-up production of ethyl butyrate was examined in a packed column with recycling of n-hexane containing substrates. Increased substrate concentrations were stimulatory up to a point after which inhibition and enzyme destabilization in repeated runs occurred.     

Hydrolysis of rapeseed oil by lipase immobilized on inorganic oxide supports

Summary Various inorganic oxide materials coated with 3-aminopropyltriethpxysilane and glutaraldehyde were examined as support materials for lipase catalysing the hydrolysis of rapeseed oil. Nine commercial glass products of different structure and surface area and magnetite were compared. Hydrolytical activity of channel-like carriers was 100× higher than that of controlled pore glass, glass cloth and powders. Lipase on magnetite was tested in hydrolysis of oil in industrial waste having viscosity of 30mPa.s. After 100% conversion of oil the lipase on magnetite was separated in magnetic field and reused 7× without decrease of activity.     

Enrichment of polyunsaturated fatty acids from tuna oil using immobilized Pseudomonas fluorescens lipase

Immobilized Pseudomonas fluorescens lipase enzyme was used to enrich the important polyunsaturated fatty acid (PUFA), docosahexaenoic acid (DHA) and eicosapentaenoic acid (EPA) from tuna oil. Hydrolysis, esterification, and transesterification reactions were studied in detail to find out the fractionation pattern of DHA and EPA during these processes due to preferential selectivity for or against these PUFA. Hydrolysis with P. fluorescens biotype I lipase with stoichiometric amount of water content gave more than 80% of DHA and EPA in the free fatty acid (FFA) form after around 60% of hydrolysis. After some preferential specificity during the early stages of hydrolysis, P. fluorescens lipase exhibits nonselective characteristics on extended hydrolysis. Esterification of FFA extracted from the completely hydrolyzed mixture of tuna oil was found to be better with long chain fatty alcohol like octanol which lead to good enrichment (44.5% for DHA and 11.3% for EPA) and yields of the PUFA in the FFA form. Transesterification (ethanolysis) with immobilized P. fluorescens lipase enzyme resulted in good enrichment and recovery of DHA and EPA in the glyceride mixture. After around 60% of ester synthesis, 74% of (DHA + EPA) enrichment was achieved with yields of more than 90% in the glyceride mixture.     

Production of omega-3 polyunsaturated fatty acids through hydrolysis of fish oil by Candida rugosa lipase immobilized and stabilized on different supports

This paper describes the fish oil hydrolysis performed to obtain Omega-3 fatty acids using Candida rugosa lipase (CRL) immobilized and stabilized on different supports. The enzyme was successfully immobilized, presenting higher thermal stability than the free enzyme. Besides, the cationic derivatives were more stable than the others derivatives and free enzyme in methanol, propanol and cyclohexane. Reactions of fish oil hydrolysis were carried out in organic aqueous medium using 10?U of biocatalyst per gram of oil, at 37?°C. After 96?h, the CRL immobilized on cyanogen bromide agarose rendered the lower fish oil hydrolysis, producing 218?μM of Omega-3, which was 1.1-fold more than the hydrolysis catalyzed by free enzyme, while the ionic derivatives rendered the highest fish oil hydrolysis producing 582 and 577?μM of Omega-3 using the carboxymethyl and sulfopropyl derivatives, respectively. The carboxymethyl and the sulfopropyl derivatives resulted in a 2.9-fold increase in the hydrolysis of fish oil, making these derivatives attractive for industrial applications.     

2-Ethyl-1-hexanol fatty acid esters from rapeseed oil by transesterification

Summary Fatty acid esters of 2-ethyl-1-hexanol were produced in a small pilot scale from rapeseed oil by Candida cylindracea lipase catalyzed transesterification (alcoholysis) without added solvent. Up to 90% conversion of rapeseed oil (97% of theoretical) was obtained in 8 h in 2 kg scale at 37° C with 3.4% (w/w) lipase immobilized on an anion exchange resin Amberlite XAD-7, rapeseed oil:2-ethyl-1-hexanol substrate molar ratio of 2.8, and 3% (w/w) of added water.     

Epoxidation of fatty acids,fatty methyl esters,and alkenes by immobilized oat seed peroxygenase

Fatty epoxides are used as plasticizers and plastic stabilizers and are intermediates for the production of other chemical substances. The currently used industrial procedure for fatty epoxide synthesis requires a strong acid catalyst which can cause oxirane ring opening and side product formation. To find a replacement for the acid catalyst, we have been conducting research on a peroxygenase enzyme from oat (Avena sativa) seeds and have devised a method for immobilization of this enzyme using a hydrophobic membrane support. In this study, fatty acids and fatty methyl esters commonly encountered in commercial vegetable oils were tested as substrates for immobilized peroxygenase, and the epoxide products were characterized. The epoxidation time course of linoleic acid showed two distinct phases with nearly complete conversion to monoepoxide before diepoxide was produced. The diepoxide formed from linolenic acid was found to be 9,10-15,16-diepoxy-12-octadecenoic acid, and only a trace of triepoxide was obtained. Additionally it was discovered that acyclic alkenes with internal double bonds, a cyclic alkene, and an alkene with an aromatic substituent were substrates of peroxygenase. However, alkenes with terminal unsaturation were unreactive. With every substrate examined, oat seed peroxygenase exhibited specificity for epoxidation, producing no other products, and oxirane ring opening did not occur.     

Alcoholysis of olive oil for producing wax esters by intracellular lipase in immobilized fungus cells

Summary Alcoholysis of olive oil was carried out with lauryl and palmityl alcohols for producing wax esters. The reaction can be catalyzed efficiently by cell-bound lipase of Rhizopus niveous fungus cells immobilized within cellulose biomass support particles. Influences of reaction conditions such as water content, temperature, and substrate concentrations on reaction rates and yields were investigated.     

Enzymatic synthesis of 2-ethylhexyl esters of fatty acids by immobilized lipase from Candida sp. 99–125

The 2-ethylhexyl esters of fatty acids were synthesized by immobilized lipase from Candida sp. 99–125. The reuse stability of immobilized lipase was at least four batches. The conditions of enzymatic synthesis of 2-ethylhexyl palmitate were optimized. In the system of petroleum ether, 10% (w/w) immobilized lipase was used in the esterfication of 2-ethyl hexanol (7.8 mmol) and palmitic acid (7.8 mmol) at 40 °C with silica gel as the water absorbent. The esterification degree was 91% under these conditions. The purity of 2-ethylhexyl palmitate was 98% after purification consisting washing by water and evaporation to remove the organic solvent.     

Kinetically controlled synthesis of monoglyceryl esters from chiral and prochiral acids methyl esters catalyzed by immobilized Rhizomucor miehei lipase

Partial acylation of only one primary hydroxyl group of glycerol generates a chiral center at position 2. Rhizomucor miehei lipase (RML) catalyzes the kinetically controlled transesterification of different aromatic carboxylic acids methyl esters with glycerol. High synthetic yields of glyceryl esters (around 70-80%) were obtained even in the presence of significant concentrations of water (from 5% to 20%). After a long incubation of the reaction mixture in the presence of the biocatalyst only pure free acid was obtained. Other lipases (from Geobacillus thermocatenulatus and from Thermomyces lanuginose) also catalyzed similar kinetically controlled transesterifications although less efficiently. RML immobilized on Sepharose-Q showed a high activity and specificity, compared to the immobilization by other techniques, only producing monoglyceryl esters with all substrates. In particular, monoglyceryl-phenylmalonate product was synthesized in 82% overall yield and >99% diastereomeric excess at pH 7.0 and 37 °C and 90% glycerol.     

Reactivity of triglycerides and fatty acids of rapeseed oil in supercritical alcohols

A catalyst-free biodiesel production method with supercritical methanol has been developed that allows a simple process and high yield because of simultaneous transesterification of triglycerides and methyl esterification of fatty acids. From these lines of evidence, we expected that similar results would be attained with the use of various alcohols by the supercritical treatment. However, it still remains unclear which type of reaction, transesterification or alkyl esterification, is faster. This parameter would be important in designing the optimum reaction conditions of the supercritical alcohol method. Therefore, we studied the effect of transesterification of triglycerides and esterification of fatty acids in rapeseed oil. Reaction temperature was set at 300 degrees C, and methanol, ethanol, 1-propanol, 1-butanol or 1-octanol was used as the reactant. The results showed that transesterification of triglycerides (rapeseed oil) was slower in reaction rates than alkyl esterification of fatty acids for any of the alcohols employed. Furthermore, saturated fatty acids such as palmitic and stearic acids had slightly lower reactivity than that of the unsaturated fatty acids; oleic, linoleic and linolenic.     

Enzymatic synthesis of esters using an immobilized lipase

Various esters were synthesized in nearly anhydrous hexane from alcohols and carboxylic acids using a lipase from Candida cylindracea. The enzyme was immobilized on a nylon support and protein loadings as high as 10 mg/g were obtained. The activity of the immobilized enzyme was maximum in a range of temperatures from 25 to 37 degrees C. Ethylpropionate was formed from ethanol and propionic acid at a rate of 0.017 mol/h g immobilized protein. Different esters were formed at comparable rates and equilibrium conversions could generally be approached in less than 10 h in a batch reaction system. The immobilized lipase catalyst was quite stable and retained about one third of the initial activity after repeated experiments during the course of 72 days. A stirred tank continuous flow reactor was used successfully for the continuous production of esters.     

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。     

Synthesis of acetone glycerol acyl esters by immobilized lipase ofMucor miehei

Summary The applications of immobilized lipase ofMucor miehei for the synthesis of acetone glycerol acyl ester from acetone glycerol and fatty acid, which is the first step for monoglyceride production was investigated. With a high oleic acid to acetone glycerol ratio (O/A, mol/mol), a high catalytic activity was observed under low water content in the reaction mixture. By the combination of high O/A ratio (>3) and removal of water which was produced during the reaction, the conversion degree was increased to almost 100%. With the O/A ratio of 3, the approximate half-life of the immobilized lipase and productivity of ester was estimated to be 20 days and 869 g product/g immobilized enzyme per 2 half-lives, respectively.     

Synthesis of sugar fatty acid esters by modified lipase.

A simple synthesis of sugar fatty acid esters was developed in a nonaqueous solution using lipase modified by synthetic detergent. Esterification of sugar was accelerated by continuous removal of water from the reaction mixture with a molecular sieve. When glucose and palmitic acid (1:1 by mole) were used as the starting substrates, more than 90% of glucose was converted to its ester in this system. The resultant product was 6-O-palmitoylglucose. Other mono- or disaccharides were also esterified by the modified lipase with high yield. It was shown that the modified lipase might act as a catalyst for the synthesis of sugar fatty acid esters.     

Synthesis of terpene esters by an immobilized lipase in a solvent-free system

Geraniol and citronellol were esterified with short and medium chain fatty acids using an immobilized lipase of Rhizomucor miehei (Lipozyme IM) in a solvent-free system. The optimum temperature and substrate concentrations for the reactions were 55 to 60 °C and 0.1 M respectively. Yields ranging from 96 to 99% molar conversion were achieved after 6 h. © Rapid Science Ltd. 1998     

Simultaneous conversion of free fatty acids and triglycerides to biodiesel by immobilized Aspergillus oryzae expressing Fusarium heterosporum lipase

The presence of high levels of free fatty acids (FFA) in oil is a barrier to one‐step biodiesel production. Undesirable soaps are formed during conventional chemical methods, and enzyme deactivation occurs when enzymatic methods are used. This work investigates an efficient technique to simultaneously convert a mixture of free fatty acids and triglycerides (TAG). A partial soybean hydrolysate containing 73.04% free fatty acids and 24.81% triglycerides was used as a substrate for the enzymatic production of fatty acid methyl ester (FAME). Whole‐cell Candida antarctica lipase B‐expressing Aspergillus oryzae, and Novozym 435 produced only 75.2 and 73.5% FAME, respectively. Fusarium heterosporum lipase‐expressing A. oryzae produced more than 93% FAME in 72 h using three molar equivalents of methanol. FFA and TAG were converted simultaneously in the presence of increasing water content that resulted from esterification. Therefore, F. heterosporum lipase with a noted high level of tolerance of water could be useful in the industrial production of biodiesel from feedstock that has high proportion of free fatty acids.     

Continuous hydrolysis of oil by immobilized lipase in a countercurrent reactor

Lipase from Pseudomonas fluorescens biotype I was immobilized by adsorption of anion exchange resin using glutaraldehyde to enhance the adsorption. The activity yield of the immobilized lipase was very low (below 1%) when lipase activity was measured using emulsion substrate. The activity yield was 10-70% when lipase activity was measured using non-emulsion substrate. Countercurrent reactors for hydrolysis of oil using non-emulsion substrate were studied. A fluidized bed reactor was found to be superior to a fixed bed one since in a fixed bed reactor the separation rate of the two layers was slow and the flow rate of the reactor had to be slower than the separation rate. A fluidized bed reactor system equipped with settling compartments and stirring compartments was devised. Continuous lipolysis at 60 degrees C and continuous separation of oily product and water soluble product were performed. After continuous operation for more than 3 months, 70% of the initial activity of the immobilized lipase was observed at the end of the reaction.     

Continuous hydrolysis of olive oil by immobilized lipase in organic solvent

Lipase (EC 3.1.1.3) from Candida rugosa was immobilized with DEAE-Sephadex A50, Sephadex G50, Sephadex LH-20, Amberlite IRA94, and Amberlite XAD-7. The enzye immobilized with DEAE-Sephadex A50 was found to be most effective for continuous hydrolysis of olive oil in isooctane. For the continuous reaction, 0.2 g of dry immobilized enzyme was swollen with predetermined amount of water, and packed in a glass column reactor. When the organic solvent (Isooctane) containing olive oil substrate was cocurrently fed with aqueous buffer, the two phases were evenly distributed throughout the packed bed without surfactant supplement or prior mixing of the two phases. A small amount of the surfactant (AOT) was used only in packing procedure, and no additional surfactant was necessary thereafter. Effects of initial water content of the swollen gel, buffer types, and strength were examined in the continuous reaction. Our results suggest that the operational half-life was affected by desorption of the bound enzyme. Under the conditions of 20% olive oil in isooctane and 25 mM triethanolamine buffer (pH 7.0), operational half life was 220 h at 30 degrees C. The reactor was also operable with n-hexane, but the operational stability of the immobilized enzyme in n-hexane was only half of that in isooctane. Our results indicate that various enzyme carrier having hydrophilic or amphiphilic properties could be used for two-phase continuous reaction in packed-bed column, reactor without any surfactant supply or prior dispersion of the two immiscible phases. (c) 1992 John Wiley & Sons, Inc.