Optimization and kinetic study of immobilized lipase-catalyzed synthesis of ethyl lactate

Abstract

Enzymatic synthesis of ethyl lactate catalyzed by immobilized lipase has been investigated. The reaction variables (including the molar ratio of ethanol to acid, total substrate amount, temperature, reaction time and rotation speed) were selected in accordance with the Plackett–Burman design and were further optimized via response surface methodology. The molar ratio of ethanol to acid, total substrate amount and reaction time were screened out as significant variables for the optimization study. A 20-run, full-factorial, central composite design was used to construct the statistical model and the optimal conditions obtained were as follows: molar ratio of ethanol to acid of 8.3:1, total substrate amount of 0.4 g, reaction time of 26.87 h with temperature of 55°C and rotation speed of 150 rpm. Under the optimal conditions, the yield of ethyl lactate was up to 24.32%; close to the 25.13% obtained using the commercial lipase, Novozym 435. Due to the low cost and simple immobilization process, the lipase prepared in the present work could have great potential in enzymatic applications. Additionally, a kinetic model with inhibition by both ethanol and lactic acid following a ping-pong bi-bi mechanism was proposed.     

Improvement of the enzymatic synthesis of ethyl valerate by esterification reaction in a solvent system

The present study reports the improved enzymatic synthesis of ethyl valerate (green apple flavor) by esterification reaction of ethanol and valeric acid in heptane medium. Lipase from Thermomyces lanuginosus (TLL) was immobilized by physical adsorption on polyhydroxybutyrate (PHB) particles and used as a potential biocatalyst. The effect of certain parameters that influence the ester synthesis was evaluated by factorial design. The experimental conditions that maximized the synthesis of ethyl valerate were 30.5°C, 18% m/v of biocatalyst (TLL–PHB), absence of molecular sieves, agitation of 234?rpm, and 1,000?mM of each reactant (ethanol and valeric acid). Under these conditions, conversion percentage ≈92% after 105?min of reaction was observed. Soluble TLL was also used as biocatalyst and the highest conversion was of 82% after 120?min of reaction. Esterification reaction performed in a solvent-free system exhibited conversion of 13% after 45?min of reaction catalyzed by immobilized lipase, while the soluble lipase did not exhibit catalytic activity. The synthesis of the ester was confirmed by Fourier transform infrared spectroscopy and gas chromatography–mass spectrometry analyses. After six consecutive cycles of ethyl valerate synthesis, the prepared biocatalyst retained ≈86% of its original activity.     

Comparison of esterification and transesterification of fructose by porcine pancreas lipase immobilized on different supports

The syntheses of fructose butyrate with five different immobilized porcine pancreas lipases were studied in acetonitrile with butyric acid and tributyrin as acyl donors. The hydrolytic activities of the enzymes were measured during the syntheses. The transesterification yield was the highest with the Celite-adsorbed enzyme: 57% (1.42 g fructose butyrate l–1), and this form exhibited the highest degree of hydrolytic activity preservation (57%) after operation for 20 days.     

Exploiting the pressure effect on lipase-catalyzed wax ester synthesis in dense carbon dioxide

The present work focuses on the thermodynamic interpretation of the lauryl oleate biosynthesis in high-pressure carbon dioxide. Lipase-catalyzed lauryl oleate production by oleic acid esterification with 1-dodecanol over immobilized lipase from Rhizomucor miehei (Lipozyme RM IM) was successfully performed in a sapphire window batch stirred tank reactor (BSTR) using dense CO(2) as reaction medium. The experiments were planned to elucidate the pressure effect on the reaction performance. With increasing the pressure up to 10 MPa, the catalytic efficiency of the studied enzyme improved rising up to a maximum and decreased at higher pressure values. Kinetic observations, exhibiting that dense CO(2) expanded reaction mixture in subcritical conditions led to higher performance than when diluted in a single supercritical phase, were elucidated by phase-equilibrium arguments. The experimental results were justified with emphasis on thermodynamic interpretation of the studied system. Particularly, the different reaction performances obtained were related to the position of the operating point with respect to the location of liquid-vapor phase boundaries of the reactant fatty acid/alcohol/CO(2) ternary system. The outlook for exploitation of CO(2) expanded phase at lower pressure compared to supercritical phase, with heterogeneous system in which the solid catalyst particles are exposed to dense CO(2) expanded reaction mixture, in developing new biotransformation schemes is promising.     

Modeling and optimization of lipase-catalyzed esterification of policosanols with conjugated linoleic acid by response surface methodology

Abstract

The aim of this study was to model the lipase-catalyzed esterification of policosanols with conjugated linoleic acid (CLA) in a solvent-free system to produce wax esters which had a lower melting point than that of their corresponding policosanol forms and to optimize the reaction conditions by response surface methodology (RSM). Novozym 435 was selected as a suitable biocatalyst for the reaction. The molar ratio of substrates (policosanols to CLA) was 1:2. A well-fitting quadratic polynomial regression model for the degree of esterification (DE) of policosanols with CLA was established with regard to temperature (35–65°C), enzyme loading (1–5% of weight of total substrates), and reaction time (10–50 min). Optimal reaction conditions were 61.3°C for temperature, 3.7% for enzyme loading, and 34.1 min for reaction time, and the DE was ? 95 mol% under these conditions. The policosanols and wax esters synthesized under optimal conditions had melting points of 79°C and 57°C, respectively.     

有机相中固定化脂肪酶促有机硅烷醇的转酯

探讨了有机相中固定化脂肪酶（Lipozyme）催化非天然的有机硅院醇与脂肪酸酯转酯反应的可能性;系统地研究了有机溶剂特性、水活度、有机硅烷醇结构、脂肪酸酯碳链长等因素对转酯反应的影响。     

Ester synthesis from trimethylammonium alcohols in dry organic media catalyzed by immobilized Candida antarctica lipase B

Twenty-one different organic solvents were assayed as possible reaction media for the synthesis of butyryl esters from trimethylammonium alcohols in dry conditions catalyzed by immobilized Candida antarctica lipase B. The reactions were carried out following a transesterification kinetic approach, using choline and L-carnitine as primary and secondary trimethylammonium alcohols, respectively, and vinyl butyrate as acyl donor. The synthetic activity of the enzyme was strictly dependent on the water content, the position of the hydroxyl group in the trimethylammonium molecule, and the Log P parameter of the assayed solvent. Anhydrous conditions and a high excess of vinyl butyrate over L-carnitine were necessary to synthesize butyryl-L-carnitine. The synthetic reaction rates of butyryl choline were practically 100-fold those of butyryl-L-carnitine with all the assayed solvents. In both cases, the synthetic activity of the enzyme was dependent on the hydrophobicity of the solvent, with the optimal reaction media showing a Log P parameter of between -0.5 and 0.5. In all cases, 2-methyl-2-propanol and 2-methyl-2-butanol were shown to be the best solvents for both their high synthetic activity and negligible loss of enzyme activity after 6 days.     

Sol-gel powders and supported sol-gel polymers for immobilization of lipase in ester synthesis

Candida rugosa lipase was entrapped in hybrid organic–inorganic sol-gel powder prepared by acid-catalyzed polymerization of tetramethoxysilane (TMOS) and alkyltrimethoxysilanes, and used in catalyzing esterification reactions between ethanol and butyric acid in hexane. Optimum preparation conditions were studied, which are gels made from propyltrimethoxysilane (PTMS)/TMOS molar ratio=4:1, hydrolysis time of silane precursor=30 min, water/silane molar ratio=24, enzyme loading=6.25% (w/w) of gel, and 1 mg PVA/mg lipase. The percentage of protein immobilization was 95% and the resulting lipase specific activity was 59 times higher than that of a non-immobilized lyophilized lipase. To prepare magnetic lipase-immobilized sol-gel powder (MLSP) for easier recovery of the biocatalyst, Fe₃O₄ nanoparticles were prepared and co-entrapped with lipase during gel formation. This procedure induced surface morphological change of the sol-gel powder and showed adverse effect on enzyme activity. Hence, although only 9% decrease in protein immobilization efficiency was observed, the corresponding reduction in enzyme activity could be up to 45% when sol-gel powder was doped with 25% (v/v) Fe₃O₄ magnetic nanoparticles solution. Lipase-immobilized sol-gel polymer was also formed within the pores of different porous supports to improve its mechanical stability. Non-woven fabric, with a medium pore size of all the supports tested, was found to be the best support for this purpose. The thermal stability of lipase increased 55-fold upon entrapment in sol-gel materials. The half-lives of all forms of sol-gel-immobilized lipase were 4 months at 40 °C in hexane.     

Wax ester formation catalysed by isoenzymes of lipolytic acyl hydrolase

Wax ester formation by esterification of a long chain fatty acid (palmitic acid) with a long chain fatty alcohol (octadecanol) was enzymically catalysed by acetone dried powder preparations of potato tubers. The enzyme responsible for wax ester formation had multiple isoenzymic forms and was identical with lipolytic acyl hydrolase, a lipid deacylating enzyme. Tubers from different varietiees of potato (Solanum tuberosum) demonstrated markedly different levels of activity and electrophoretic patterns for both wax ester formation and lipid deacylation.     

Short chain fatty acid esters synthesis by commercial lipases in low-water systems and by resting microbial cells in aqueous medium

Thirteen commercial lipases in hexane and seventeen bacterial cell suspensions in aqueous media were screened for the production of ethyl valerate and ethyl butyrate. The highest esterifying activity was obtained with commercial Pancrealipase (Biozymes Inc.) and Candida rugosa lipase (Amano Enzyme Ltd) and with bacterial cell suspension from Pseudomonas fragi CRDA 446. Commercial enzymes gave molar conversion yield of 68% over 24 h as compared to 17% with whole cells in aqueous medium. However, a comparison of both sources of biocatalyst i.e. whole microbial cells and commercial lipases, based on the amount of ester produced per g of protein for a complete reaction, indicated similar activities. © Rapid Science Ltd. 1998     

Optimization of lipase-catalyzed glucose fatty acid ester synthesis in a two-phase system containing ionic liquids and t-BuOH

Selective lipase-catalyzed synthesis of glucose fatty acid esters in two-phase systems consisting of an ionic liquid (1-butyl-3-methyl imidazolium tetrafluoroborate [BMIM][BF₄] or 1-butyl-3-methyl imidazolium hexafluorophosphate [BMIM][PF₆]) and t-butanol as organic solvent was investigated. The best enzyme was commercially available lipase B from Candida antarctica (CAL-B), but also lipase from Thermomyces lanuginosa (TLL) gave good conversion. After thorough optimization of several reaction conditions (chain-length and type of acyl donor, temperature, reaction time, percentage of co-solvent) conversions up to 60% could be achieved using fatty acid vinyl ester as acyl donors in [BMIM][PF₆] in the presence of 40% t-BuOH with CAL-B at 60 °C.     

Scaling-up the synthesis of myristate glucose ester catalyzed by a CALB-displaying Pichia pastoris whole-cell biocatalyst

The novel whole-cell biocatalyst Candida antarctica lipase B displaying-Pichia pastoris (Pp-CALB) is characterized by its low preparation cost and could be an alternative to the commercial immobilized Candida antarctica lipase B (CALB). This study addresses the feasibility of using Pp-CALB in large scale glucose fatty acid esters production. 1,2-O-Isopropylidene-α-d-glucofuranose (IpGlc) was used as the acyl acceptor to overcome the low solubility of glucose in an organic solvent and to avoid the addition of toxic co-solvents. IpGlc significantly improved the Pp-CALB catalyzing esterification efficiency when using long chain fatty acids as the acyl donor. Under the preferred operating conditions (50 °C, 40 g/L molecular sieve dosage and 200 rpm mixing intensity), 60.5% of IpGlc converted to 6-O-myristate-1, 2-O-isopropylidene-α-d-glucofuranose (C14-IpGlc) after a 96-h reaction in a 2-L stirred reactor. In a 5-L pilot scale test, Pp-CALB also showed a similar substrate conversion rate of 55.4% and excellent operational stability. After C14-IpGlc was collected, 70% trifluoroacetic acid was adopted to hydrolyze C14-IpGlc to myristate glucose ester (C14-Glc) with a high yield of 95.3%. In conclusion, Pp-CALB is a powerful biocatalyst available for industrial synthesis, and this study describes an applicable and economical process for the large scale production of myristate glucose ester.     

L-谷氨酸氧化酶与CBD的融合表达及其在微晶纤维素上固定化分析

酶的固定化作为一种重要的技术,已在生物催化领域得到了广泛的应用。现将来源于普拉特链霉菌3304(Streptomyces platensis NTU3304)产生的胞外L-谷氨酸氧化酶(L-glutamate oxidase,Gox)基因gox融合到来源于粪碱纤维单胞菌Cellulomonas fimi的纤维素结合域(CBDcex)的基因上,构建表达载体p ETM10-Gox-CBD,并在大肠杆菌中表达。通过蛋白纯化获得融合蛋白,并命名为Gox-CBD。利用CBD对微晶纤维素特异性吸附的特性将其固定在微晶纤维素上,并对固定化酶的制备条件、结合量、酶学性质及其微晶纤维素结合稳定性等进行了研究。在4℃条件下结合约1 h,融合蛋白Gox-CBD结合在纤维素上的结合量即可达到9.0 mg/g。通过对重组型、融合表达游离的以及固定化在微晶纤维素上的谷氨酸氧化酶的酶学性质进行比较发现,固定化酶的比酶活有所降低;但固定化酶的热稳定性相对于游离酶有了很大的提高,在60℃孵育30 min后还保留有约70%的活性,而游离的重组Gox在相同条件下几乎完全失去活性。当固定化结合蛋白在p H10或者盐浓度5 mmol/L的Na Cl条件下可以牢固结合。并且可以通过一步纯化方法固定化融合蛋白Gox-CBD于微晶纤维素上。因此,L-谷氨酸氧化酶与纤维素结合域融合表达的研究为蛋白的纯化及酶的固定化提供了一种新策略。     

Enzymatic synthesis of isoamyl butyrate using immobilized Rhizomucor miehei lipase in non-aqueous media

Isoamyl butyrate, an important fruity flavor ester, was synthesized using Rhizomucor miehei lipase immobilized on a weak anion exchange resin (Lipozyme IM-20) by the esterification of isoamyl alcohol and butyric acid. The effects of various reaction parameters such as substrate and enzyme concentrations, substrate molar ratio, temperature and incubation time have been investigated. Yields above 90% were obtained with substrate concentrations as high as 2.0 M. No evidence of enzyme inhibition by butyric acid was present up to 1.0 M concentration. Acid inhibition and, to a small extent, alcohol inhibition were evident above 1.0 M substrate concentration. Conversions reached a saturation value by the end of 24–48 h of incubation due to the accumulation of the water of reaction. The equilibrium was successfully pushed forward towards esterification by removing the accumulated water using a molecular sieve.Journal of Industrial Microbiology & Biotechnology (2000) 25, 147–154. Received 09 February 2000/ Accepted in revised form 24 June 2000     

Improving lipase-catalyzed enantioselective ammonolysis of phenylglycine methyl ester in organic solvent by in situ racemization

Lipase-catalyzed enantioselective ammonolysis of phenylglycine methyl ester was processed by in situ racemization with ammonium carbamate as the acyl acceptor. Using 1 mM benzaldehyde or 0.6 mM chloropyridoxal as the racemizing catalyst, 80% substrate conversion with an enantiomeric excess of the product of 95% were achieved at 20 °C after 7 h reaction.     

Kinetics of solvent-free geranyl acetate synthesis by Rhizopus oligosporus NRRL 5905 lipase immobilized on to cross-linked silica

The objective of the present work was to study the kinetics of the solvent-free synthesis of geranyl acetate by a novel lipase (activity 60 U g^?1) made by immobilization of lipase from Rhizopus oligosporous NRRL 5905 on to cross-linked silica gel. Transesterification was performed with vinyl acetate as the acyl donor. Vinyl acetate was used in large excess compared to geraniol, which made the reaction pseudo first order with respect to geraniol and the reaction rate followed Michaelis–Menten kinetics for a single substrate. To obtain the highest yield for geranyl acetate, various relevant physical parameters such as shaking speed, reaction time, enzyme concentration, initial water amount and reaction temperature that influence the activity of lipase were investigated. A maximum molar conversion of 67% was achieved after 48 h of reaction at 30°C, at an enzyme concentration of 25% w/v of reaction mixture. Substrate conversion remained constant for five successive cycles; thereafter the conversion dropped by only 11%. Using a pseudo first-order kinetic model for geranyl acetate synthesis in the absence of organic solvents, apparent K_m and V_max values were evaluated as 60 mM and 141 µmol g^?1 h^?1, respectively.     

Phorbol ester stimulates the synthesis of sphingomyelin in NIH 3T3 cells. A diminished response in cells transformed with human A-raf carrying retrovirus

The tumor promoter 12-O-tetradecanoylphorbol-13-acetate (TPA) stimulated the synthesis of sphingomyelin (CerPCho) from a [¹⁴C]choline-labelled phosphatidylcholine (PtdCho) pool in NIH 3T3 cells. Maximal stimulation (68%) of CerP-Cho synthesis, accompanied by an increase (38%) in its cellular content, required only 2 nM TPA. Higher concentrations of TPA (2–100 nM) had progressively less effect on CerPCho synthesis which correlated with increased hydrolysis of precursor PtdCho. In cells transformed with human or mouse A-raf carrying retroviruses TPA-stimulated PtdCho hydrolysis, but not CerPCho synthesis, suggesting independent regulation of these processes by the TPA-stimulated signal transduction system.     

Enrichment of pinolenic acid from pine nut oil via lipase-catalyzed ethanolysis with an immobilized Candida antarctica lipase

Abstract

Pinolenic acid (PLA) enrichment as an ethyl ester from pine nut oil was successfully accomplished in a batch reactor by lipase-catalyzed ethanolysis using Novozym 435 lipase from Candida antarctica as a biocatalyst. PLA is predominantly an sn-3 substituent of the pine nut oil triacylglycerol (TAG), where it accounts for about 39 mol% of the fatty acids esterified at that position. In the presence of ethanol, Novozym 435 exhibited sn-3 regiospecificity with respect to the TAG of pine nut oil. The effect of the molar ratio of reactants on PLA enrichment by ethanolysis was investigated. The molar ratios of pine nut oil to ethanol were varied from 1:20 to 1:100. A fatty acid ethyl ester (FAEE) fraction with higher PLA content was obtained in the early stage of the reaction, although the yield of PLA was small. However, the PLA content of the FAEEs decreased with increasing reaction time, while the yield of PLA increased. The molar ratio of pine nut oil to ethanol that produced the optimum content and yield of PLA in FAEEs was 1:80.     

Phorbol ester stimulates the synthesis of sphingomyelin in NIH 3T3 cells A diminished response in cells transformed with human A-raf carrying retrovirus

The tumor promoter 12-O-tetradecanoylphorbol-13-acetate (TPA) stimulated the synthesis of sphingomyelin (CerPCho) from a [¹⁴C]choline-labelled phosphatidylcholine (PtdCho) pool in NIH 3T3 cells. Maximal stimulation (68%) of CerP-Cho synthesis, accompanied by an increase (38%) in its cellular content, required only 2 nM TPA. Higher concentrations of TPA (2–100 nM) had progressively less effect on CerPCho synthesis which correlated with increased hydrolysis of precursor PtdCho. In cells transformed with human or mouse A-raf carrying retroviruses TPA-stimulated PtdCho hydrolysis, but not CerPCho synthesis, suggesting independent regulation of these processes by the TPA-stimulated signal transduction system.     

Development of yeast cells displaying <Emphasis Type="Italic">Candida antarctica</Emphasis> lipase B and their application to ester synthesis reaction

We isolated the lipase B from Candida antarctica CBS 6678 (CALB CBS6678) and successfully constructed CALB-displaying yeast whole-cell biocatalysts using the Flo1p short (FS) anchor system. For the display of CALB on a yeast cell surface, the newly isolated CALB CBS6678 exhibited higher hydrolytic and ester synthesis activities than the well-known CALB, which is registered in GenBank (Z30645). A protease accessibility assay using papain as a protease showed that a large part of CALB, approximately 75%, was localized on an easily accessible part of the yeast cell surface. A comparison of the lipase hydrolytic activities of yeast whole cells displaying only mature CALB (CALB) and those displaying mature CALB with a Pro region (ProCALB) revealed that mature CALB is preferable for yeast cell surface display using the Flo1p anchor system. Lyophilized yeast whole cells displaying CALB were applied to an ester synthesis reaction at 60°C using adipic acid and n-butanol as substrates. The amount of dibutyl adipate (DBA) produced increased with the reaction time until 144 h. This indicated that CALB displayed on the yeast cell surface retained activity under the reaction conditions.