Enhancement of ethyl propionate synthesis by poly (AAc-co-HPMA-cl-MBAm)-immobilized Pseudomonas aeruginosa MTCC-4713, exposed to Hg2+ and NH4+ ions

A purified alkaline thermo-tolerant bacterial lipase from Pseudomonas aeruginosa MTCC-4713 was immobilized on a poly (AAc-co-HPMA-cl-MBAm) hydrogel. The hydrogel-bound lipase achieved 93.6% esterification of ethanol and propionic acid (300 mM: 100 mM) into ethyl propionate at temperature 65 degrees C in 3 h in the presence of a molecular sieve (3 angstroms). In contrast, hydrogel-immobilized lipase pre-exposed to 5 mM of HgCl2 orNH4Cl resulted in approximately 97% conversion of reactants in 3 h into ethyl propionate under identical conditions. The salt-exposed hydrogel was relatively more efficient in repetitive esterification than the hydrogel-bound lipase not exposed to any of the cations. Moreover, bound lipase exposed Hg2+ or NH4+ ions showed altered specificity towards p-nitrophenyl esters and was more hydrolytic towards higher C-chain p-nitrophenyl esters (p-nitrophenyl laurate and p-nitrophenyl palmitate with C 12 and C 16 chain) than the immobilized lipase not exposed to any of the salts. The later showed greater specificity towards p-nitrophenyl caprylate (C 8).     

Effect of Solvents and Kinetic Parameters on Synthesis of Ethyl Propionate Catalysed by Poly (AAc-co-HPMA-cl-MBAm)-Matrix-Immobilized Lipase of Pseudomonas aeruginosa BTS-2.

Summary A purified alkaline thermo-tolerant bacterial lipase from Pseudomonas aeruginosa BTS-2 was immobilized on a poly (AAc-co-HPMA-cl-MBAm) hydrogel network. The hydrogel showed approximately 95% binding efficiency for lipase (specific activity 1.96 U mg⁻¹). The immobilized enzyme achieved 65.1% conversion of ethanol and propionic acid (100 mM each) into ethyl propionate in n-nonane at 65 °C in 9 h. When alkane of C-chain length lower than n-nonane was used as the organic solvent, the conversion of ethanol and propionic acid into ethyl propionate decreased with a decrease in the log P value of alkanes. The immobilized lipase retained approximately 30% of its original catalytic activity after five cycles of reuse for esterification of ethanol and propionic acid into ethyl propionate at temperature 65 °C in 3 h. Addition of a molecular sieve (3 ?) to the reaction mixture enhanced the formation of ethyl propionate to 89.3%. Moreover, ethanol and propionic acid when taken a molar ratio of 3:1 further promoted the conversion rate to 94%. However, an increase in the molar ratio of propionic acid with respect to ethanol resulted in a decline of ethyl propionate synthesis.     

Triglyceride interesterification by lipases. 3. Alcoholysis of pure triglycerides

Lipase-catalyzed alcoholysis of triolein dissolved in ethanol or isopropanol for the formation of ethyl and isopropyl esters was investigated. Of 16 lipases screened, Amano lipase from P. fluorescens was selected for investigation of the effects of basic reaction conditions on alcoholysis yields. Ethanolysis yields were only slightly affected by water additions to immobilized lipase preparations. Isopropyl ester yields decreased with water addition. Good operational stability was observed over 17 days. Changes in initial triolein concentration in the range 5–50 mM had very little effect on ester yields. The ionic strength of the phosphate buffer used in lipase immobilization affected ethanolysis and isopropanolysis yields in opposite ways. The highest ethanolysis yields were obtained with lipases immobilized from 250 mM buffer, while isopropyl ester yields were highest with lipases immobilized from water. In addition, the quantities and isomers of monoglyceride intermediates in ethanolysis were affected by the immobilization buffer strength. Larger quantities of 2-monoglycerides were formed in ethanolysis reactions with lipase preparations immobilized from water.     

Synthesis of triglycerides of phenylalkanoic acids by lipase-catalyzed esterification in a solvent-free system

Immobilized Candida antarctica lipase B catalyzed the synthesis of triglycerides from glycerol and phenylalkanoic acids in a solvent-free system. 4-Phenylbutyric acid was the best acyl donor and displayed the highest synthetic rate of triphenylbutyrin (glyceryl triphenylbutyrate) at 65 degrees C among various phenylalkanoic acids with straight alkyl chains. The external mass transfer between the immobilized lipase and the bulk reaction mixture was limited. Different methods of removing water during the lipase-catalyzed esterification including spontaneous evaporation, the use of saturated salts solutions, and the use of molecular sieves were studied. The highest yield of triphenylbutyrin at 65 degrees C was 98%, by the elimination of water using molecular sieves in a solvent-free system. The glycerol was almost completely esterified to triphenylbutyrin in excess phenylbutyric acid with various substrate molar ratios.     

Enhanced thermostability of silica-immobilized lipase from Bacillus coagulans BTS-3 and synthesis of ethyl propionate

A lipase from the thermophilic isolate Bacillus coagulans BTS-3 was produced and purified. The enzyme was purified 40-fold to homogeneity by ammonium sulfate precipitation and DEAE-Sepharose column chromatography. Its molecular weight was 31 kDa on SDS-PAGE. The purified lipase was immobilized on silica and its binding efficiency was found to be 60%. The enzyme took 60 min to bind maximally onto the support. The pH and temperature optima of immobilized lipase were same as those of the free enzyme, i.e. 8.5 and 55 degrees C, respectively. The immobilized enzyme had shown marked thermostability on the elevated temperatures of 55, 60, 65 and 70 degrees C. The immobilized enzyme was reused for eigth cycles as it retained almost 80% of its activity. The catalytic activity of immobilized enzyme was enhanced in n-hexane and ethanol. The immobilized enzyme when used for esterification of ethanol and propionic acid showed 96% conversion in n-hexane in 12 h at 55 degrees C.     

Synthesis of 4-nitrophenyl acetate using molecular sieve-immobilized lipase from <Emphasis Type="Italic">Bacillus coagulans</Emphasis>

Extracellular lipase from Bacillus coagulans BTS-3 was immobilized on (3 Å × 1.5 mm) molecular sieve. The molecular sieve showed approximately 68.48% binding efficiency for lipase (specific activity 55 IU mg^?1). The immobilized enzyme achieved approx 90% conversion of acetic acid and 4-nitrophenol (100 mM each) into 4-nitrophenyl acetate in n-heptane at 65°C in 3 h. When alkane of C-chain length other than n-heptane was used as the organic solvent, the conversion of 4-nitrophenol and acetic acid was found to decrease. About 88.6% conversion of the reactants into ester was achieved when reactants were used at molar ratio of 1:1. The immobilized lipase brought about conversion of approximately 58% for esterification of 4-nitrophenol and acetic acid into 4-nitrophenyl acetate at a temperature of 65°C after reuse for 5 cycles.     

Lipase-catalyzed esterification of conjugated linoleic acid with sorbitol: a kinetic study

The kinetics of esterification of conjugated linoleic acid (CLA) with sorbitol in acetone was investigated. An immobilized lipase from Candida antarctica (Chirazyme L-2) was used as the biocatalyst. A 2(2) x 3 factorial design was employed to find an experimental region in which one obtains a high rate of formation of the diester product. Best results were obtained at 10 degrees C using a CLA to sorbitol molar ratio of 5 and a biocatalyst loading of 150 mg/mL of acetone. Under these conditions, in 72 h one obtains a nearly quantitative yield (ca. 98%) of the diester of sorbitol with CLA. To minimize formation of products with degrees of esterification greater than two, the reaction should be carried out at 10 degrees C. A kinetic model developed using the King-Altman method was employed to fit the data. Use of the steady-state approximation for the monoester and an assumption that the concentration of sorbitol was constant and equal to its solubility limit permit one to minimize the number of parameters necessary to model the reaction network. Nonlinear regression analysis based on either two or three parameters provides very good fits of the multiresponse data in the presence or absence of triesters, respectively.     

Lipolytic activity of suspended and membrane immobilized lipase originating from indigenous Burkholderia sp. C20

In this work, a simple, inexpensive, and efficient method of preparing immobilized lipase is presented. The lipase originating from a newly isolated indigenous strain Burkholderia sp. C20 was immobilized onto cellulose nitrate (CN) membrane via filtration. The CN-immobilized lipase was able to retain 60% of its original activity after repeated uses for nine times. The thermal stability of the lipase was also slightly improved after immobilization. The optimal reaction conditions of CN-lipase were pH 9.0 and 55 degrees C, which are similar to those for the suspended lipase. Both suspended and immobilized lipase could hydrolyze the six oil substrates examined, while immobilized lipase displayed less specificity over the oil substrates. Kinetic analysis shows that the dependence of lipolytic activity of both suspended and immobilized lipase on oil substrate concentration can be described by Michaelis-Menten model with good agreement. The estimated kinetic constants for suspended lipase (v(max)=243.9 U/mg, K(m)=0.024 mM) and immobilized lipase (v(max)=32.8 U/mg, K(m)=5.61 mM) were quite different. Employment of immobilization seemed to result in a decrease in v(max) and an increase in K(m), most likely due to the mass transfer resistance arising from formation of micelles during the lipase immobilization process.     

酶法合成糖及糖醇酯

以脂肪酸为酰基供体,糖和糖醇为酰基受体,利用吸附到涤棉布上的假丝酵母脂肪酶作催化剂,在含叔丁醇的系统中,研究了酯化反应条件。酯化最适温度和pH值分别为40℃～45℃和50～75。在酰基供体中,以亚油酸和油酸最好,C8到C22的饱和脂肪酸的酯化程度相仿。在23种糖和糖醇中,果糖、木糖、海藻糖、山梨糖、木糖醇、甘露醇以及异丙基葡萄糖和甲基葡萄糖比其它酰基受体的酯化率高。糖醇的酯化程度明显高于相应的糖。此外,酰基供体与受体的摩尔比大于2∶1时,有利于酯化。在由30mmol(085g)油酸,02mmol山梨醇(0036g),3mL叔丁醇和30mg固定化酯肪酶(600u)组成的反应系统中,40℃震荡反应48h,以等摩尔的底物计算,酯化程度达到90%以上。反应产物经薄层色谱鉴定为单酯和双酯。     

Glutaraldehyde activation of polymer Nylon-6 for lipase immobilization: enzyme characteristics and stability

An extracellular alkaline lipase of a thermo tolerant Bacillus coagulans BTS-3 was immobilized onto glutaraldehyde activated Nylon-6 by covalent binding. Under optimum conditions, the immobilization yielded a protein loading of 228 microg/g of Nylon-6. Immobilized enzyme showed maximum activity at a temperature of 55 degrees C and pH 7.5. The enzyme was stable between pH 7.5-9.5. It retained 88% of its original activity at 55 degrees C for 2h and also retained 85% of its original activity after eight cycles of hydrolysis of p-NPP. Kinetic parameters Km and Vmax were found to be 4mM and 10 micromol/min/ml, respectively. The influence of organic solvents on the catalytic activity of immobilized enzyme was also evaluated. The bound lipase showed enhanced activity when exposed to n-heptane. The substrate specificity of immobilized enzyme revealed more efficient hydrolysis of higher carbon length (C-16) ester than other ones.     

Lipase of <Emphasis Type="Italic">Aspergillus niger</Emphasis> NCIM 1207: A Potential Biocatalyst for Synthesis of Isoamyl Acetate

Commercial lipase preparations and mycelium bound lipase from Aspergillus niger NCIM 1207 were used for esterification of acetic acid with isoamyl alcohol to obtain isoamyl acetate. The esterification reaction was carried out at 30°C in n-hexane with shaking at 120 rpm. Initial reaction rates, conversion efficiency and isoamyl acetate concentration obtained using Novozyme 435 were the highest. Mycelium bound lipase of A. niger NCIM 1207 produced maximal isoamyl acetate formation at an alcohol/acid ratio of 1.6. Acetic acid at higher concentrations than required for the critical alcohol/acid ratio lower than 1.3 and higher than 1.6 resulted in decreased yields of isoamyl acetate probably owing to lowering of micro-aqueous environmental pH around the enzyme leading to inhibition of enzyme activity. Mycelium bound A. niger lipase produced 80 g/l of isoamyl acetate within 96 h even though extremely less amount of enzyme activity was used for esterification. The presence of sodium sulphate during esterification reaction at higher substrate concentration resulted in increased conversion efficiency when we used mycelium bound enzyme preparations of A. niger NCIM 1207. This could be due to removal of excess water released during esterification reaction by sodium sulphate. High ester concentration (286.5 g/l) and conversion (73.5%) were obtained within 24 h using Novozyme 435 under these conditions.     

Synthesis of N-Octyl Oleate with Lipase from Mucor miehei Immobilized onto Polyethylene Based Graft Copolymers

Lpase from Mucor miehei was immobilized onto partially hydrolyzed poly(ethylene)-g.co-hydroxyethyl methacrylate (PE/HEMA) via spacer arms of 1,6-diaminohexane and glutaraldehyde-. The PE/HEMA-lipase system was used for the enzymatic esterification of n-octanol with oleic acid in the absence of organic solvents. The influence of lipase' concentration, in the attachment solution, on the ester production profile and initial reaction rate was studied. It was found that very small amounts of lipase gave preparations which reached good degrees of conversion. The effect of the initial oleic acid concentration on that pseudo-first order reaction, as well as the presence of water in the reactional medium and the influence of temperature were evaluated. It was found that initial oleic acid concentrations lesser than 1.2 M did not inhibit the immobilized lipase activity; the presence of small amount of water (10–30μ) solubilized in the reaction mixture (6.5 cm³) increased the lipase activity and a maximum of activity of the immobilized lipase preparation was found at 55d`C. The operational stability of the preparation was determined at 37d`C in a BSTR type reactor and a half-life time of three days for the immobilized lipase was obtained.     

Preparation of o-palmitoyl alkyl lactates through lipase atalysis

Preparation of o-palmitoyl alkyl lactates with methyl, ethyl, propyl, isopropyl and butyl lactates were attempted in a complex esterification reaction using lipases as catalysts. Compared to lactic acid, alkyl lactates were found to be less inhibitory in nature as they resulted in slightly better yields at shake-flask level. Of the alkyl lactates tested, butyl lactate showed better esterification. Porcine pancreas lipase gave higher yields of esters than Rhizomucor miehei lipase (Lipozyme IM20).     

Enzymatic Preparation of Mono- and Di-Stearin by Glycerolysis of Ethyl Stearate and Direct Esterification of Glycerol in the Presence of a Lipase from Candida Antarctica (Novozym 435)

Mixtures of 1(3)-monostearin and distearin were prepared by direct esterification of glycerol with stearic acid or transesterification using ethyl stearate as acyl donor in the presence of Candida antarctica lipase (Novozym 435) using a variety of solvents of differing polarity. In all cases, the transesterification resulted in higher product yields. In n-heptane as reaction medium the addition of water (3%) was essential for high product yields, with mono- and distearin being produced in almost equal amounts. Using more polar solvents as reaction media, such as acetonitrile or acetone, again the highest yields were obtained in the transesterification mode; employing these solvents the reactions were much more selective towards the formation of monostearin.     

Synthesis of ethyl isovalerate using Rhizomucor miehei lipase: optimization

Immobilized lipase from Rhizomucor miehei (Lipozyme IM-20) was used to catalyze the esterification reaction between isovaleric acid and ethanol to synthesize ethyl isovalerate in n-hexane. Response surface methodology based on five-level four-variable central composite rotatable design was employed to optimize four important reaction variables such as enzyme/substrate E/S ratio, substrate concentration, incubation time, and temperature affecting the synthesis of ethyl isovalerate. The optimum conditions predicted for achieving maximum ester yield (500 mM) are as follows: E/S ratio, 48.41 g/mol; substrate concentration, 1 M; reaction time, 60 h; temperature, 60 degrees C. The predicted value matched well with experimentally obtained value of 487 mM.     

Characteristics of immobilized lipase on hydrophobic superparamagnetic microspheres to catalyze esterification

A novel immobilized lipase (from Candida rugosa) on hydrophobic and superparamagnetic microspheres was prepared and used as a biocatalyst to catalyze esterification reactions in diverse solvents and reaction systems. The results showed that the immobilized lipase had over 2-fold higher activities in higher log P value solvents. An exponential increase of lipase activity against log P of two miscible solvent mixtures was observed for the first time. Both free and immobilized lipase achieved its maximum activity at the range of water activity (a(w)) 0.5-0.8 or higher. At a(w) 0.6, the immobilized lipase exhibited markedly higher activities in heptane and a solvent-free system than did the native lipase. In multicompetitive reactions, the alcohol specificity of the lipase showed a strong chain-length dependency, and the immobilized enzyme exhibited more preference for a longer-chain alcohol, which is different from previous reports. The immobilized lipase showed higher specificities for butyric acid and the medium-chain-length fatty acids (C(8)-C(12)). Then, the immobilized lipase was extended to solvent-free synthesis of glycerides from glycerol and fatty acids. Recovered by magnetic separation, the immobilized lipase exhibited good reusability in repeated batch reaction, indicating its promising feature for biotechnology application.     

Synthesis of ethyl ferulate in organic medium using celite-immobilized lipase

In the present work we have evaluated synthesis of ethyl ferulate by the esterification reaction of ferulic acid and ethanol catalyzed by a commercial lipase (Steapsin) immobilized onto celite-545 in a short period of 6 h in DMSO. The immobilized lipase was treated with cross-linking agent glutaraldehyde (1%; v/v). The optimum synthesis of ethyl ferulate was recorded at 45 °C, pH 8.5 and 1:1 ratio of ethanol and ferulic acid. Co²⁺, Ba²⁺and Pb²⁺ ions enhanced the synthesis of ethyl ferulate Hg²⁺, Cd³⁺and NH⁴⁺ ions had mild inhibitory effect. The celite-bound lipase produced 68 mM of ethyl ferulate under optimized reaction conditions.     

Immobilized Pseudomonas cepacia lipase for biodiesel fuel production from soybean oil

Enzymatic transesterification of soybean oil with methanol and ethanol was studied. Of the nine lipases that were tested in the initial screening, lipase PS from Pseudomonas cepacia resulted in the highest yield of alkyl esters. Lipase from Pseudomonas cepacia was further investigated in immobilized form within a chemically inert, hydrophobic sol-gel support. The gel-entrapped lipase was prepared by polycondensation of hydrolyzed tetramethoxysilane and iso-butyltrimethoxysilane. Using the immobilized lipase PS, the effects of water and alcohol concentration, enzyme loading, enzyme thermal stability, and temperature in the transesterification reaction were investigated. The optimal conditions for processing 10 g of soybean oil were: 35 degrees C, 1:7.5 oil/methanol molar ratio, 0.5 g water and 475 mg lipase for the reactions with methanol, and 35 degrees C, 1:15.2 oil/ethanol molar ratio, 0.3 g water, 475 mg lipase for the reactions with ethanol. Subject to the optimal conditions, methyl and ethyl esters formation of 67 and 65 mol% in 1h of reaction were obtained for the immobilized enzyme reactions. Upon the reaction with the immobilized lipase, the triglycerides reached negligible levels after the first 30 min of the reaction and the immobilized lipase was consistently more active than the free enzyme. The immobilized lipase also proved to be stable and lost little activity when was subjected to repeated uses.     

(Trans)esterification of mannose catalyzed by lipase B from Candida antarctica in an improved reaction medium using co-solvents and molecular sieve

Four co-solvents (dimethylformamide [DMF], formamide, dimethyl sulfoxide [DMSO], and pyridine) were tested with tert-butanol (tBut) to optimize the initial rate (v?) and yield of mannosyl myristate synthesis by esterification catalyzed by immobilized lipase B from Candida antarctica. Ten percent by volume of DMSO resulted in the best improvement of v? and 48-hr yield (respectively 115% and 13% relative gain compared to pure tBut). Use of molecular sieve (5% w/v) enhances the 48-hr yield (55% in tBut/DMSO [9:1, v/v]). Transesterification in tBut/DMSO (9:1, v/v) with vinyl myristate leads to further improvement of v? and 48-hr yield: a relative gain of 85% and 65%, respectively, without sieve and 25% and 10%, respectively, with sieve, compared to esterification. No difference in v? and 48-hr yield is observed when transesterification is carried out with or without sieve.     

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.