Refolding,purification and characterization of an organic solvent-tolerant lipase from Serratia marcescens ECU1010

Expression of recombinant proteins as inclusion bodies in bacteria is one of the most efficient ways to produce cloned proteins, as long as the inclusion bodies can be successfully refolded. In this study, the different parameters were investigated and optimized on the refolding of denatured lipase. The maximum lipase activity of 5000 U/L was obtained after incubation of denatured enzyme in a refolding buffer containing 20 mM Tris–HCl (pH 7.0), 1 mM Ca²⁺ at 20 °C. Then, the refolded lipase was purified to homogeneity by anion exchange chromatography. The purified refolded lipase was stable in broad ranges of temperatures and pH values, as well as in a series of water-miscible organic solvents. In addition, some water-immiscible organic solvents, such as petroleum ether and isopropyl ether, could reduce the polarity and increase the nonpolarity of the refolding system. The results of Fourier transform infrared (FT-IR) microspectroscopy were the first to confirm that lipase refolding could be further improved in the presence of organic solvents. The purified refolded lipase could enantioselectively hydrolyze trans-3-(4-methoxyphenyl) glycidic acid methyl ester [(±)-MPGM]. These features render the lipase attraction for biotechnological applications in the field of organic synthesis and pharmaceutical industry.     

Synthesized tyrosyl hydroxyphenylacetate,a novel antioxidant,anti-stress and antibacterial compound

New tyrosyl ester derivative, a naturally occurring phenol with interesting biological properties, has been synthesized in good yield by a direct esterification of tyrosol (Ty) with p-hydroxyphenylacetic acid (p-HPA) using Candida antarctica lipase as a catalyst. The response surface methodology was used to modulate the effects of the enzyme amount (10–50 mg), the tert-butanol/hexane (v/v) ratio (0.16–0.84), the temperature (35–55 °C) and the reaction time (15–45 h) on the tyrosyl hydroxyphenylacetate (Ty-HPA) conversion yield. Under the optimal predicted conditions (enzyme amount: 10 mg, solvents volume ratio 0.16, reaction temperature; 45 °C and 34 h of incubation), a high conversion yield of 79.33 ± 4% was reached. The obtained ester was purified and characterized by NMR, LC/MS and FT-IR methods. ABTS free radical quenching potency demonstrated that the esterified tyrosol (Ty-HPA) was more effective than the natural separated antioxidants: Ty and p-HPA. Furthermore, when used at a non-cytotoxic concentration (100 μM), tyrosyl ester showed significant effectiveness in preventing iron-induced oxidative stress in blood cells compared to the two separated compounds. The antibacterial activity of Ty, p-HPA, mixed solution of Ty + p-HPA and Ty-HPA was performed by determining the minimum inhibitory concentration (MIC) and minimum bactericidal concentration (MBC) using a micro-well dilution method. Compared to the separated substrates, synthesized ester exhibits the most antibacterial effect mainly against Gram+ bacteria.     

An extracellular solvent stable alkaline lipase from Pseudomonas sp. DMVR46: Partial purification,characterization and application in non-aqueous environment

The biosynthesis of esters is currently of much commercial interest because of the increasing popularity and demand for natural products among consumers. Biotransformation and enzymatic methods of ester synthesis are more effective when performed in non-aqueous media. In present study, an organic solvent stable Pseudomonas sp. DMVR46 lipase was partially purified by acetone precipitation and ion exchange chromatography with 28.95-fold purification. The molecular mass of the lipase was found to be ∼32 kDa. The partially purified lipase was optimally active at 37 °C and pH 8.5. The enzyme showed greater stability toward organic solvents such as isooctane, cyclohexane and n-hexane retaining more than 70% of its initial activity. The metal ions such as Ca²⁺, Ba²⁺ and Mg²⁺ had stimulatory effects on lipase activity, whereas Co²⁺ and Zn²⁺ strongly inhibited the activity. Also lipase exhibited variable specificity/hydrolytic activity toward different 4-nitrophenyl esters. DMVR46 lipase was further immobilized into AOT-based organogels used for the synthesis of flavor ester pentyl valerate in presence of organic solvents. The organogels showed repeated use of enzyme with meager loss of activity even upto 10 cycles. The solvent-stable lipase DMVR46 thus proved to be an efficient catalyst showing an attractive potency for application in biocatalysis under non-aqueous environment.     

Biocatalytic acylation of sugar alcohols by 3-(4-hydroxyphenyl)propionic acid

Enzymatic synthesis of aromatic esters of four different sugar alcohols (xylitol, arabitol, mannitol, and sorbitol) with 3-(4-hydroxyphenyl)propionic acid was performed in organic solvent medium, using immobilized Candida antarctica lipase (Novozyme 435), and molecular sieves for control of the water content. The influence of reaction parameters on the conversion has been investigated, including reaction time, temperature, alcohol/acid molar ratio, and enzyme amount. The highest conversions (94% for xylitol, 98% for arabitol, 80% for mannitol, and 93% for sorbitol) were obtained in pure tert-butanol at 60 °C and 72 h reaction time, 0.3 alcohol/acid molar ratio, and 0.5 g/mol enzyme/substrate ratio. The isolated new sugar alcohols esters were identified by different spectral analyses. MALDI-TOF MS analysis showed the formation of monoesters, diesters, and small quantities of triesters for all investigated sugar alcohols. The catalytic efficiency of the enzyme was higher for the pentitol substrates, decreasing in the following order: arabitol > xylitol > sorbitol > mannitol. These new compounds could have interesting applications in food, pharmaceutical and cosmetic formulations.     

Enzymatic hydrolysis of racemic ibuprofen esters using Rhizomucor miehei lipase immobilized on different supports

This research describes the immobilization of Rhizomucor miehei lipase (RML) and chemically aminated RML (NH₂-RML) on different supports including octyl-sepharose (octyl-RML), activated sepharose with cyanogen bromide (CNBr-RML and CNBr-NH₂-RML), glyoxyl sepharose (Gx-RML and Gx-NH₂-RML) and glyoxyl sepharose dithiothreitol (Gx-DTT-RML and Gx-DTT-NH₂-RML). The highest immobilization yield was achieved for octyl-RML (>98%) followed by CNBr-RML (88%). Octyl-RML had the most specific activity (13.6) among all derivatives. The other preparations had moderate activities likely because of chemical reaction during covalent attachment of the enzyme. The catalytic behavior of lipase immobilized in hydrolysis reactions was investigated using methyl, ethyl, propyl, butyl and isobutyl-ibuprofen esters and the influence of the alkyl chain and the alcoholic residue of the ester were studied. Butyl ester was the most interesting ester for carrying out hydrolysis. The highest enantioselectivity of enzyme (E = 8.8) was obtained with isooctane/sodium phosphate buffer pH 7.0 at temperature of 40 °C. Increasing temperature from 40 to 50 °C caused decreasing in enantioselectivities and conversions. Also esterification of ibuprofen was carried out in solvent systems containing isooctane and two ionic liquids (ILs); [BMIM][PF₆] and [BMIM][BF₄]. Poor conversions and enantioselectivities were observed during esterification in all solvents.     

An organic solvent and thermally stable lipase from Burkholderia ambifaria YCJ01: Purification,characteristics and application for chiral resolution of mandelic acid

A solvent-tolerant bacterium Burkholderia ambifaria YCJ01 was newly isolated by DMSO enrichment of the medium. The lipase from the strain YCJ01 was purified to homogeneity with apparent molecular mass of 34 kDa determined by SDS-PAGE. The purified lipase exhibited maximal activity at a temperature of 60 °C and a pH of 7.5. The lipase was very stable below 55 °C for 7 days (remaining 80.3% initial activity) or at 30 °C for 60 days. PMSF significantly inhibited the lipase activity, while EDTA had no effect on the activity. Strikingly, the lipase showed distinct super-stability to the most tested hydrophilic and hydrophobic solvents (25%, v/v) for 60 days, and different optimal pH in contrast with the alkaline lipase from B. cepacia S31. The lipase demonstrated excellent enantioselective transesterification toward the S-isomer of mandelic acid with a theoretical conversion yield of 50%, ee_p of 99.9% and ee_s of 99.9%, which made it an exploitable biocatalyst for organic synthesis and pharmaceutical industries.     

A robust whole-cell biocatalyst that introduces a thermo- and solvent-tolerant lipase into Aspergillus oryzae cells: Characterization and application to enzymatic biodiesel production

To develop a robust whole-cell biocatalyst that works well at moderately high temperature (40–50 °C) with organic solvents, a thermostable lipase from Geobacillus thermocatenulatus (BTL2) was introduced into an Aspergillus oryzae whole-cell biocatalyst. The lipase-hydrolytic activity of the immobilized A. oryzae (r-BTL) was highest at 50 °C and was maintained even after an incubation of 24-h at 60 °C. In addition, r-BTL was highly tolerant to 30% (v/v) organic solvents (dimethyl carbonate, ethanol, methanol, 2-propanol or acetone). The attractive characteristics of r-BTL also worked efficiently on palm oil methanolysis, resulting in a nearly 100% conversion at elevated temperature from 40 to 50 °C. Moreover, r-BTL catalyzed methanolysis at a high methanol concentration without a significant loss of lipase activity. In particular, when 2 molar equivalents of methanol were added 2 times, a methyl ester content of more than 90% was achieved; the yield was higher than those of conventional whole-cell biocatalyst and commercial Candida antarctica lipase (Novozym 435). On the basis of the results regarding the excellent lipase characteristics and efficient biodiesel production, the developed whole-cell biocatalyst would be a promising biocatalyst in a broad range of applications including biodiesel production.     

Lipase-catalyzed synthesis of palmitanilide: Kinetic model and antimicrobial activity study

Enzymatic syntheses of fatty acid anilides are important owing to their wide range of industrial applications in detergents, shampoo, cosmetics, and surfactant formulations. The amidation reaction of Mucor miehei lipase Lipozyme IM20 was investigated for direct amidation of triacylglycerol in organic solvents. The process parameters (reaction temperature, substrate molar ratio, enzyme amount) were optimized to achieve the highest yield of anilide. The maximum yield of palmitanilide (88.9%) was achieved after 24 h of reaction at 40 °C at an enzyme concentration of 1.4% (70 mg). Kinetics of lipase-catalyzed amidation of aniline with tripalmitin has been investigated. The reaction rate could be described in terms of the Michaelis–Menten equation with a Ping–Pong Bi–Bi mechanism and competitive inhibition by both the substrates. The kinetic constants were estimated by using non-linear regression method using enzyme kinetic modules. The enzyme operational stability study showed that Lipozyme IM20 retained 38.1% of the initial activity for the synthesis of palmitanilide (even after repeated use for 48 h). Palmitanilide, a fatty acid amide, exhibited potent antimicrobial activity toward Bacillus cereus.     

High catalytic performances of Pseudomonas fluorescens lipase adsorbed on a new type of cyclodextrin-based nanosponges

Lipases are water-soluble enzymes that catalyze the hydrolysis of triacylglycerols (in aqueous media) or trans-esterification reactions (in microaqueous media) and are involved in a number of industrial applications. As a limit to lipase application is represented by the need for interfacial activation, the search for suitable solid supports able to fulfill this requirement is always ongoing. In the present work, we report the preliminary characterization of a system obtained by adsorbing Pseudomonas fluorescens lipase on a newly synthesized cyclodextrin-based carbonate nanosponge (CD–NS–1:4). The activity and structural stability of lipase adsorbed on this new support were evaluated by checking the effect of temperature, pH changes and organic solvents (methanol) on the enzyme structure and function, which were compared with those of the free enzyme in solution. Our data show that the non-covalent interaction of Ps. fluorescens lipase with CD–NS–1:4 results in enzyme structural and functional stabilization, as it was still active after 66 days of incubation at T ～ 18 °C. Stabilization with respect to T, pH and the presence of organic solvent was observed as well as, unlike the solubilized enzyme, the adsorbed lipase was active at T > 40 °C, at pH 5 and after 24-h incubation with 70% (v/v) methanol (13% residual activity).     

Isoamyl acetate synthesis in imidazolium-based ionic liquids using packed bed enzyme microreactor

The acylation of isoamyl alcohol with acetic anhydride catalyzed by immobilized Candida antarctica lipase B was studied in ionic liquids (ILs) based on quaternary imidazolium cations with alkyl, alkenyl, alkynyl, benzyl, alkoxyl or N-aminopropyl side chains. Among the tested ILs, the highest enzyme activity together with the highest isoamyl acetate yield were obtained in [C₇mmim][Tf₂N]. No loss of lipase B activity was observed during one-month incubation in this hydrophobic IL without the presence of substrates. Isoamyl acetate synthesis using [C₇mmim][Tf₂N] as solvent was further studied in a continuously operated miniaturized enzymatic packed bed reactor at various flow rates and temperatures. Up to 92% isoamyl acetate yield could be obtained within 15 min by using 0.5 M acetic anhydride and 1.5 M isoamyl alcohol inlet concentrations at 55 °C, corresponding to the volumetric productivity of 61 mmol l^?1 min^?1, which to the best of our knowledge is the highest reported so far for this reaction. No decrease in productivity was experienced during the subsequent runs of continuous microbioreactor operation performed within 14 consecutive days. The benefits of reactor miniaturization along with the green solvent application were therefore successfully exploited for the development of a sustainable flavour ester production.     

A novel mono- and diacylglycerol lipase highly expressed in Pichia pastoris and its application for food emulsifier preparation

A mono- and diacylglycerol lipase (MDL) was cloned from Penicillium cyclopium and expressed in Pichia pastoris strain GS115. The recombinant enzyme was named Lipase GH1. High cell density fermentation was performed by culture in a 7.5-L fermenter using BSMG medium, in which the phosphate in basal salt medium was replaced by sodium glycerophosphate (Na₂GP). The maximal lipase activity detected was 18,000 U per mL, and total protein content in the fermentation supernatant was 3.94 g per L. The activity of the liquid enzyme remained stable under alkaline conditions at 4 °C for 6 months and was 50% after one year. Lipase GH1 was used for the synthesis of mono- and diacylglycerols (MAGs and DAGs), which are commonly used emulsifiers for industrial applications. A conversion rate of 84% after 24 h of reaction was obtained using glycerol/oleic acid molar ratio 11:1, water content 1.5 wt%, enzyme dosage 80 U per g, and reaction temperature 35 °C. Lipase GH1 was more efficient for the synthesis of MAGs and DAGs than was Lipase G50 (a similar, commercially available lipase derived from Penicillium camemberti) when oleic acid was used as an acyl donor. Lipase GH1 has potential for food emulsifier preparation.     

Esterification activity and stability of Talaromyces thermophilus lipase immobilized onto chitosan

The Talaromyces thermophilus lipase (TTL) was immobilized by different methods namely adsorption, ionic binding and covalent coupling, using various carriers. Chitosan, pre-treated with glutaraldehyde, was selected as the most suitable support material preserving the catalytic activity almost intact and offering maximum immobilization capacity (76% and 91%, respectively). The chitosan-immobilized lipase could be reputably used for ten cycles with more than 80% of its initial hydrolytic activity. Shift in the optimal temperature from 50 to 60 °C and in the pH from 9.5 to 10, were observed for the immobilized lipase when compared to the free enzyme.The catalytic esterification of oleic acid with 1-butanol has been carried out using hexane as organic solvent. A high performance synthesis of 1-butyl oleate was obtained (95% of conversion yield) at 60 °C with a molar ratio of 1:1 oleic acid to butanol and using 100 U (0.2 g) of immobilized lipase. The esterification product is analysed by GC/MS to confirm the conversion percentage calculated by titration.     

Enhancing performance of lipase immobilized on methyl-modified silica aerogels at the adsorption and catalysis processes: Effect of cosolvents

Hydrophobic silica aerogels modified with methyl group were applied as support to immobilize Candida rugosa lipase (CRL). At the adsorption process, different alcohols were used to intensify the immobilization of CRL. The results showed that n-butanol wetting the hydrophobic support prior to contacting with enzyme solution could promote lipase activity, but the adsorption quantity onto the support decreased. Based on this, a novel immobilization method was proposed: the support contacted with enzyme solution without any alcohols, and then the immobilized enzymes were activated by 90% (V) n-butanol solution. The experimental results showed that this method could keep high adsorption quantity (413.0 mg protein/g support) and increase the lipase specific activity by more than 50%. To improve the stability of immobilized lipase, the support after adsorption was contacted with n-octane to form an oil layer covering the immobilized lipases, thus the leakage can be decreased from over 30–4% within 24 h. By utilizing proper cosolvents, a high enzyme activity and loading capacity as well as little loss of lipase was achieved without covalent linkage between the lipase and the support. This is known to be an excellent result for immobilization achieved by physical adsorption only.     

Characterization of a spore surface lipase from the biocontrol agent Metarhizium anisopliae

A Metarhizium anisopliae spore surface lipase (MASSL) strongly bound to the fungal spore surface has been purified by ion exchange chromatography on DEAE sepharose followed by ultrafiltration and hydrophobic interaction chromatography on phenyl sepharose. Electrophoretic analyses showed that the molecular weight of this lipase is ～66 kDa and pI is 5.6. Protein sequencing revealed that identified peptides in MASSL shared identity with several lipases or lipase-related sequences. The enzyme was able to hydrolyze triolein, the animal lipid cholesteryl stearate and all ρNP ester substrates tested with some preference for esters with a short acyl chain. The values of K_m and V_max for the substrates ρNP palmitate and ρNP laurate were respectively 0.474 mM and 1.093 mMol min^?1 mg^?1 and 0.712 mM and 5.696 mMol min^?1 mg^?1. The optimum temperature of the purified lipase was 30 °C and the enzyme was most stable within the most acid pH range (pH 3–6). Triton X-100 increased and SDS reduced enzyme lipolytic activity. MASSL activity was stimulated by Ca²⁺, Mg²⁺ and Co²⁺ and inhibited by Mn²⁺. The inhibitory effect on activity exerted by EDTA and EGTA was limited, while the lipase inhibitor Ebelactone B completely inhibited MASSL activity as well as PMSF. Methanol 0.5% apparently did not affect MASSL activity while β-mercaptoethanol activated the enzyme.     

Homologous expression,purification and characterization of a novel high-alkaline and thermal stable lipase from Burkholderia cepacia ATCC 25416

The lipase secreted by Burkholderia cepacia ATCC 25416 was particularly attractive in detergent and leather industry due to its specific characteristics of high alkaline and thermal stability. The lipase gene (lipA), lipase chaperone gene (lipB), and native promoter upstream of lipA were cloned. The lipA was composed of 1095 bp, corresponding to 364 amino acid residues. The lipB located immediately downstream of lipA was composed of 1035 bp, corresponding to 344 amino acid residues. The lipase operon was inserted into broad host vector pBBRMCS1 and electroporated into original strain. The homologous expression of recombinant strain showed a significant increase in the lipase activity. LipA was purified by three-step procedure of ammonium sulfate precipitation, phenyl-sepharose FF and DEAE-sepharose FF. SDS-PAGE showed the molecular mass of the lipase was 33 kDa. The enzyme optimal temperature and pH were 60 °C and 11.0, respectively. The enzyme was stable at 30–70 °C. After incubated in 70 °C for 1 h, enzyme remained 72% of its maximal activity. The enzyme exhibited a good stability at pH 9.0–11.5. The lipase preferentially hydrolyzed medium-chain fatty acid esters. The enzyme was strongly activated by Mg²⁺, Ca²⁺, Cu²⁺, Zn²⁺, Co²⁺, and apparently inhibited by PMSF, EDTA and also DTT with SDS. The enzyme was compatible with various ionic and non-ionic surfactants as well as oxidant H₂O₂. The enzyme had good stability in the low- and non-polar solvents.     

Characterization of the lipase immobilized on Mg–Al hydrotalcite for biodiesel

Immobilization of Saccharomyces cerevisiae lipase by physical adsorption on Mg–Al hydrotalcite with a Mg/Al molar ratio of 4.0 led to a markedly improved performance of the enzyme. The immobilized lipase retained activity over wider ranges of temperature and pH than those of the free lipase. The immobilized lipase retained more than 95% relative activity at 50 °C, while the free lipase retained about 88%. The kinetic constants of the immobilized and free lipases were also determined. The apparent activation energies (E_a) of the free and immobilized lipases were estimated to be 6.96 and 2.42 kJ mol^?1, while the apparent inactivation energies (E_d) of free and immobilized lipases were 6.51 and 6.27 kJ mol^?1, respectively. So the stability of the immobilized lipase was higher than that of free lipase. The water content of the oil must be kept below 2.0 wt% and free fatty acid content of the oil must be kept below 3.5 mg KOH g [oil]^?1 in order to get the best conversion. This immobilization method was found to be satisfactory to produce a stable and functioning biocatalyst which could maintain high reactivity for repeating 10 batches with ester conversion above 81.3%.     

Synthesis of structured lipids by two enzymatic steps: Ethanolysis of fish oils and esterification of 2-monoacylglycerols

This paper studies the synthesis of structured triacylglycerols (STAGs), rich in polyunsaturated fatty acids (PUFAs) by a two-step enzymatic process: (i) alcoholysis of fish oils (cod liver and tuna oils) with ethanol to obtain 2-monoacylglycerols (2-MAGs), catalyzed by 1,3 specific lipases and (ii) esterification of these 2-MAGs with caprylic acid (CA, 8:0), also catalyzed by a 1,3 specific lipase, to produce STAGs of structure CA–PUFA–CA. As regards the alcoholysis reaction, three factors have been studied: the influence of the type of lipase used (lipase D from Rhizopus oryzae, immobilized on Accurel MP1000, and Novozym 435 from Candida antarctica), the operational mode of a stirred tank reactor (STR operating in discontinuous and continuous mode) and the intensity of treatment (IOT = lipase amount × reaction time/oil amount). Although higher 2-MAG yields were obtained with lipase D, Novozym 435 was selected due to its greater stability in the operational conditions. The highest 2-MAG yield (63%) was attained in the STR operating in discontinuous mode at an IOT of 1 g lipase × h g oil^?1 (at higher IOT the 2-MAGs were degraded to glycerol). This system was scaled up to 100 times the initial volume, achieving a similar yield (65%) at the same IOT. The 2-MAGs in the final alcoholysis reaction mixture were separated from ethyl esters by solvent extraction using solvents of low toxicity (ethanol and hexane); the 2-MAG recovery yield was over 90% and the purity was approximately 87–90%. Regarding the esterification of the 2-MAGs, the following factors were studied: the influence of the lipase type used, the presence or absence of solvent (hexane) and the reaction time or intensity of treatment (IOT = lipase amount × reaction time/2-MAG amount). Of the five lipases tested, the highest STAG percentages (over 90%) were attained with lipases D and DF, immobilized on Accurel MP1000. These STAGs contain 64% CA, of which 98% is at positions 1 and 3. Position 2 contains 5% CA and 45% PUFAs, which means that all the PUFAs that were located at position 2 in the original oil remain in that position in the final STAGs. The lipase D immobilized on Accurel MP1000 is stable in the operational conditions used in the esterification reaction. Finally the purification of STAGs was carried out by neutralization of free fatty acids with hydroethanolic solution of KOH and extraction of STAGs with hexane. By this method purity was over 95% and separation yields were about 80%.     

Esterification and transesterification reactions catalysed by addition of fermented solids to organic reaction media

We report for the first time both the production of the lipase of Burkholderia cepacia in solid-state fermentation and the biocatalysis of esterification and transesterification reactions through the direct addition of the lyophilised fermented solids to organic reaction media. B. cepacia produced a lipolytic activity equivalent to 108 U of pNPP-hydrolysing activity per gram of dry solids after 72 h growth on corn bran with 5% (v/w) commercial corn oil as the inducer. The fermented solid material was lyophilised and added directly to the reaction medium in esterification and transesterification reactions. A factorial design was used to study the effects on esterification of temperature, alcohol-to-acid molar ratio and amount of lipolytic activity added. All three variables affected the ester yield significantly, with the amount of enzyme being most important. A 94% ester yield was obtained at 18 h at 37 °C, with an alcohol-to-acid molar ratio of 5:1 and 60 U of added lipolytic activity. For the transesterification reaction, a factorial design was undertaken with the variables being the alcohol-to-acid molar ratio and the added lipolytic activity. Ester yields of over 95% were obtained after 120 h. Our results suggest that biocatalysis using direct addition of fermented solids to organic reaction medium should be further explored.     

Lipase-catalyzed hydrazinolysis of phenyl benzoate: Kinetic modeling approach

Immobilized lipase-catalyzed synthesis of benzoic acid hydrazide from hydrazine and phenyl benzoate is reported in this work. A series of immobilized lipases such as Candida antarctica lipase B, Mucor miehei lipase and Thermomyces lanuginosus lipase were screened to establish that C. antarctica lipase B was the best lipase for hydrazinolysis. When phenyl benzoate (0.01 mol) and hydrazine (0.02 mol) in toluene (15 ml) were reacted with C. antarctica lipase B (Novozym 435) at 50 °C, 95% of phenyl benzoate was converted to benzoic acid hydrazide after 2 h. The effects of various parameters such as speed of agitation, concentration of the substrates, temperature, enzyme concentration, and reusability of the enzyme were studied to deduce kinetics and mechanism of the reaction. A mechanism based on an ordered bi–bi dead end complex with hydrazine was found to fit the data. Systematic deactivation studies indicated that the enzyme was deactivated due to the hydrazine and phenol, enzyme deactivation obeys first-order series model. The kinetic parameters deduced from these models were used to simulate the lipase activity. There was a very good agreement between the simulated and experimental values.     

Kinetics and optimization of lipase-catalyzed synthesis of rose fragrance 2-phenylethyl acetate through transesterification

Lipase from Candida rugosa was immobilized on a polyvinylidene fluoride membrane for synthesis of rose flavor ester, 2-phenylethyl acetate. Response surface methodology (RSM) was employed for kinetic modeling of process and prediction the yield. The RSM was used in practice for determining the kinetic models by fitting the initial rate dates based on the equations of ping-pong bi–bi and order bi–bi model. The maximum reaction rate and kinetic constants were matched with the order bi–bi model. The specificity constant of the immobilized lipase was 10-folds higher than the free form indicated the enzyme–substrate affinity, and catalytic ability was enhanced after immobilization. Moreover, the effects of reaction parameters on the yield were evaluated by RSM using a Box–Behnken experimental design. Based on a ridge max analysis, the maximum conversion was 95.33 ± 2.57% at 38.78 h, 35.85 °C, and substrate mole ratio of 3.65:1. Furthermore, the order bi–bi kinetic model was simulated successfully in a batch reaction. A good prediction existed between the RSM results and integrated equation was found.