pH-optima in lipase-catalysed esterification

Though lipases are frequently applied in ester synthesis, fundamental information on optimal pH or substrate concentration, can almost only be found for the reverse reaction - hydrolysis. This study demonstrates that the pH-optima of lipase-catalysed esterifications differ significantly from the optima of the hydrolysis reaction. In the esterification of n-butanol and propionic acid with lipases of Candida rugosa (CRL) and Thermomyces lanuginosa (TLL) pH-optima of 3.5 and 4.25, respectively, were found. This is about 3-4 units (CRL) and 7 units (TLL) in pH lower than optimum for hydrolysis. Enzyme activity increased with increasing concentrations of protonated acid indicating that the protonated acid rather than the deprotonated form is substrate for esterification. The rate of esterification can be drastically increased by ensuring acid concentrations up to 1000 mmol L^-1 for CRL and 600 mmol L^-1 for TLL in the reaction system.     

Response surface methodology-based optimization of glucose acylation bio-catalyzed by immobilized lipase

This paper describes in detail the selection and optimization of immobilized lipases for enhanced regioselective acylation of glucose into glucose monolaurate (GlcML). Initially, nature of biocatalyst, immobilization approach, reaction media, glucose, and lauric acid concentration were screened out. Finally, lipases from Rhizopus arrhizus immobilized on dead mycelia were investigated under various reaction conditions (Temperature, shaking speed, enzyme dose, and water content) following a fully rotatable central composite design (FRCCD) to optimize the activity of lipases. The immobilized lipases-based biocatalysts in the presence of polar solvents (tertiary alcohols) and higher concentrations of substrates i.e. glucose and lauric acid (100 and 300?mmol?L^?1, respectively) offered conversion rate of 1.5 mmolmin^?1?L^?1. Moreover, optimization of reaction conditions revealed that 162.5 lipase units/100mL at 31.25?°C, 3% water content, and 105?RPM shaking speed enhanced the conversion rate by 0.5 mmolmin^?1?L^?1 rendering the reaction more economical. Hence, lipases-based immobilized biocatalysts may provide an intelligent and green choice for commercial scale synthesis of GlcML for food and pharmaceutical industries.     

Production of Ricinoleic Acid from Castor Oil by Immobilised Lipases

Abstract

Porcine pancreatic lipase (PPL), Candida rugosa lipase (CRL), and Castor bean lipase (CBL) were immobilized on celite by deposition from aqueous solution by the addition of hexane. Lipolytic performance of free and immobilized lipases were compared and optimizations of lipolytic enzymatic reactions conditions were performed by free and immobilized derivatives using olive oil as substrate. Afterwards, the influence on lipolysis of castor oil of free lipases and immobilized lipase derivatives have been studied in the case of production of ricinoleic acid. All of the lipases performances were compared and enzyme derivative was selected to be very effective on the production of ricinoleic acid by lipolysis reaction. Various reaction parameters affecting the production of ricinoleic acid were investigated with selected the enzyme derivative.

The maximum ricinoleic acid yield was observed at pH 7–8, 50°C, for 3 hours of reaction period with immobilized 1,3-specific PPL on celite. The kinetic constants K_m and V_max were calculated as 1.6 × 10^?4 mM and 22.2 mM from a Lineweaver–Burk plot with the same enzyme derivative. To investigate the operational stability of the lipase, the three step lipolysis process was repeated by transferring the immobilized lipase to a substrate mixture. As a result, the percentange of conversion after usage decreased markedly.     

Enzymatic synthesis of ethyl esters from waste oil using mixtures of lipases in a plug‐flow packed‐bed continuous reactor

This work describes the continuous synthesis of ethyl esters via enzymatic catalysis on a packed‐bed continuous reactor, using mixtures of immobilized lipases (combi‐lipases) of Candida antarctica (CALB), Thermomyces lanuginosus (TLL), and Rhizomucor miehei (RML). The influence of the addition of glass beads to the reactor bed, evaluation of the use of different solvents, and flow rate on reaction conditions was studied. All experiments were conducted using the best combination of lipases according to the fatty acid composition of the waste oil (combi‐lipase composition: 40% of TLL, 35% of CALB, and 25% of RML) and soybean oil (combi‐lipase composition: 22.5% of TLL, 50% of CALB, and 27.5% of RML). The best general reaction conditions were found to be using tert‐butanol as solvent, and the flow rate of 0.08 mL min^?1. The combi‐lipase reactors operating at steady state for over 30 days (720 h), kept conversion yields of ～50%, with average productivity of 1.94 g_{ethyl esters} h^?1, regardless of the type of oil in use. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:952–959, 2018     

Production of precursors for anti-Alzheimer drugs: Asymmetric bioreduction in a packed-bed bioreactor using immobilized D. carota cells

(S)-1-Phenylethanol derivatives, which are the precursors of many pharmacological products, have also been used as anti-Alzheimer drugs. Bioreduction experiments were performed in a batch and packed-bed bioreactor. Then, the kinetics constants were determined by examining the reaction kinetics in the batch system with free and immobilized carrot cells. Also, the effective diffusion coefficient (D_e) of acetophenone in calcium alginate-immobilized carrot cells was investigated. Kinetics constants for free cells, which are intrinsic values, are reaction rate V_max?=?0.052?mmol?L^?1?min^?1, and constants of the Michaelis–Menten K_M?=?2.31?mmol?L^?1. Kinetics constants for immobilized cells, which are considered apparent values, are V_{max, app}?=?0.0407?mmol?L^?1 min^?1, K_{M, app}?=?3.0472?mmol?L^?1 for 2?mm bead diameter, and V_{max, app}?=?0.0453?mmol?L^?1 min^?1, K_{M, app}?=?4.9383?mmol?L^?1 for 3?mm bead diameter. Average value of effective diffusion coefficient of acetophenone in immobilized beads was determined as 1.97?×?10^?6?cm²?s^?1. Using immobilized carrot cells in an up-flow packed-bed reactor, continuous production of (S)-1-phenylethanol through asymmetric bioreduction of acetophenone was performed. The effects of the residence time and concentrations of substrate were investigated at pH 7.6 and 33°C. Enantiomerically pure (S)-1-phenylethanol (ee?>?99%) was produced with 75% conversion at 4-hr residence time.     

Application of central composite rotatable design to lipase catalysed synthesis of m-cresyl acetate

Esterification of m-cresol with acetic acid using porcine pancreas lipase (PPL) was investigated by response surface methodology (RSM). A central composite rotatable design (CCRD) involving 32 experiments of five variables at five levels was employed to analyse the esterification behaviour. The effect of five variables studied namely, m-cresol concentrations (0.005–0.025 mol), enzyme/substrate ratios (0.18–1.22 activity units/millimol, AU/mmol), incubation periods (6–54 h), pH (4–8) and buffer volumes (0–0.2 ml) was useful in arriving at an optimum ester yield. The methodology projected conditions for higher yields up to 6.0 mmol. Validation experiments carried out under these predicated conditions showed good correspondence between experimental and predicted yields. CCRD treatment clearly showed the inhibitory nature of m-cresol in the esterification process. The reaction required the presence of buffer for better conversions and a minimum amount of 0.1 ml buffer was found necessary for this reaction. Buffer pH values around 6.0 and below appeared to favour better esterification than those at pH values in the range 6.0–8.0. However an optimum condition for maximum yield was: incubation period: 54 h; buffer volume: 0.2 ml; pH: 8; E/S ratio: 0.83 AU/mmol; m-cresol: 0.02 mol; predicted yield: 6.0 mmol; experimental yield: 6.4 mmol.     

Optimization of enzymatic hydrolysis and fermentation conditions for improved bioethanol production from potato peel residues

The aim of this work was the optimization of the enzyme hydrolysis of potato peel residues (PPR) for bioethanol production. The process included a pretreatment step followed by an enzyme hydrolysis using crude enzyme system composed of cellulase, amylase and hemicellulase, produced by a mixed culture of Aspergillus niger and Trichoderma reesei. Hydrothermal, alkali and acid pretreatments were considered with regards to the enhancement of enzyme hydrolysis of potato peel residues. The obtained results showed that hydrothermal pretreatment lead to a higher enzyme hydrolysis yield compared to both acid and alkali pretreatments. Enzyme hydrolysis was also optimized for parameters such as temperature, pH, substrate loading and surfactant loading using a response surface methodology. Under optimized conditions, 77 g L^?1 of reducing sugars were obtained. Yeast fermentation of the released reducing sugars led to an ethanol titer of 30 g L^?1 after supplementation of the culture medium with ammonium sulfate. Moreover, a comparative study between acid and enzyme hydrolysis of potato peel residues was investigated. Results showed that enzyme hydrolysis offers higher yield of bioethanol production than acid hydrolysis. These results highlight the potential of second generation bioethanol production from potato peel residues treated with onsite produced hydrolytic enzymes. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:397–406, 2017     

Improved production of (R)-2-octanol via asymmetric reduction of 2-octanone with Oenococcus oeni CECT4730 in a biphasic system

Abstract

Oenococcus oeni CECT4730, which catalyses the asymmetric reduction of 2-octanone to (R)-2-octanol with high enantioselectivity, was further studied to exploit its potential for production of (R)-2-octanol in an aqueous/organic solvent biphasic system. Variables such as the volume ratio of aqueous to organic phase (V_a/V_o), buffer pH, reaction temperature, shaking speed, co-substrates and the ratio of biocatalyst to substrate were examined with respect to the molar conversion, the initial reaction rate and the product enantiomeric excess (e.e.). Under the optimized conditions (V_a/V_o=1:1 (v/v), buffer pH=8.0, reaction temperature=30°C, shaking speed=150 rev/min, ratio of glucose to biomass=5.4:l (w/w), ratio of biocatalyst to substrate=0.51:l (g/mol)), the highest space time yield of (R)-2-octanol, 24 mmol L^?1 per h, and >98% product e.e. were obtained at a substrate concentration close to 1.0 mol L^?1 after 24 h reduction.     

Preparation of stearoyl lactic acid ester catalyzed by lipases from Rhizomucor miehei and porcine pancreas optimization using response surface methodology

The esterification reaction between stearic acid and lactic acid using Rhizomucor miehei lipase and porcine pancreas lipase was optimized for maximum esterification using response surface methodology. The formation of the ester was found to depend on three parameters namely enzyme/substrate ratio, lactic acid (stearic acid) concentration and incubation period. The maximum esterification predicted by theoretical equations for both lipases matched well with the observed experimental values. In the case of R. miehei lipase, stearoyl lactic acid ester formation was found to increase with incubation period and lactic acid (stearic acid) concentrations with maximum esterification of 26.9% at an enzyme/substrate (E/S) ratio of 125 g mol⁻¹. In the case of porcine pancreas lipase, esterification showed a steady increase with increase in incubation period and lactic acid (stearic acid) concentration independent of the E/S ratios employed. In the case of PPL, a maximum esterification of 18.9% was observed at an E/S ratio of 25 g mol⁻¹ at a lactic acid (stearic acid) concentration of 0.09 M after an incubation period of 72 h. Received: 12 February 1999 / Received revision: 31 May 1999 / Accepted: 4 June 1999     

Substrate selectivity of various lipases in the esterification of cis- and trans-9-octadecenoic acid

The substrate selectivity of numerous commercially available lipases from microorganisms, plants and animal tissue towards 9-octadecenoic acids with respect to the cis/trans configuration of the CC double bond was examined by the esterification of cis- and trans-9-octadecanoic acid (oleic and elaidic acid respectively) with n-butanol in n-hexane. A great number of lipases studied, e.g. those from Pseudomonas sp., porcine pancreas or Carica papaya, were unable to discriminate between the isomeric 9-octadecenoic acids. However, lipases from Candida cylindracea and Mucor miehei catalysed the esterification of oleic acid 3–4 times faster than the corresponding reaction of elaidic acid and therefore have a high preference for the cis isomer. Of all biocatalysts examined, only recombinant lipases from Candidaantarctica favoured elaidic acid as substrate. While the preference of Candida antarctica lipase B for the trans isomer was quite low, Candida antarctica lipase A had an extraordinary substrate selectivity and its immobilized enzyme preparation [Chirazyme L-5 (3) from Boehringer] esterified elaidic acid about 15 times faster than oleic acid. Received: 29 October 1998 / Received revision: 18 December 1998 / Accepted: 21 December 1998     

The effects of pH and dissolved inorganic carbon on external carbonic anhydrase activity in Chlorella saccharophila

External carbonic anhydrase (CA) activity in Chlorella saccharophila is suppressed by growth at high dissolved inorganic carbon and at acid pH. External CA activity was shown to be suppressed by growth at pHs below 7.0, with total repression at pH5.0. Growth in the presence of the buffer 3-[N-Morpholino]propane-sulphonic acid (MOPS) between pH 7 and 8 suppressed CA activity. Cells grown at pH8.0 aerated at 6 dm³ h^?1 exhibited external CA activity of 5 units mg^?1 Chl once the dissolved inorganic carbon (DIC) was reduced to 300 mmol m^?3, and this increased to 30 units mg^?1 Chl over a period of 3d while the DIC dropped to 30mmol m^?3. Cells aerated at 180 dm³ h^?1 showed a similar trend in CA activity, although the onset was delayed by 1 d and the DIC did not drop below 300 mmol m^?3. Cells grown at pH 7.8 near an air equilibrium DIC of 300 mmol m^?3had no detectable external CA activity. It is probable that it is the CO² supply to the cell, and not total DIC or HCO^?₃ which controls external CA activity. Cells grown at pH 5.0 had no detectable activity, although they reduced the CO² concentration to 0.6 mmol m^?3. The loss of CA upon transfer of air-grown cells to 10 mmol mol^?1 CO² took place over 48 h and was light dependent, while the loss upon transfer from alkaline pH to acid pH look place over 12 h and was independent of light. The effects of pH are independent of the response to CO₂.     

Discrimination between rival laccase inhibition models from data sets with one inhibitor concentration using a penalized likelihood analysis and Akaike weights

Laccase from the white-rot fungus Fomes fomentarius was used for the biodegradation of ferulic acid (FA) in the presence of chloride anions. The initial reaction rates of substrate depletion were obtained by reverse-phase HPLC determination of remaining FA since substrate and reaction products have absorption peaks at similar wavelengths. Modelling of time-course data was accomplished by discrimination of the best enzyme inhibition equation from an initial set of seven different models based on Michaelis–Menten kinetics: competitive; uncompetitive; non-competitive; mixed; mixed hyperbolic; mixed parabolic; mixed hyperbolic and parabolic. Corrected Akaike information criterion was used to evaluate the relative merit of each kinetic model in order to rank them and find the more likely one. The discrimination results showed that the models with higher probabilities were the competitive and mixed inhibition types, but Akaike weights supported the selection of competitive inhibition (CI). After optimization by nonlinear regression, laccase kinetic parameters of FA biodegradation in the presence of chloride anions were: V_max?=?0.11?μmol?min^?1?mg^?1, K_m?=?44?μmol?L^?1 and a CI constant K_ic?=?14?mmol?L^?1.     

Lipase-catalyzed esterification of conjugated linoleic acid with <Emphasis Type="SmallCaps">l</Emphasis>-carnitine in solvent-free system and acetonitrile

Lipase-catalyzed esterification of conjugated linoleic acid (CLA) with l-carnitine in solvent-free system and acetonitrile was studied. Three lipases (Novzym 435, Amamo AY30 and Amano AYS) have been assayed as suitable biocatalysts in the reaction. It was found that Amano AY30 was the most effective biocatalyst in both solvent-free system and acetonitrile. The conversion rate varied from 8.05 to 60.9% in terms of reaction conditions such as the amount of lipase, the presence of water, the amount of molecular sieves and reaction time. The conversions of substrate in solvent-free system were higher than that in acetonitrile. When the substrates were 1 mmol CLA and 1 mmol l-carnitine, the maximum conversion (60.9%) was obtained in solvent-free system with 150 mg lipase AY30, 50% water content and 150 mg molecular sieves at the reaction time of 24 h. A novel CLA ester product was successfully isolated and characterized by ESI-MS and ¹H NMR.     

A study on the enzyme catalysed enantioselective hydrolysis of methyl 2-methyl-4-oxopentanoate,a precursor of chiral γ-butyrolactones

Porcine pancreas lipase (PPL) resolution of the α-methyl group of racemic methyl 2-methyl-4-oxopentanoate, a valuable synthetic precursor of fragrances and marine natural products, was enhanced by salt modulation of the enzymatic hydrolysis. For the enantioselective hydrolysis of the title ester, PPL was selected from a series of esterases and lipases, and its enantioselectivity was evaluated by changing the reaction medium parameters. The use of 1.6?mol L^–1 sodium sulfate in phosphate buffer (pH 7.2) improved the enantioselectivity allowing the formation of methyl (2R)-(+)-2-methyl-4-oxopentanoate and (2S)-(–)-2-methyl-4-oxopentanoic acid with an enantiomeric excess of >99% and 71%, respectively. The study showed that a modulation of PPL enantioselectivity could be achieved by using kosmotropic salts in the reaction media. The present method consists of a practical and low-cost option to improve enzymatic kinetic resolution reactions.     

Kinetic biosynthesis of l-ascorbyl acetate by immobilized Thermomyces lanuginosus lipase (Lipozyme TLIM)

Thermomyces lanuginosus lipase (Lipozyme TLIM)-catalyzed esterification of l-ascorbic acid was studied. It was suggested that Lipozyme TLIM was a suitable biocatalyst for enzymatic esterification of l-ascorbic acid. Three solvents were investigated for the reaction, and acetone was found to be a suitable reaction medium. Furthermore, it was found that water activity could notably affect the conversion. Moreover, pH memory of Lipozyme TLIM lipase for catalyzing l-ascorbic acid esterification in acetone was observed and the effect of pH on the reaction was estimated. In addition, the influences of other parameters such as substrate mole ratio, enzyme loading, and reaction temperature and reusability of lipase on esterification of l-ascorbic acid were also analyzed systematically and quantitatively. Kinetic characterization of Lipozyme TLIM showed that K _m,a and V _max were 80.085 mM and 0.747 mM min⁻¹, respectively. As a result, Lipozyme TLIM-catalyzed esterification of l-ascorbic acid gave a maximum conversion of 99%.     

Morphological,biochemical and kinetic properties of lipase from Candida rugosa immobilized in zirconium phosphate

Zirconium phosphate (ZrP), a low-cost inorganic material with well-defined physicochemical properties, was successfully used as support for immobilizing Candida rugosa lipase by covalent bonding. The immobilized derivative showed high catalytic activity in both aqueous and non-aqueous media. Fourier transform infrared spectroscopy, X-ray diffraction, and scanning electron microscopy measurements demonstrated that the ZrP fulfilled the morphological requirements for use as a matrix for immobilizing lipases. The free and immobilized lipases were compared in terms of pH, temperature and thermal stability. The immobilized lipase had a higher pH optimum (7.5) and higher optimum temperature (50°C) than the free lipase. Immobilization also increased the thermal stability. The hydrolysis of p-nitrophenyl palmitate (pNPP) by immobilized lipase, examined at 37°C, followed Michaelis–Menten kinetics. Values for K_m=1.18 µM and V_max=325Umg^?1 indicated that the immobilized system was subject to mass transfer limitations. The immobilized derivative was also tested under repetitive reaction batches in both ester hydrolysis and synthesis.     

Inducibility of Rat Liver Drug-Metabolizing Enzymes as an Index of Food-Screeing for Safety Assessment

D-Lactate dehydrogenase (D-LDH) from Pediococcus pentosaceus ATCC 25745 was found to produce D-3-phenyllactic acid from phenylpyruvate. The optimum pH and temperature for enzyme activity were pH 5.5 and 45 °C. The Michaelis-Menten constant (K _m), turnover number (k _cat), and catalytic efficiency (k _cat?K _m) values for the substrate phenylpyruvate were estimated to be 1.73 mmol/L, 173 s^?1, and 100 (mmol/L)^?1 s^?1 respectively.     

Molecular Modelling Studies on the Catalytic Mechanism of Candida Rugosa Lipase

Quantum chemical and molecular dynamics investigations have been performed on model systems for Candida rugosa lipase (CRL) to study mechanistic and conformational features of the catalytic hydrolysis. Based on X-ray data, a simplified model of the CRL substrate complex was created for the PM3 and ab initio calculations, including the amino acid residues both of the catalytic triad and the oxyanion hole.The energetic and structural properties of significant species along the pathway of the hydrolysis of the model substrate acetic acid methyl ester have been calculated. By modifications of the residues of the oxyanion hole as well as the catalytic triad, the influence of these parts of the active site on the pathway of the reaction was analysed in more detail.Moreover, molecular dynamics simulations have been carried out on CRL adducts with (±)-cis-4-acetamido-cyclopent-2-ene-1-carboxylic esters with different lengths of their alkyl chain and their absolute configuration as substrates. For the MD simulations using the AMBER program, all amino acid residues and water molecules with a cut-off radius less than 1500 pm from the substrate were taken into account. From the analysis of the trajectories and histograms for significant hydrogen bonds in the active site of the enzyme adducts, some hints were obtained for the enantiodifferentiation and the chain dependence of the esters in catalytic hydrolysis by CRL.Electronic Supplementary Material available.     

A Study on the Process of Lipase-catalyzed Synthesis of α-pinene Oxide in Organic Solvents

The synthesis of α-pinene oxide was studied in a three-phase system where immobilized Candida antarctica lipase B (Novozyme 435) was used to catalyze the formation of peroxyoctanoic acid from the parent carboxylic acid and hydrogen peroxide in toluene. The peroxycarboxylic acid formed was then used in situ for the oxidation of α-pinene to the corresponding epoxide. When hydrogen peroxide was added in the reaction mixture gradually over 6 h, conversions increased up to 31.6%. Initial rates of α-pinene oxidation increased from 85 to 708 mmol L^?1 h^?1 when the amount of H₂O₂ increased from 5 to 60 mmol. When the lipase was exposed to 75 mmol H₂O₂ for 0.5 h before its addition in the reaction mixture, its activity decreased to about 50%. The reusability of lipase was studied in five reaction cycles and was found to depend on the concentration of the hydrogen peroxide used.     

Butanol production from sweet sorghum bagasse with high solids content: Part I—comparison of liquid hot water pretreatment with dilute sulfuric acid

In these studies, we pretreated sweet sorghum bagasse (SSB) using liquid hot water (LHW) or dilute H₂SO₄ (2 g L^?1) at 190°C for zero min (as soon as temperature reached 190°C, cooling was started) to reduce generation of sugar degradation fermentation inhibiting products such as furfural and hydroxymethyl furfural (HMF). The solids loading were 250–300 g L^?1. This was followed by enzymatic hydrolysis. After hydrolysis, 89.0 g L^?1 sugars, 7.60 g L^?1 acetic acid, 0.33 g L^?1 furfural, and 0.07 g L^?1 HMF were released. This pretreatment and hydrolysis resulted in the release of 57.9% sugars. This was followed by second hydrolysis of the fibrous biomass which resulted in the release of 43.64 g L^?1 additional sugars, 2.40 g L^?1 acetic acid, zero g L^?1 furfural, and zero g L^?1 HMF. In both the hydrolyzates, 86.3% sugars present in SSB were released. Fermentation of the hydrolyzate I resulted in poor acetone‐butanol‐ethanol (ABE) fermentation. However, fermentation of the hydrolyzate II was successful and produced 13.43 g L^?1 ABE of which butanol was the main product. Use of 2 g L^?1 H₂SO₄ as a pretreatment medium followed by enzymatic hydrolysis resulted in the release of 100.6–93.8% (w/w) sugars from 250 to 300 g L^?1 SSB, respectively. LHW or dilute H₂SO₄ were used to economize production of cellulosic sugars from SSB. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:960–966, 2018