Optimization of Synthesis of Ethyl Isovalerate Using Rhizomucor miehei Lipase

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 a four-variable, five-level, central composite rotatable design was employed to optimize four important reaction variables—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; and temperature, 60°C. The predicted value matched well with the experimentally obtained value of 487 mM.     

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     

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.     

Optimization of isoamyl acetate production by using immobilized lipase from Mucor miehei by response surface methodology

Immobilized lipase from Mucor miehei was employed for the esterification of isoamyl alcohol with acetic acid in n-heptane solvent. The important process variables studied were enzyme/substrate (E/S) ratio, alcohol (acid) concentration, and incubation period. Based on Box-Behnken design of experiments, a second order response function was developed. The percentage esterification increased with both E/S ratio and time and decreased with alcohol (acid) concentration. The model indicated optimum conditions for maximum esterification ranging from 20 to 99.6% in the alcohol (acid) concentration range of 0.031 to 0.3 M for a range of E/S ratios 8.33 to 50 g/mol, which were in good agreement with the experimental yields.     

Modelling and experimental studies on lipase-catalyzed isoamyl acetate synthesis in a microreactor

A lipase-catalyzed synthesis of isoamyl acetate was studied in a continuously operated pressure-driven microreactor. The esterification of isoamyl alcohol and acetic acid occurred at the interface between n-hexane and an aqueous phase with dissolved lipase B from Candida antarctica. By adjusting flow rates of both phases, a parallel laminar flow with liquid–liquid boundary in the middle of the microchannel could be reestablished and a separation of phases was achieved at the y-shaped exit of the microreactor. Since product remained in the organic phase, this also enabled its continuous separation from the aqueous phase with the enzyme. A three-dimensional mathematical model was developed, considering the velocity profile developed for steady-state conditions between two immiscible fluids. The model contained convection, diffusion, and enzyme reaction terms, where esterification rate was described with a Ping-Pong Bi-Bi mechanism and inhibition by both substrates. Experimental data, which were in good agreement with model simulations, have demonstrated 35% conversion at residence time 36.5 s at 45 °C and at 0.5 M acetic acid and isoamyl alcohol inlet concentrations, which is much faster as in any literature reported so far. According to model simulations, obtained by non-equidistant finite differences numerical solutions of complex non-linear equations system, further microreactor design and process optimization are feasible.     

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.     

Scanning electron microscopic studies of lipase-catalysed esterification catalysis for the synthesis of stearoyl lactate and p-cresyl laurate

The state of three lipases, two from Rhizomucor miehei and one from porcine pancreas, employed in the esterification reactions leading to the preparation of food additive esters were investigated by scanning electron microscopy (SEM). The lipases employed in the synthesis of stearoyl lactic acid and p-cresyl laurate in 10 ml solvent at 40–60 °C in shake-flask experiments and 150 ml in non-polar solvents at 50–60 °C in bench-scale level experiments were compared. All three lipases, which were subjected to high temperatures and non-polar solvents for a prolonged period of incubation of 72–120 h, showed decrease in the compactness when compared to unused lipase. The presence of buffer preserved the activity and compactness and the absence of the same reduced the amount of enzyme per unit area on the support. R. miehei lipase samples subjected to reaction in presence of 0.0004 ml of 0.1 M buffer/mg enzyme preparation at different pH values (4.0–9.0) showed a decrease in compactness of the enzyme on the surface which correlated to an increase in esterification activity. An increase in volume of buffer (0.0002–0.003 ml/mg enzyme preparation) in the reaction mixture at pH 7.0 showed a decrease in compactness and also a reduction in activity. The studies indicate that a compromise between pH and volume of buffer can lead to variation in the extent of adsorption, distribution and activity, enabling the achievement of maximum conversions in the esterification reactions.     

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.     

Preparation of short chain esters by the lipase from mucor miehei using heptane and silica gel

Butyl acetate, isoamyl acetate and isoamyl valerate were prepared by Mucor miehei lipase catalyzed esterification of free acids and alcohols carried out in non-aqueous systems using heptane and silica gel which removes water formed in the reaction. For butyl and isoamyl acetate 1:3 and for isoamyl acetate 1:2 molar proportions of acid to alcohol were found to be optimal. Heptane(5 ml) and 0.01g silica gel per 0.1M acid were found to improve the yields. Under optimum conditions using 60°C, within 48 hours 40% butyl acetate, 53% isoamyl acetate and 61% isoamyl valerate conversions were observed.     

Enzymatic synthesis of isoamyl acetate using immobilized lipase from Rhizomucor miehei

The effects of important reaction parameters for enhancing isoamyl acetate formation through lipase-catalyzed esterification of isoamyl alcohol were investigated in this study. Increase in substrate (acid) concentration led to decrease in conversions. A critical enzyme concentration of 3 g l(-1) was detected for a substrate concentration of 0.06 M (each of alcohol and acid). Solvents with partition coefficient higher than 1000 (log P>3.0) supported enzyme activity to give high conversions. Acetic acid at higher concentrations could not be esterified easily probably owing to its role in lowering the microaqueous pH of the enzyme. Extraneous water/buffer addition decreased the isoamyl acetate yields slightly ( approximately 10%) at 0.005-0.01% v/v of the reaction mixture and drastically (>40%) at above 0.01% v/v. Buffer saturation of the organic solvent employed improved esterification (upto two-fold), particularly at moderately higher substrate concentrations (>0.18 M). Employing acetic anhydride instead of acetic acid resulted in a two-fold increase in the yields (at 0.25 M substrate). Use of excess nucleophile (alcohol) concentration by increasing the alcohol/acid molar ratio resulted in higher conversions in shorter duration (upto eight-fold even at 1.5 M acetic acid). Yields above 80% were achieved with substrate concentrations as high as 1.5 M and more than 150 g l(-1) isoamyl acetate concentrations were obtained employing a relatively low enzyme concentration of 10 g l(-1). The operational stability of lipase was also observed to be reasonably high enabling ten reuses of the biocatalyst.     

Biosynthesis and function of trehalose inEctothiorhodospira halochloris

Trehalose-6-phosphate synthase, catalyzing the reaction between UDP-glucose and glucose 6-phosphate and forming trehalose 6-phosphate, was isolated and partially purified (30-fold) from the phototrophic, haloalkaliphilic bacteriumEctothiorhodospira halochloris. The activity is stabilized by 20mM MgCl₂, 50mM NaCe and 2M glycine betaine. The molecular weight was 63000.The enriched enzyme had a MgCl₂ optimum at 3–6mM, a pH optimum at 7.5 (in Tris-HCl buffer) and a temperature optimum at 50°C. The K_m-values were 1.5×10^–3M for UDP-glucose and 2×10^–3M for glucose 6-phosphate. The enzyme showed a salinity dependence with optimal concentrations between 100 and 300mM salt. Higher concentrations of salt resulted in a decrease in activity. In the presence of inhibitory salt concentrations the compatible solute glycine betaine had a protective effect with a maximum between 0.5 and 2.0M.     

Biochemical characterisation of extracellular phytase (myo-inositol hexakisphosphate phosphohydrolase) from a hyper-producing strain of Aspergillus niger van Teighem

Aspergillus niger van Teighem, isolated in our laboratory from samples of rotten wood logs, produced extracellular phytase having a high specific activity of 22,592 units (mg protein)^–1 . The enzyme was purified to near homogeneity using ion-exchange and gel-filtration chromatography. The molecular properties of the purified enzyme suggested the native phytase to be oligomeric, with a molecular weight of 353 kDa, the monomer being 66 kDa. The purified enzyme exhibited maximum activity at pH 2.5 and 52–55°C. The enzyme retained 97% activity after a 24-h incubation at 55°C in the presence of 10 mM glycine, while 87% activity was retained when no thermoprotectant was added. Phytase activity was not affected by most metal ions, inhibitors and organic solvents. Non-ionic and cationic detergents (0.1–5%) stabilise the enzyme, while the anionic detergent (SDS), even at a 0.1% level, severely inhibited enzyme activity. The chaotropic agents guanidinium hydrochloride, urea, and potassium iodide (0.5–8 M), significantly affected phytase activity. The maximum hydrolysis rate (V_max) and apparent Michaelis-Menten constant (K_m) were 1,074 IU/mL and 606 M, respectively, with a catalytic turnover number of 3×10⁵ s^–1 and catalytic efficiency of 3.69×10⁸ M^–1 s^–1.     

Purification and characterization of naringinase from a newly isolated strain of <Emphasis Type="Italic">Aspergillus niger</Emphasis> 1344 for the transformation of flavonoids

Summary An extracellular naringinase (an enzyme complex consisting of α-L-rhamnosidase and β-D-glucosidase activity, EC 3.2.1.40) that hydrolyses naringin (a trihydroxy flavonoid) for the production of rhamnose and glucose was purified from the culture filtrate of Aspergillus niger 1344. The enzyme was purified 38-fold by ammonium sulphate precipitation, ion exchange and gel filtration chromatography with an overall recovery of 19% with a specific activity of 867 units per mg of protein. The molecular mass of the purified enzyme was estimated to be about 168 kDa by gel filtration chromatography on a Sephadex G-200 column and the molecular mass of the subunits was estimated to be 85 kDa by sodium dodecyl sulphate-Polyacrylamide gel electrophoresis (SDS-PAGE). The enzyme had an optimum pH of 4.0 and temperature of 50 °C, respectively. The naringinase was stable at 37 °C for 72 h, whereas at 40 °C the enzyme showed 50% inactivation after 96 h of incubation. Hg²⁺, SDS, p-chloromercuribenzoate, Cu²⁺ and Mn²⁺ completely inhibited the enzyme activity at a concentration of 2.5–10 mM, whereas, Ca²⁺, Co²⁺ and Mg²⁺ showed very little inactivation even at high concentrations (10–100 mM). The enzyme activity was strongly inhibited by rhamnose, the end product of naringin hydrolysis. The enzyme activity was accelerated by Mg²⁺ and remained stable for one year after storage at −20 °C. The purified enzyme preparation successfully hydrolysed naringin and rutin, but not hesperidin.     

Purification and Characterization of S-Adenosyl-L-Methionine Nicotinic Acid-N-Methyltransferase from Leaves of Glycine max

Trigonelline (TRG), which act as a cell cycle regulator and a compatible solute in response to salinity and water-stress, is the N-methyl conjugate of nicotinic acid the formation of which is catalyzed by S-adenosyl-L-methionine nicotinic acid-N-methyltransferase. The enzyme was purified 2650-fold from soybean (Glycine max L.) leaves with a recovery of 4 %. The purification procedure included ammonium sulfate (45 – 60 %) precipitation, linear gradient DEAE-Sepharose chromatography, adenosine-agarose affinity chromatography, hydroxyapatite chromatography and gel filtration (Sephacryl-S-200). The purified enzyme preparation showed a major band with a molecular mass of 41.5 kDa in sodium dodecyl sulfate-polyacrylamide gel electrophoresis that is related to the enzyme activity. The native enzyme had a molecular mass of about 85 kDa as estimated by gel filtration. The K_m values for S-adenosyl-L-methionine and nicotinic acid were 31 and 12.5 M, respectively. The purified enzyme showed optimum activity at pH 6.5 and temperature of 40 – 45 °C. High concentration of dithiothreitol (10 mM) and glycerol (20 %) stabilize the enzyme during purification and storage. Hg²⁺ strongly inhibits enzyme activity.     

Standardized extraction method for paralytic shellfish toxins in phytoplankton

The optimal conditions were established for extraction of paralytic shellfish toxins from a Danish clone of Alexandrium tamarense using extraction with acetic acid and HCl in the concentration range 0.01–1.0 N. Physical destruction of the cells was investigated microscopically to select the most efficient extraction procedure.The toxin content was quantitated by an automized isocratic reversed-phase high-performance liquid chromatography (HPLC) method. The best results as judged from the total amount of toxins and the toxin profile were obtained using 0.05–1.0 N acetic acid and 0.01–0.02 N HCl. Hydrochloric acid in the concentration range 0.03–1.0 N caused the amount of C1 and C2 toxins to decrease sharply and concomitant increase of gonyautoxins 2 and 3.The phytoplankton extracts with 0.1 to 0.5 N acetic acid or 0.01 N HCl were stable during 6 months at –20 °C, but the extracts with HCl 0.02 N underwent a change in toxin profile, although the total amount of toxins was constant.     

Microbiological degradation of the herbicide dicamba

Summary Pseudomonas paucimobilis was isolated from a consortium which was capable of degrading dicamba (3,6-dichloro-2-methoxybenzoic acid) as the sole source of carbon. The degradation of dicamba byP. paucimobilis and the consortium was examined over a range of substrate concentration, temperature, and pH. In the concentration range of 100–2000 mg dicamba L^–1 (0.5–9.0 mM), the degradation was accompanied by a stoichiometric release of 2 mol of Cl^– per mol of dicamba degraded. The cultures had an optimum pH 6.5–7.0 for dicamba degradation. Growth studies at 10°C, 20°C, and 30°C yielded activation energy values in the range of 19–36 kcal mol^–1 and an average Q₁₀ value of 4.0. Compared with the pure cultureP. paucimobilis, the consortium was more active at the lower temperature.     

Effect of incubation temperature on zearalenone production by strains of Fusarium crookwellense

After 6 weeks incubation on rice 2 strains of Fusarium crookwellense produced more zearalenone (6060–5010 mg/kg dry wt of culture) at ambient temperature (16–29°C) in daylight than at ambient temperature (18–23 °C) in darkness or at controlled temperatures of 11 °C, 20 °C or 25 °C in darkness. Yields at 25 °C were low. Incubation at 11 °C during the second 3 weeks incubation increased yields only when preliminary incubation had been at 25 °C. After 6 weeks incubation at controlled temperatures in darkness, 4 strains produced most zearalenone at 20 °C (2460-21 360 mg/kg), 1 strain at 11 °C (6570 mg/kg). Yields at a temperature oscillating daily from 10–20 °C were less than at 15 °C. One of the 5 strains produced appreciable amounts of a-zearalenol (1645 mg/kg at 20°C) and 2 of nivalenol (340 and 499 mg/kg at 20 °C).     

Reduction of Cr(VI) by Desulfovibrio vulgaris and Microbacterium sp.

Many industrial wastes contain Cr(VI), a carcinogen and mutagen, the toxicity of which can be ameliorated by reduction to Cr(III). Microbacterium sp. NCIMB 13776 andDesulfovibrio vulgaris NCIMB 8303 reduced Cr(VI) to Cr(III) anoxically using 25 mM sodium citrate buffer (pH 7), with 25 mM sodium acetate and 25 mM sodium formate as electron donors at 30 °C, under which conditions the rates of reduction of 500 M sodium chromate were 77 and 6 nmol h^–1 mg dry cell wt for D. vulgaris and Microbacterium sp., respectively, these being increased to 127 and 17 nmol h^–1 mg dry cell wt in the presence of 20 mM MOPS/NaOH buffer.     

Purification and characterization of a new type of serine carboxypeptidase from<Emphasis Type="Italic"> Monascus purpureus</Emphasis>

Carboxypeptidase produced by Monascus purpureus IFO 4478 was purified to homogeneity. The purified enzyme is a heterodimer with a molecular mass of 132 kDa and consists of two subunits of 64 and 67 kDa. It is an acidic glycoprotein with an isoelectric point of 3.67 and 17.0% carbohydrate content. The optimum pH and temperature were 4.0 and 40 °C, respectively. The enzyme was stable between pH 2.0 and 8.0 at 37 °C for 1 h, and up to 50 °C at pH 5.0 for 15 min. The enzyme was strongly inhibited by piperastatin A, diisopropylfluoride phosphate (DFP), phenylmethylsulfonylfluoride (PMSF), and chymostatin, suggesting that it is a chymotrypsin-like serine carboxypeptidase. Monascus purpureus carboxypeptidase was also strongly inhibited by p-chloromercuribenzoic acid (PCMB) but not by ethylenediaminetetraacetic acid (EDTA) and 1,10-phenanthroline, indicating that it requires cysteine residue but not metal ions for activity. Benzyloxycarbonyl-l-tyrosyl-l-glutamic acid (Z-Tyr-Glu), among the substrates tested, was the best substrate of the enzyme. The K_m, V_max, K_cat, and K_cat/K_m values of the enzyme for Z-Tyr-Glu at pH 4.0 and 37 °C were 0.86 mM, 0.917 mM min^–1, 291 s^–1, and 339 mM^–1 s^–1, respectively.     

ATP and ADP hydrolysis in fish, chicken and rat synaptosomes

Ecto-enzymes capable of hydrolyzing ATP and ADP (NTPDase) are present in the central nervous system of various species. In the present investigation we studied the synaptosomal NTPDase (ATP diphosphohydrolase, apyrase, E.C. 3.6.1.5) from fish, chicken and rats under different conditions and in the presence of several classical inhibitors. The cation concentration required for maximal activity was 0.5 mM for fish, 1.0 mM for chickens and 1.5 mM for rats with both substrates. The results showed that the pH optimum for all animal preparations was close to 8.0. The temperature used was 25–27°C for fish and 35–37°C for chicken and rat preparations. The inhibitors azide and fluoride only inhibited the preparation at high concentrations (10 mM). Lanthanum (0.1–0.4 mM), N-ethylmaleimide (0.4–3.0 mM) and ouabain (0.5–3.0 mM) had no effect on NTPDase activity from fish, chickens or rats. Orthovanadate (0.1–0.3 mM) only inhibited fish synaptosomal NTPDase. Trifluoperazine (0.05–0.2 mM) and suramin (0.03–0.3 mM) inhibited NTPDase at all concentrations tested. Suramin was the most potent compound in causing inhibition, presenting inhibition at 30 μM. Our results demonstrate that the synaptosomal NTPDase response to several factors is similar in fish, chickens and rats, and that the enzyme presents functional homology.