Enzymatic production of biodiesel from cotton seed oil using t-butanol as a solvent

The enzymatic production of biodiesel by methanolysis of cottonseed oil was studied using immobilized Candida antarctica lipase as catalyst in t-butanol solvent. Methyl ester production and triacylglycerol disappearance were followed by HPLC chromatography. It was found, using a batch system, that enzyme inhibition caused by undissolved methanol was eliminated by adding t-butanol to the reaction medium, which also gave a noticeable increase of reaction rate and ester yield. The effect of t-butanol, methanol concentration and temperature on this system was determined. A methanolysis yield of 97% was observed after 24h at 50 degrees C with a reaction mixture containing 32.5% t-butanol, 13.5% methanol, 54% oil and 0.017 g enzyme (g oil)(-1). With the same mixture, a 95% ester yield was obtained using a one step fixed bed continuous reactor with a flow rate of 9.6 mlh(-1) (g enzyme)(-1). Experiments with the continuous reactor over 500 h did not show any appreciable decrease in ester yields.     

Continuous production of kyotorphin

The continuous alpha-chymotrypsin-catalyzed peptide synthesis of kyotorphin, tyrosyl-arginine, via the N(alpha) formyltyrosyl-arginine propyl ester is described. For continuous process development, two reaction systems were studied: immobilized alpha-chymotrypsin covalently bound to Eupergit C packed in a column, and soluble alpha-chymotrypsin utilizing an enzyme membrane reactor. Selectivities and kinetic parameters are discussed. The use of soluble enzyme in an enzyme membrane reactor proved superior to the covalently immobilized enzyme. A significant loss of enzyme activity and a certain decrease of selectivity was observed during immobilization. It was shown that the addition of organic solvent, in this case n-propanol, causes a severe diminuation of the enzyme activity.     

Synthesis of acetone glycerol acyl esters by immobilized lipase ofMucor miehei

Summary The applications of immobilized lipase ofMucor miehei for the synthesis of acetone glycerol acyl ester from acetone glycerol and fatty acid, which is the first step for monoglyceride production was investigated. With a high oleic acid to acetone glycerol ratio (O/A, mol/mol), a high catalytic activity was observed under low water content in the reaction mixture. By the combination of high O/A ratio (>3) and removal of water which was produced during the reaction, the conversion degree was increased to almost 100%. With the O/A ratio of 3, the approximate half-life of the immobilized lipase and productivity of ester was estimated to be 20 days and 869 g product/g immobilized enzyme per 2 half-lives, respectively.     

Synthesis of L-tyrosine glyceryl ester catalyzed by α-chymotrypsin in water-miscible organic solvents: A possible sun-tan accelerator product

Summary The synthesis of L-tyrosine glyceryl ester, from glycerol and L-tyrosine methyl ester, was carried out by a transesterification reaction catalyzed by -chymotrypsin. Values of 60 % (v/v) for glycerol and 200 mM for L-tyrosine methyl ester were optimal for the transesterification reaction. Additionally to glycerol, several other water miscible cosolvents (acetonitrile, N,N'-dimetyl formamide and tetrahydrofurane) were tested in the reaction media, but their presence did not give an enhancement on the transesterification activity with respect to the glycerol/water medium. However, increasing the hydrophobicity of the cosolvent resulted in a reduction of the enzyme activity, the water:glycerol mixture being the best reaction media.     

The mechanism of action of ethanolamine ammonia-lyase, an adenosylcobalamin-dependent enzyme. Evidence for a carboxyl group at the active site

Ethanolamine ammonia-lyase is an adenosylcobalamin-dependent enzyme that catalyzes the rearrangement of ethanolamine and other vicinal amino alcohols to oxo-compounds and ammonia. Treatment of this enzyme with the sulfhydryl group-blocking reagent methyl methanethiosulfonate produces a species with diminished catalytic activity. When methyl methanethiosulfonate -treated ethanolamine ammonia-lyase was incubated with a carboxyl-blocking reagent consisting of glycine ethyl ester plus a water-soluble carbodiimide, the enzyme lost more than 80% of its residual activity, while at the same time glycine ethyl ester was incorporated into it at a stoichiometry of 6 mol/mol of enzyme. Both the loss of activity and the incorporation of glycine ethyl ester were prevented if ethanolamine was included in the glycine ethyl ester-containing incubation mixture. These results suggest that an active site carboxyl group plays a role in the mechanism of catalysis by ethanolamine ammonia-lyase, and that this carboxyl group is amidated when the enzyme is incubated with glycine ethyl ester plus carbodiimide.     

The effect of solvent viscosity on the rate-determining step of fatty acid synthetase

The overall activity of an animal fatty acid synthetase at the saturation level of substrate concentration decreased when the solvent viscosity, eta, of the reaction mixture was increased with viscogens such as glycerol, sucrose, and polyethylene glycol. The activity of the enzyme changed roughly proportional to eta-P, where p = 1.0 for glycerol, p = 0.66 for sucrose, and p less than 0.6 for polyethylene glycol with different molecular sizes. The thioesterase activity, which catalyzes the final partial reaction in the multifunctional enzyme, was not affected by 5-fold increase of solvent viscosity with sucrose. These results suggested that the rate-determining step of the enzyme other than the thioesterase reaction involves a microscopic transport step, the rate of which is influenced by the solvent viscosity. The microscopic transport step may be related to the transfer of the reaction intermediate from one active site to another or to the motion of a larger part of the enzyme requisite for the catalytic reaction. In the solution containing glycerol, the rate-determining motion was primarily diffusion limited since the inverse of the initial rate was proportional to eta, i.e., p = 1. Since the substrate concentration was at a saturation level in this experiment, the viscosity-dependent step cannot be the encounter between the enzyme and substrates, but must be intramolecular in origin, most probably the reaction catalyzed by beta-ketoacyl synthetase. In solutions containing other viscogens, however, p was less than 1.0, indicating a significant involvement of chemical steps in the rate-determining step as well. Bovine serum albumin, when used as a proteinic viscogen, also decreased the initial rate.(ABSTRACT TRUNCATED AT 250 WORDS)     

Enantioselective esterification of butanol-2 in an enzyme membrane reactor

The enzymatic esterification of octanoic acid with racemic butanol-2 was investigated. Esterifications of the acid were performed in a forced flow enzyme membrane reactor. The used membrane was prepared by a phase inversion process in polyamide-6 solution followed by the chemical immobilization of a lipase-catalyst. Influences of water content and pH were estimated. Their optimum values are equal to 0.5% w/w and pH 8. The reaction rate (at 303 K) of 5.1 × 10^?5 mol/h·cm² of the membrane area, and at least 85% enantiomeric excess in the produced ester mixture were obtained. The activity of immobilized lipase in the membrane process is about two times higher than that of the native lipase in the esterification performed in a tank reactor.     

Synthetic branched-chain analogues of distearoylphosphatidylcholine: structure-activity relationship in inhibiting and activating protein kinase C

A series of distearoylphosphatidylcholine (DSPC) analogues having various branched alkyl chains were synthesized and tested for their abilities to regulate protein kinase C (PKC). The greatest improvement (about 3-fold) in the PKC inhibitory activity over that seen for the parental lipid (i.e., DSPC) was accomplished by substitution of 8-methylstearate at sn-2 and 16-methylstearate at both sn-1 and sn-2 positions of glycerol; substitutions at both sn-1 and sn-2 with 8-methylstearate, on the other hand, caused a decrease (about 4-fold) in its inhibitory activity. Introduction of butyl, phenyl, or keto functions to various positions in the fatty alkyl chain substituted at both sn-1- and sn-2 positions imparted upon the DSPC analogues an ability to potently stimulate PKC to an extent comparable to those attainable by diacylglycerol or phorbol ester; the analogues having substitution only at the sn-2 position, in comparison, had no or reduced stimulatory activity. The butyl, phenyl, and keto analogues of DSPC, as with DSPC itself and its methyl analogues, inhibited PKC at high concentrations. Kinetic analysis indicated that the methyl DSPC analogues inhibited the enzyme competitively with respect to phosphatidylserine (PS; a phospholipid cofactor) and Ca2+. The butyl analogues activated the enzyme without affecting its affinity for PS or Ca2+, indicating a mechanism different from that seen for diacylglycerol or phorbol ester. The inhibitory activity of the methyl DSPC analogues and the stimulatory activity of the butyl DSPC analogues were reduced when PKC was activated by phorbol ester. Both classes of the analogues were unable to compete for the binding of [3H]phorbol dibutyrate to PKC.(ABSTRACT TRUNCATED AT 250 WORDS)     

Immobilized lipase Candida sp. 99-125 catalyzed methanolysis of glycerol trioleate: solvent effect

The immobilized lipase Candida sp. 99-125 catalyzed methanolysis of glycerol trioleate was studied in twelve different solvents in order to deduce the solvent effect through an attempt to correlate the highest yield with such solvent properties as hydrophobicity (log P), dielectric constant (epsilon), and Hildebrand solubility parameter (delta). The results showed that the conversion of glycerol trioleate and yield of oleic acid methyl ester were quite dependent on the solvent. The catalyst lipase in various solvents also needed different optimum amount of water to keep its maximum activity, and generally this lipase in more hydrophobic solvents required more water. The correlation between the highest yield and log P value was found to be reasonable except deviation of data points of certain solvents, while no obvious correlation existed between the other two parameters, dielectric constant (epsilon) and Hildebrand solubility parameter (delta), and the enzyme activity. The study revealed that more hydrophobic solvents such as n-hexane or cyclohexane were more suitable solvents for Candida sp. 99-125 catalyzed transesterification of glycerol trioleate to oleic acid methyl ester.     

The size and curvature of anionic covesicle substrate affects the catalytic action of cytosolic phospholipase A2.

Cytosolic phospholipase A2 (cPLA2) is normally located in the cytosol, but in response to cellular activation the enzyme binds to the membrane at the lipid/water interface where it catalyzes the hydrolysis of the sn-2 ester of arachidonate-containing phospholipids. Synthetic phospholipid vesicle systems have been used in kinetic and mechanistic analyses of cPLA2, but these systems result in a rapid loss of enzyme activity. In the present research, covesicles of 1,2-dimyristoyl-sn-glycero-3-phosphomethanol (DMPM) containing 相似文献   

Kinetics and mechanism of the cutinase-catalyzed transesterification of oils in AOT reversed micellar system

The kinetics of the enzymatic transesterification between a mixture of triglycerides (oils) and methanol for biodiesel production in a bis(2-ethylhexyl) sodium sulfosuccinate (AOT)/isooctane reversed micellar system, using recombinant cutinase from Fusarium solani pisi as a catalyst, was investigated. In order to describe the results that were obtained, a mechanistic scheme was proposed, based on the literature and on the experimental data. This scheme includes the following reaction steps: the formation of the active enzyme–substrate complex, the addition of an alcohol molecule to the complex followed by the separation of a molecule of the fatty acid alkyl ester and a glycerol moiety, and release of the active enzyme. Enzyme inhibition and deactivation effects due to methanol and glycerol were incorporated in the model. This kinetic model was fitted to the concentration profiles of the fatty acid methyl esters (the components of biodiesel), tri-, di- and monoglycerides, obtained for a 24 h transesterification reaction performed in a stirred batch reactor under different reaction conditions of enzyme and initial substrates concentration.     

Optimizing lipase activity, enantioselectivity, and stability with medium engineering and immobilization for beta-blocker synthesis.

Lipase from Pseudomonas cepacia showed poor activity and moderate enantioselectivity (E) in pure aqueous systems for hydrolysis of a racemic mixture (+/-)-1-chloro-2-acetoxy-3-(1-naphthyloxy)-propane, which is a potential intermediate for beta-blocker synthesis. However, addition of polar organic solvents to the reaction can change both the activity and the enantioselectivity for this chiral reaction significantly. It was observed, in general, that the activity increases and the enantioselectivity decreases with the increase in the polarity of the organic solvent added to the medium. Among the six solvents chosen (i.e., dimethylsulfoxide [DMSO], 1, 4-dioxane, dimethylformamide [DMF], acetone, 1-propanol, and tetrahydrofuran [THF]), maximum activity and minimum enantioselectivity was obtained with DMSO, whereas minimum activity and maximum enantioselectivity was obtained with THF as the cosolvents. In the subsequent studies, native or polyethylene glycol (PEG)-modified lipase was immobilized by entrapping in Caalginate gel beads. In a fixed-bed continuous reactor containing these catalyst beads, the enzyme was found to be at least three times more enantioselective than the native form in a batch reactor. This fixed-bed reactor with the beads could be operated with high concentration of acetone (33% v/v) for about 1 month without a significant loss of enzyme activity and enantioselectivity.     

The partial purification and properties of a phytoene synthesizing enzyme system.

An enzyme system catalyzing the synthesis of phytoene from isopentenyl pyrophosphate has been isolated from tomato fruit plastids and purified approximately 350-fold in specific activity. This enzyme system has a molecular weight of approximately 200,000. The rate of phytoene formation is maximal at pH 7.0 and 23 °C and the apparent K_m for isopentenyl pyrophosphate is 10 μm The rates of phytoene synthesis when geranylgeranyl pyrophosphate and isopentenyl pyrophosphate were used as substrates were 0.08 and 0.17 nmol of phytoene/mg of protein/h, respectively. The enzyme complex showed an absolute requirement for Mn²⁺, but not for NADP⁺. At a concentration of 2 mm, NADP⁺ produced only a 1.5- to 3-fold stimulation, and this effect varied from preparation to preparation. The addition of NADPH to the incubation mixture produced inhibition of phytoene synthesis and there was no evidence for the concomitant accumulation of lycopersene. The acid labiles produced on acid treatment of the incubation mixture indicated that geranylgeranyl pyrophosphate was formed by the enzyme complex. The enzyme system is stabilized in the presence of 30% glycerol and 10 mm dithiothreitol and it can be stored at ?20 °C for over 1 month without significant loss of activity. However, the enzyme activity for phytoene formation is heat labile, and it is not stable when attempts are made to purify it further by ion-exchange chromatography.     

Conversion of Soybean Oil to Biodiesel Fuel Using Lipozyme TL IM in a Solvent-free Medium

The conversion of soybean oil to biodiesel fuel was investigated in the presence of a lipase from Thermomyces lanuginosus (commercially called Lipozyme TL IM) in a solvent-free medium. The lipase was inactivated when more than 1.5 molar equivalent of methanol was added to the oil mixture. To fully convert the oil to its corresponding methyl esters, the reaction was performed successfully by a three-step addition of 1 molar equivalent of methanol and under the optimized conditions (40°C, 150 rpm, 10% enzyme quantity based on oil weight), the maximum methyl ester (ME) yield was 98% after 12 h reaction. By-product glycerol had a negative effect on enzymatic activity and iso-propanol was found to be effective for glycerol removal, in the presence of which lipase expressed relatively high activity and more than 94% of the ME yield was maintained after being used repeatedly for 15 batches.     

Process engineering and optimization of glycerol separation in a packed-bed reactor for enzymatic biodiesel production

A process model for efficient glycerol separation during methanolysis in an enzymatic packed-bed reactor (PBR) was developed. A theoretical glycerol removal efficiency from the reaction mixture containing over 30% methyl esters was achieved at a high flow rate of 540 ml/h. To facilitate a stable operation of the PBR system, a batch reaction prior to continuous methanolysis was conducted using oils with different acid values and immobilized lipases pretreated with methyl esters. The reaction system successfully attained the methyl ester content of over 30% along with reduced viscosity and water content. Furthermore, to obtain a high methyl ester content above 96% continuously, long-term lipase stability was confirmed by operating a bench-scale PBR system for 550 h, in which the intermediates containing methyl esters and residual glycerides were fed into the enzyme-packed columns connected in series. Therefore, the developed process model is considered useful for industrial biodiesel production.     

The Influence of Fatty Acid and Glycerol on the Kinetics of Fat Hydrolysis by Candida Rugosa Lipase in a Membrane Reactor

The kinetics of lipid-hydrolysis by Candida rugosa lipase was investigated in a membrane reactor and in an emulsion system. Two models were chosen to describe the kinetics of the enzyme:

(1) The hydrolysis of triglycerides to fatty acids was considered to be a chain reaction with the intermediary products di- and mono-glyceride; each step was assumed to be a reversible second-order reaction. The reaction rate constants were determined from batch experiments. The experimental results could be described with this model.

(2) For process optimization and control, a model based on the power law was developed. For this model, the rate of hydrolysis was measured as a function of fatty acid and glycerol concentrations. Relations for the initial rate and equilibrium ester fraction as a function of the glycerol concentration were determined. Further, the reaction rate could be described with the power-law model with a power of 1.75 in the hydrolyzable ester fraction for a wide range of glycerol concentrations. The model with power 1.75 gave much better results when compared to a similar first order model. Although simpler, the first order model can not be used. The power law model was applied in the simulation of a reactor composed of three modules. The fatty acid production rate was calculated for this reactor system as a function of the outgoing glycerol concentration at different conditions.     

Esterification of ferulic acid with polyols using a ferulic acid esterase from Aspergillus niger

Commercially available enzyme preparations were screened for enzymes that have a high ability to catalyze direct ester-synthesis of ferulic acid with glycerol. Only a preparation, Pectinase PL "Amano" produced by Aspergillus niger, feruloylated glycerol under the experimental conditions. The enzyme responsible for the esterification was purified and characterized. This enzyme, called FAE-PL, was found to be quite similar to an A. niger ferulic acid esterase (FAE-III) in terms of molecular mass, pH and temperature optima, substrate specificity on synthetic substrates, and the N-terminal amino acid sequence. FAE-PL highly catalyzed direct esterification of ferulic acid and sinapinic acid with glycerol. FAE-PL could feruloylate monomeric sugars including arabinose, fructose, galactose, glucose, and xylose. We determined the suitable conditions for direct esterification of ferulic acid with glycerol to be as follows: 1% ferulic acid in the presence of 85% glycerol and 5% dimethyl sulfoxide at pH 4.0 and 50 degrees C. Under these conditions, 81% of ferulic acid could be converted to 1-glyceryl ferulate, which was identified by (1)H-NMR. The ability of 1-glyceryl ferulate to scavenge 1,1-diphenyl-2-picrylhydrazyl (DPPH) radicals was higher than that of the anti-oxidant butyl hydroxytoluene.     

Production of lipolyzed butteroil by a calf pregastric esterase immobilized in a hollow fiber reactor: III. Effect of glycerol

Lipolysis of butter oil in a hollow fiber reactor containing an immobilized calf pregastric esterase was studied at 40 degrees C, a pH of 6.0, and glycerol concentrations of 0, 150, and 500 g/L in the buffer solution. The concentrations of 10 fatty acid species in the lipolyzed product were determined using high-performance liquid chromatography. The rate of loss of enzyme activity and the relative selectivities of this esterase depended on the glycerol concentration. By contrast, the overall rate of release of fatty acids was not affected by the glycerol concentration. Loss of enzyme activity was modeled using first-order kinetics. The models for deactivation and reaction kinetics were fit simultaneously to the data. The model was successful in describing the rates of release of all 10 fatty acid species for a range of space times from 0 to 25 h. The parameters of the model were tested for dependence on glycerol concentration.     

Lipase-Catalyzed Resolution of Isopropylidene Glycerol: Effect of Co-Solvents on Enantioselectivity

The resolution of 1,2-O-isopropylidene glycerol via enzyme catalyzed hydrolysis of the corresponding benzoic ester was investigated. Using lipase PS from Pseudomonas cepacia, we determined the influence of organic co-solvents on the activity and enantioselectivity of the enzyme. The performance of the lipase was correlated to the nature (logP, ε,μ and the percentage of the organic media. The highest enzymatic activity was found in solvents completely miscible or completely immiscible in water. The enzyme stereoselectivity was inversely related to the logP of the solvent.     

Lipase-Catalyzed Resolution of Isopropylidene Glycerol: Effect of Co-Solvents on Enantioselectivity

The resolution of 1,2-O-isopropylidene glycerol via enzyme catalyzed hydrolysis of the corresponding benzoic ester was investigated. Using lipase PS from Pseudomonas cepacia, we determined the influence of organic co-solvents on the activity and enantioselectivity of the enzyme. The performance of the lipase was correlated to the nature (logP, ?,μ and the percentage of the organic media. The highest enzymatic activity was found in solvents completely miscible or completely immiscible in water. The enzyme stereoselectivity was inversely related to the logP of the solvent.