A novel alkaline lipase from Ralstonia with potential application in biodiesel production

With the aim of isolating a biocatalyst able to catalyze biodiesel production from microbial source, Ralstonia sp. CS274 was isolated and a lipase from the strain (RL74) was purified. Molecular weight of RL74 was estimated to be 28,000 Da by SDS-PAGE. The activity was highest at 50-55 °C and pH 8.0-9.5 and was stable at pH 7.0-12.0 and up to 45 °C. It was resistant to oxidizing and reducing agents and the activity was enhanced by detergents. RL74 was 1,3 specific and K_m and V_max for p-nitrophenyl palmitate were 2.73 ± 0.6 mM and 101.4 ± 1.9 mM/min mg, respectively. N-terminal amino acid sequence showed partial homology with that of Penicillium lipases. RL74 produced biodiesel more efficiently in palm oil than in soybean oil; and the production was highest at pH 8.0, at 5% methanol and at 20% water content.     

Factors screening to statistical experimental design of racemic atenolol kinetic resolution via transesterification reaction in organic solvent using free Pseudomonas fluorescens lipase

As the (R )‐enantiomer of racemic atenolol has no β‐blocking activity and no lack of side effects, switching from the racemate to the (S )‐atenolol is more favorable. Transesterification of racemic atenolol using free enzymes investigated as a resource to resolve the racemate via this method is limited. Screenings of enzyme, medium, and acetyl donor were conducted first to give Pseudomonas fluorescens lipase, tetrahydrofuran, and vinyl acetate. A statistical design of the experiment was then developed using Central Composite Design on some operational factors, which resulted in the conversions of 11.70–61.91% and substrate enantiomeric excess (ee ) of 7.31–100%. The quadratic models are acceptable with R² of 95.13% (conversion) and 89.63% (ee ). The predicted values match the observed values reasonably well. Temperature, agitation speed, and substrate molar ratio factor have low effects on conversion and ee , but enzyme loading affects the responses highly. The interaction of temperature–agitation speed and temperature–substrate molar ratio show significant effects on conversion, while temperature–agitation speed, temperature–substrate molar ratio, and agitation speed–substrate molar ratio affect ee highly. Optimum conditions for the use of Pseudomonas fluorescens lipase, tetrahydrofuran, and vinyl acetate were found at 45°C, 175 rpm, 2000 U, and 1:3.6 substrate molar ratio.     

Immobilized Pseudomonas cepacia lipase for biodiesel fuel production from soybean oil

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

Cloning and expression of a novel lipase gene from Pseudomonas fluorescens B52

Here we describe an advanced polymerase chain reaction (PCR) technique, the compatible ends ligation inverse PCR (CELI-PCR) for chromosome walking. In CELI-PCR, several restriction enzymes, which produce compatible cohesive ends, were used to digest target DNA simultaneously or sequentially to produce DNA fragments of suitable size. DNA fragments were then easily circularized and PCR amplification could be carried out efficiently. The previous limitations of inverse PCR were overcome, such as unavailable restriction sites, poor template DNA circularization, and low amplification efficiency. Therefore, successive chromosome walking was performed successfully. Our work, isolating a 11,395-bp fragment from Gossypium hirsutum, was presented as an example to describe how CELI-PCR was carried out.     

A monolithic lipase reactor for biodiesel production by transesterification of triacylglycerides into fatty acid methyl esters

An enzymatic reactor with lipase immobilized on a monolithic polymer support has been prepared and used to catalyze the transesterification of triacylglycerides into the fatty acid methyl esters commonly used for biodiesel. A design of experiments procedure was used to optimize the monolithic reactor with variables including control of the surface polarity of the monolith via variations in the length of the hydrocarbon chain in alkyl methacrylate monomer, time of grafting of 1-vinyl-4,4-dimethylazlactone used to activate the monolith, and time used for the immobilization of porcine lipase. Optimal conditions involved the use of a poly(stearyl methacrylate-co-ethylene dimethacrylate) monolith, grafted first with vinylazlactone, then treated with lipase for 2 h to carry out the immobilization of the enzyme. Best conditions for the transesterification of glyceryl tributyrate included a temperature of 37°C and a 10 min residence time of the substrate in the bioreactor. The reactor did not lose its activity even after pumping through it a solution of substrate equaling 1,000 reactor volumes. This enzymatic reactor was also used for the transesterification of triacylglycerides from soybean oil to fatty acid methyl esters thus demonstrating the ability of the reactor to produce biodiesel.     

The diversity of lipases from psychrotrophic strains of Pseudomonas : a novel lipase from a highly lipolytic strain of Pseudomonas fluorescens

Strains of Pseudomonas fluorescens and Ps. fragi are the predominant psychrotrophs found in raw milk and may cause spoilage due to the secretion of hydrolytic enzymes such as lipase and protease. The diversity of lipases has been examined in Pseudomonas isolates from raw milk which represent different taxonomic groups (phenons). Significant diversity was found using both DNA hybridization and immunoblotting techniques, which has implications for the development of a diagnostic test. The lipase-encoding gene ( lipA ) was cloned from one strain, C9, of Ps. fluorescens biovar V. In contrast to previously reported lipase sequences from Ps. fluorescens , the gene encodes a lipase of M_r 33 kDa. Alignment of all known Pseudomonas and Burkholderia lipase amino acid sequences indicates the existence of two major groups, one of M_r approximately 30 kDa comprising sequences from Ps. fragi , Ps. aeruginosa , Ps. fluorescens C9 and Burkholderia , and one of approximately 50 kDa comprising Ps. fluorescens lipases. The lipase from C9 does not contain a signal peptide and is presumed to be secreted via a signal peptide-independent pathway. The lipA gene of strain C9 was disrupted by insertional mutagenesis. The mutant retained its lipolytic phenotype, strongly suggesting the presence of a second lipase in this strain.     

Overexpression of a thermostable lipase gene from Pseudomonas fluorescens in Escherichia coli

Summary A thermostable lipase gene from Pseudomonas fluorescens SIK W1 was overexpressed in Escherichia coli BL21 using expression vector pTTY2. The amount of lipase produced by E. coli BL21 with pTTY2 was more than 40% of the total cell proteins when induced with isopropyl--d-thiogalactopyranoside. The lipase was produced as inclusion bodies in the cytoplasm of E. coli. They were solubilized by 8 m urea and refolded into biologically active form. The refolded lipase showed high thermostability; the time required for 90% inactivation of the enzyme (D-value) was 4 h at 95°C and the increment of temperature to reduce heating times by 90% (z _d value) was 76°C.Offprint requests to: J. S. Rhee     

Purification, crystallization and properties of triacylglycerol lipase from Pseudomonas fluorescens.

Triacylglycerol lipase of Pseudomonas fluorescens was purified from the crude enzyme by ammonium sulfate precipitation and chromatographies on Sephadex G-75 and DEAE-cellulose. The crystallization of the lipase was successfully carried out. The purified lipase was demonstrated to be homogenous on disc electrophoresis and its molecular weight was calculated to be 32 000 by gel filtration. The optimum pH for hydrolysis of sesame oil was 7.0. The enzyme was stable up to 40 degrees C under the condition of pH 7.0 for 30 min and had more than 80% of the remaining activity between pH 5.0--11.0 at 37 degrees C for 60 min. The lipase was strongly inhibited by iodine and partially inhibited by FeCl3 and N-bromosuccinimide, and showed the most activity on tricaproyglycerol, among the triacylglycerols used.     

Enzymatic transesterification with the lipase from Pseudomonas fragi 22.39 B in a non-aqueous reaction system

The lipase from Pseudomonas fragi 22.39 B catalyzed the transesterification in ester and alcohol mixtures without any other solvent. Activated esters, such as vinyl and phenyl esters, were excellent acyl donors for the reaction, and the activity was enhanced by increasing the carbon number of the fatty acid fraction of the esters. Primary alcohols were esterified faster than secondary ones in this reaction system, while tertiary alcohols such as alpha-terpineol did not react at all. The lipase exhibited stereoselectivity in the esterification of alcohols such as 2-octanol.     

Optimization of the reaction medium for esterification catalyzed by A lipase from Pseudomonas fluorescens

The performance of a crude extract lipase from Pseudomonas fluorescensin esterification was evaluated in microaqueous, biphasic and surfactant-enriched biphasic systems containing various amounts of water (from almost no water to pure water). The results showed a strong negative influence of the water content on the thermodynamic equilibrium of the reaction in biphasic systems. From a kinetic point of view, the enzyme was more efficient in systems involving a water/organic solvent interface (4 times in the biphasic system, 12 times in the surfactant-enriched biphasic system).     

Integrated production for biodiesel and 1,3-propanediol with lipase-catalyzed transesterification and fermentation

Biodiesel, a renewable alternative to fossil energy, has shown great prospects for global proliferation in the past decade. Lipase catalyzed transesterification for biodiesel production, as a biological process with many advantages has drawn increasing attention. As a by-product, glycerol accounts for about 10% w/w of biodiesel during the process of biodiesel production. As a result, the conversion of glycerol has become a common problem which has to be resolved if considering large amount of biodiesel production. Glycerol can be fermented into 1,3-propanediol, a high value added chemical with a promising future in the polymers, for example, polytrimethylene terephthalate, and also fermentation approaches for 1,3-propanediol production which have drawn more and more attention due to advantages such as relatively low investment, mild reaction conditions and using renewable sources as the starting materials. Based on the latest technology advancements in lipase-mediated transformation for biodiesel production, the aerobic fermentation technology and genetic engineering for 1,3-propanediol production, and the integrated production of 1,3-propanediol from crude glycerol could be a promising way to improve the profit of the whole process during biodiesel production.     

Isolation and characterization of lipase from Pseudomonas fluorescens 533-5b]

The enzyme was isolated from the culture fluid of Pseudomonas fluorescens 533-5b and purified by precipitation with (NH4)SO4 and acetone and by gel filtration through Sephadex G-200. The enzyme was found homogeneous during polyacrylamide gel disc electrophoresis. The effects of metal ions, inhibitors, bile salts, temperature, pH and the substrate specificity of the enzyme were studied. It was shown that the enzyme from Ps. fluorescens 533-5b has a broad specificity. It can use as substrates many vegetable oils (olive, soybean, castor, sunflower, corn, mustard, linseed). In addition, the enzyme is capable to hydrolyze synthetic triglycerides consisting of short-chained saturated fatty acids (butyric and caproic) and solid triglycerides containing saturated fatty acids with long carbon chains (myristic, lauric, stearic). It is assumed that the enzyme is a glycoprotein; its molecular weight (320,000) and the amino acid composition were determined.     

Purification and characterization of an organic solvent-tolerant lipase from Pseudomonas aeruginosa LX1 and its application for biodiesel production

An organic solvent-tolerant lipase from newly isolated Pseudomonas aeruginosa LX1 has been purified by ammonium sulfate precipitation and ion-exchange chromatography leading to 4.3-fold purification and 41.1% recovery. The purified lipase from P. aeruginosa LX1 was homogeneous as determined by SDS-PAGE, and the molecular mass was estimated to be 56 kDa. The optimum pH and temperature for lipase activity were found to be 7.0 and 40 °C, respectively. The lipase was stable in the pH range 4.5–12.0 and at temperatures below 50 °C. Its hydrolytic activity was found to be highest towards p-nitrophenyl palmitate (C16) among the various p-nitrophenol esters investigated. The lipase displayed higher stability in the presence of various organic solvents, such as n-hexadecane, isooctane, n-hexane, DMSO, and DMF, than in the absence of an organic solvent. The immobilized lipase was more stable in the presence of n-hexadecane, tert-butanol, and acetonitrile. The transesterification activity of the lipase from P. aeruginosa LX1 indicated that it is a potential biocatalyst for biodiesel production.     

Lipase-catalyzed transesterification of rapeseed oils for biodiesel production with a novel organic solvent as the reaction medium

tert-Butanol, as a novel reaction medium, has been adopted for lipase-catalyzed transesterification of rapeseed oil for biodiesel production, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. Combined use of Lipozyme TL IM and Novozym 435 was proposed further to catalyze the methanolysis and the highest biodiesel yield of 95% could be achieved under the optimum conditions (tert-butanol/oil volume ratio 1:1; methanol/oil molar ratio 4:1; 3% Lipozyme TL IM and 1% Novozym 435 based on the oil weight; temperature 35 °C; 130 rpm, 12 h). There was no obvious loss in lipase activity even after being repeatedly used for 200 cycles with tert-butanol as the reaction medium. Furthermore, waste oil was also explored for biodiesel production and it has been found that lipase also showed good stability in this novel system.     

A hyper-thermostable, alkaline lipase from Pseudomonas sp. with the property of thermal activation

A hyper-thermostable, alkaline lipase from a newly-isolated, mesophilic Pseudomonas sp. was optimal at pH 11 and at 90 °C. It had a half-life of more than 13 h at 90 °C. It was activated by 30% when heated at 90 °C for 2 h. The enzyme had a greater affinity for mustard oil (K _m=40 mg ml^–1) than for olive oil (K _m=140 mg ml^–1).     

Template-based modeling of a psychrophilic lipase: Conformational changes,novel structural features and its application in predicting the enantioselectivity of lipase catalyzed transesterification of secondary alcohols

In order to fully explore the structure–function relationship of a Proteus lipase (LipK107) that was screened from the soil in our previous study, we have modeled the three-dimensional (3-D) structures of the enzyme in its active and inactive conformations on the basis of crystal structures of Burkholderia glumae and Pseudomonas aeruginosa lipases in the present study. Both homology models suggested that LipK107 possessed a catalytic triad (Ser79–Asp232–H254), an oxyanion hole (Leu13 and Gln80) which was used to stabilize the reaction tetrahedral intermediates, and a lid substructure that controlled the access of the substrate to the active site. The existence of the lid was further verified by carrying out the interfacial activation experiment. The conformational change of LipK107 which was caused by lid opening action was predicted by superimposing the two theoretical models for the first time. Finally, both 3-D structures were used to predict the enantioselectivity of LipK107 when the enzyme was used to catalyze the resolution of racemic 1-phenylethanol. Lid-open model of LipK107 identified the R-enantiomer as the preferred enantiomer, while lid-closed mode showed that the S-enantiomer was more favored. However, only the lid-open conformational model could led to predictions that agreed with the following the experimental result of real biocatalysis reaction of 1-phenylethanol.     

Immobilization of lipase from Pseudomonas fluorescens on glyoxyl-octyl-agarose beads: Improved stability and reusability

The lipase from Pseudomonas fluorescens (PFL) has been immobilized on glyoxyl-octyl agarose and compared to the enzyme immobilized on octyl-agarose. Thus, PFL was immobilized at pH 7 on glyoxyl-octyl support via lipase interfacial activation and later incubated at pH 10.5 for 20 h before reduction to get some enzyme-support covalent bonds. This permitted for 70% of the enzyme molecules to become covalently attached to the support. This biocatalyst was slightly more stable than the octyl-PFL at pH 5, 7 and 9, or in the presence of some organic solvents (stabilization factor no higher than 2). The presence of phosphate anions produced enzyme destabilization, partially prevented by the immobilization on glyoxyl-octyl (stabilization factor became 4). In contrast, the presence of calcium cations promoted a great PFLstabilization, higher in the case of the glyoxyl-octyl preparation (that remained 100% active when the octyl-PFL preparations had lost 20% of the activity). However, it is in the operational stability where the new biocatalyst showed the advantages: in the hydrolysis of 1 M triacetin in 60% 1.4 dioxane, the octyl biocatalyst released >60% of the enzyme in the first cycle, while the covalently attached enzyme retained its full activity after 5 reaction cycles.