Lipases are soluble and active in glycerol carbonate as a novel biosolvent

Glycerol carbonate was synthesized as biosolvent for the development of soluble enzymatic system. The effects of various reaction parameters on activity and stability of lipases were investigated using the transesterification of ethyl butyrate with n-butanol as a model reaction. Enzymatic activity in glycerol carbonate was compared with that in water and in conventional organic solvents with different ionizing and dissociating abilities. The pK_a value of trichloroacetic acid and transesterification activities of Candida antarctica lipase B and Candida rugosa lipase in glycerol carbonate are similar to those in water, indicating that ionizing and dissociating powers are capable of satisfactorily predicting the biocompatibility of organic solvents for soluble enzymatic systems.     

Extractive Synthesis of Ethyl‐Oleate Using Alginate Gel Co‐Entrapped Yeast Cells and Lipase Enzyme

To synthesize ethyl‐oleate ester, a complex Ca‐alginate gel co‐entrapped system was prepared. The gel beads contained two kinds of biocatalysts (living yeast cells and a lipase enzyme) and various amounts of glucose (100–400 g/L). These alginate beads dispersed directly in pure oleic acid. To follow the bioconversion of the cell growth, the glucose uptake of yeast cells, the concentration of ethanol inside the gel beads and the ethyl‐oleate concentration in oleic acid phase was monitored. The glucose was quantitatively taken up by yeast cells during 24–72 h, depending on the concentration of glucose. After this 24–72‐hour period, the glucose uptake was stopped. In accordance with changes in glucose concentration, the concentration of ethanol and ethyl‐oleate increased rapidly during the first day of fermentation and thereafter slowed down. It is supposed that the inhibitory effect of produced ethanol would be resolved by co‐immobilization of lipase in the same gel particles. Using lipase, one is able to transform ethanol to ethyl‐oleate, which is soluble in oleic acid. According to the data obtained a minimum of 4 U/mL lipase is required to increase ethyl‐oleate production significantly. Summing up it can be concluded that by means of this system a maximum yield of ethanol and ethyl‐oleate was achieved when gel beads containing 100 g/L glucose and 4 U/mL lipase enzyme were used.     

Multi‐steps green process for synthesis of six‐membered functional cyclic carbonate from trimethylolpropane by lipase catalyzed methacrylation and carbonation,and thermal cyclization

A highly functionalized six‐membered cyclic carbonate, methacrylated trimethylolpropane (TMP) cyclic carbonate, which can be used as a potential monomer for bisphenol‐free polycarbonates and isocyanate‐free polyurethanes, was synthesized by two steps transesterifications catalyzed by immobilized Candida antarctica lipase B, Novozym^®435 (N435) followed by thermal cyclization. TMP was functionalized as 70 to 80% selectivity of mono‐methacrylate with 70% conversion was achieved, and the reaction rate was evaluated using various acyl donors such as methacrylic acid, methacrylate‐methyl ester, ‐ethyl ester, and ‐vinyl ester. As a new observation, the fastest rate obtained was for the transesterfication reaction using methacrylate methyl ester. Byproducts resulted from leaving groups were adsorbed on the molecular sieves (4Å) to minimize the effect of leaving group on the equilibrium. The difference of reaction rate was explained by molecular dynamic simulations on interactions between carbonyl oxygen and amino acid residues (Thr 40 and Glu 157) in the active site of lipase. Our docking studies revealed that as acyl donor, methyl ester was preferred for the initial conformation of the first tetrahederal intermediate with hydrogen bonding interactions. TMP‐monomethacrylate (TMP‐mMA) cyclic carbonate was obtained in 63% yield (74.1% calculated in 85% conversion) from the lipase‐catalyzed carbonation reaction of TMP‐mMA with dimethylcarbonate, and followed by thermal cyclization of the monocarbonate at 90°C. From the multiple reactions demonstrated in gram scale, TMP‐mMA cyclic carbonate was obtained as a green process without using chlorinated solvent and reagent. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:83–88, 2016     

Lipase catalyzed transesterification of soybean oil using ethyl acetate,an alternative acyl acceptor

Methanol, the acyl acceptor usually used in the commercial process of biodiesel production, is associated with some problems such as immiscibility with oils and lipase deactivation. To overcome these barriers, ethyl acetate was proposed as an alternative acyl acceptor for the production of biodiesel from soybean oil using an immobilized lipase, Novozym 435, Ethyl acetate mixed well with soybean oil, and only slightly inhibited the lipase activity by 5%. The effects of various environmental parameters, such as the composition of soybean oil and ethyl acetate, lipase content, and reaction temperature, were investigated to determine the optimal conditions for biodiesel production. As a result, the highest biodiesel production yield, 63.3 (±0.6)%, was obtained by using an ethyl acetate and soybean oil mixture with a 6∶1 molar ratio, with 8% of the immobilized lipase based on the weight of oil added at 70°C and 600 rpm.     

Overexpression of Serratia marcescens lipase in Escherichia coli for efficient bioresolution of racemic ketoprofen

Lipase from Serratia marcescens ECU1010 was cloned and overexpressed in E. coli. After optimization, the maximum lipase activities reached 5000–6000 U/l and this recombinant lipase could enantioselectively hydrolyze (S)-ketoprofen esters into (S)-ketoprofen. Among six alkyl esters of racemic ketoprofen investigated, this lipase showed the best enantioselectivity for the kinetic resolution of ketoprofen ethyl ester, with an ee_p (enantiomeric excess of product) of 91.6% and E-value of 63 obtained at 48.2% conversion. Twelve nonionic surfactants were tested for enhancing the enantioselectivity of this lipase in the bioresolution of ketoprofen ethyl ester. A very high E-value of 1084 was achieved, with an optical purity of >99% ee_p and a yield of 42.6% in the presence of 3% Brij 92V. Further studies showed that the selectivity of the lipase was improved with the increase of Brij 92V concentration. The substrate (ketoprofen ethyl ester) does not inhibit the lipase activity, while the product (S)-ketoprofen inhibits the lipase activity to some extent. These results indicate that the S. marcescens lipase is very useful for biocatalytic production of chiral profens such as (S)-ketoprofen.     

Biosynthesis of glycerol carbonate from glycerol by lipase in dimethyl carbonate as the solvent

Glycerol carbonate was synthesized from renewable glycerol and dimethyl carbonate using lipase in solvent-free reaction system in which excess dimethyl carbonate played as the reaction medium. A variety of lipases have been tested for their abilities to catalyze transesterification reaction, and Candida antartica lipase B and Novozyme 435 exhibited higher catalytic activities. The silica-coated glycerol with a 1:1 ratio was supplied to prevent two-phase formation between hydrophobic dimethyl carbonate and hydrophilic glycerol. Glycerol carbonate was successfully synthesized with more than 90% conversion from dimethyl carbonate and glycerol with a molar ratio of 10 using Novozyme 435-catalyzed transesterification at 70 °C. The Novozyme 435 [5% (w/w) and 20% (w/w)] and silica gel were more than four times recycled with good stability in a repeated batch operation for the solvent-free synthesis of glycerol carbonate.     

Enzymatic coproduction of biodiesel and glycerol carbonate from soybean oil and dimethyl carbonate

The enzymatic coproduction of biodiesel and glycerol carbonate by the transesterification of soybean oil was studied using lipase as catalyst in organic solvent. To produce biodiesel and glycerol carbonate simultaneously, experiments were designed sequentially. Enzyme screening, the molar ratio of dimethyl carbonate (DMC) to soybean oil, reaction temperature and solvent effects were investigated. The results of enzyme screening, at 100 g/L Novozym 435 (immobilized Candida antarctica lipase B), biodiesel and glycerol carbonate showed conversions of 58.7% and 50.7%, respectively. The optimal conditions were 60 °C, 100 g/L Novozym 435, 6.0:1 molar ratio with tert-butanol as solvent: 84.9% biodiesel and 92.0% glycerol carbonate production was achieved.     

Enzymatic synthesis of trieicosapentaenoylglycerol in a solvent-free medium

The enzymatic synthesis of trieicosapentaenoylglycerol from glycerol and eicosapentaenoic ethyl ester in a solvent-free medium is studied here. Novozym SP 435 (immobilized lipase from Candida antarctica) has appeared as a very efficient biocatalyst for this transesterification. A nitrogen bubbling has allowed a good mixing and also the shifting of the reaction toward synthesis by eliminating the ethanol formed. The effect of temperature and of the quantity of lipase has been studied. In the optimal conditions (T=80°C, 5% (w/w) of lipase, 1 mol glycerol for 3 mol ethyl ester), pure triglyceride has been obtained after 10 h.     

Lipase-mediated conversion of vegetable oils into biodiesel using ethyl acetate as acyl acceptor

Ethyl acetate was explored as an acyl acceptor for immobilized lipase-catalyzed preparation of biodiesel from the crude oils of Jatropha curcas (jatropha), Pongamia pinnata (karanj) and Helianthus annuus (sunflower). The optimum reaction conditions for interesterification of the oils with ethyl acetate were 10% of Novozym-435 (immobilized Candida antarctica lipase B) based on oil weight, ethyl acetate to oil molar ratio of 11:1 and the reaction period of 12h at 50 degrees C. The maximum yield of ethyl esters was 91.3%, 90% and 92.7% with crude jatropha, karanj and sunflower oils, respectively under the above optimum conditions. Reusability of the lipase over repeated cycles in interesterification and ethanolysis was also investigated under standard reaction conditions. The relative activity of lipase could be well maintained over twelve repeated cycles with ethyl acetate while it reached to zero by 6th cycle when ethanol was used as an acyl acceptor.     

Novel lipase-catalyzed ring-opening copolymerization of lactide and trimethylene carbonate forming poly(ester carbonate)s.

Poly(lactide-co-trimethylene carbonate)s were prepared by the lipase-catalyzed ring-opening copolymerization of lactide and trimethylene carbonate having carbonate content from 0 to 100%. Their thermal properties and enzymatic degradability were measured. The L,L-, D,D- and D,L-lactides were copolymerized with trimethylene carbonate by porcine pancreatic lipase to produce random copolymers having molecular weights of up to 21000. The glass transition temperature (Tg of the copolymer was dependent on the carbonate content and the Tg values linearly decreased from 35 degrees C (polylactide) to -8 degrees C [poly(trimethylene carbonate)]. Among the lipases tested, the porcine pancreatic lipase and proteinase K showed biodegradability towards poly(ester-carbonate)s.     

Enhancement of ethyl propionate synthesis by poly (AAc-co-HPMA-cl-MBAm)-immobilized Pseudomonas aeruginosa MTCC-4713, exposed to Hg2+ and NH4+ ions

A purified alkaline thermo-tolerant bacterial lipase from Pseudomonas aeruginosa MTCC-4713 was immobilized on a poly (AAc-co-HPMA-cl-MBAm) hydrogel. The hydrogel-bound lipase achieved 93.6% esterification of ethanol and propionic acid (300 mM: 100 mM) into ethyl propionate at temperature 65 degrees C in 3 h in the presence of a molecular sieve (3 angstroms). In contrast, hydrogel-immobilized lipase pre-exposed to 5 mM of HgCl2 orNH4Cl resulted in approximately 97% conversion of reactants in 3 h into ethyl propionate under identical conditions. The salt-exposed hydrogel was relatively more efficient in repetitive esterification than the hydrogel-bound lipase not exposed to any of the cations. Moreover, bound lipase exposed Hg2+ or NH4+ ions showed altered specificity towards p-nitrophenyl esters and was more hydrolytic towards higher C-chain p-nitrophenyl esters (p-nitrophenyl laurate and p-nitrophenyl palmitate with C 12 and C 16 chain) than the immobilized lipase not exposed to any of the salts. The later showed greater specificity towards p-nitrophenyl caprylate (C 8).     

Synthesis of ethyl ferulate in organic medium using celite-immobilized lipase

In the present work we have evaluated synthesis of ethyl ferulate by the esterification reaction of ferulic acid and ethanol catalyzed by a commercial lipase (Steapsin) immobilized onto celite-545 in a short period of 6 h in DMSO. The immobilized lipase was treated with cross-linking agent glutaraldehyde (1%; v/v). The optimum synthesis of ethyl ferulate was recorded at 45 °C, pH 8.5 and 1:1 ratio of ethanol and ferulic acid. Co²⁺, Ba²⁺and Pb²⁺ ions enhanced the synthesis of ethyl ferulate Hg²⁺, Cd³⁺and NH⁴⁺ ions had mild inhibitory effect. The celite-bound lipase produced 68 mM of ethyl ferulate under optimized reaction conditions.     

固定化脂肪酶合成维生素A棕榈酸酯

研究了有机溶剂中脂肪酶催化维生素A棕榈酸酯的合成工艺。采用维生素A醋酸酯和棕榈酸乙酯作为反应底物, 对催化合成维生素A棕榈酸酯反应介质进行了比较, 同时对影响合成维生素A棕榈酸酯反应的因素(温度、初始水含量、底物摩尔比、反应时间和酶量等)进行了探讨, 优化了反应条件: 在10 mL的石油醚中, 体系初始含水量0.2%(体积比V/V), 0.100 g 维生素A醋酸酯和0.433 g 棕榈酸乙酯在酶量为1.1 g的固定化酶催化下, 在30°C、190 r/min下反应12 h, 转化率可以达到83%, 固定化酶可连续使用5次以上。     

固定化脂肪酶合成维生素A棕榈酸酯

研究了有机溶剂中脂肪酶催化维生素A棕榈酸酯的合成工艺。采用维生素A醋酸酯和棕榈酸乙酯作为反应底物, 对催化合成维生素A棕榈酸酯反应介质进行了比较, 同时对影响合成维生素A棕榈酸酯反应的因素(温度、初始水含量、底物摩尔比、反应时间和酶量等)进行了探讨, 优化了反应条件: 在10 mL的石油醚中, 体系初始含水量0.2%(体积比V/V), 0.100 g 维生素A醋酸酯和0.433 g 棕榈酸乙酯在酶量为1.1 g的固定化酶催化下, 在30°C、190 r/min下反应12 h, 转化率可以达到83%, 固定化酶可连续使用5次以上。     

Gas phase ethyl acetate production in a batch bioreactor

Gas phase ethyl acetate production was studied using a porcine pancreatic lipase powder. It was observed that gaseous ethyl acetate was produced from gaseous ethanol and acetic acid. Accordingly, the effects of amount of lipase powder, gaseous ethanol and acetic acid concentrations, and reaction temperature on the performance of a batch bioreactor were investigated. Apparent Michaelis-Menten constant of ethanol was 0.163 [μM] and there was no inhibition by ethanol over the range investigated. As acetic acid concentration increased, ethyl acetate production increased to a maximum, then decreased, thus suggesting the inhibition effects by acetic acid. Over the reaction temperature of 25–55?°C, activation energy was calculated as 3.93 kcal/gmol and initial reaction rate was obtained as follows: r?=?75.7 exp(?1975.7/T) [μM/mg of lipase/hr]     

Highly sensitive active-site titration of lipase in microscale culture media using fluorescent organophosphorus ester

The fluorescent organophosphorus esters, diethyl 4-methylumbelliferyl phosphate (1), ethyl hexyl 4-methylumbelliferyl phosphate (2) and ethyl 4-methylumbelliferyl heptylphosphonate (3) have been synthesized and evaluated as a sensitive active-site titrant of lipase. The phosphorus esters 1, 2 and 3 inactivated the lipase from Pseudomonas aeruginosa (LPL-312) with a second-order rate constant for enzyme inactivation (k(on)) of 1.8, 32 and 5600 s(-1) M(-1), respectively. The long-chain phosphonate 3 turned out to be the most potent inactivator of the lipase to release a stoichiometric amount of highly fluorescent 4-methylumbelliferone (4MU) as a leaving group. By using the phosphate 3 as an active-site titrant, the low concentration (4.5 nM) of the active lipase was titrated successfully. The highly sensitive active-site titration with 3 enabled the direct determination of the concentration of the active lipase expressed in a microscale culture medium. Although the expression level differed significantly from one culture to another, the titrated concentration of the active lipase was proportional to the apparent activity for all the independent cultures. The molecular activity calculated for the expressed lipase was found to be the same as that of the purified lipase. The present active-site titration method is widely applicable to the biocatalytic engineering of lipases such as directed evolution, site-directed mutagenesis, chemical modification and immobilization.     

Pancreatic cholesterol esterases. 2. Purification and characterization of human pancreatic fatty acid ethyl ester synthase

Human pancreatic fatty acid ethyl ester synthase has been isolated and purified 1200-fold to homogeneity, and its activities, binding properties, and N-terminal amino acid sequence indicate that it is a member of the lipase family. This 52-kDa monomeric protein is present at 0.6-1.2 mg/g of pancreas, and it catalyzes the synthesis and hydrolysis of ethyl oleate at rates of 2400 nmol mg-1 h-1 and 30 nmol mg-1 h-1, respectively. Kinetic analyses reveal a pronounced substrate specificity for unsaturated octadecanoic fatty acids, with ethyl ester synthetic rates of 2400 nmol mg-1 h-1 (linoleic), 2400 nmol mg-1 h-1 (oleic), 400 nmol mg-1 h-1 (arachidonic), 300 nmol mg-1 h-1 (palmitic), and 100 nmol mg-1 h-1 (stearic). Like cholesterol esterase, the enzyme binds to immobilized heparin, and this property was critical for its purification to homogeneity. Its N-terminal amino acid sequence is virtually identical with that reported for human triglyceride lipase, NH2-X-Glu-Val-Cys-5Tyr-Glu-Arg-Leu-Gly-10Cys-Phe-Ser-Asp- Asp-15Ser-Pro-Trp-Ser-Gly-20Ile, and it differs by only four residues from that reported for porcine pancreatic lipase. The synthase purified here also cleaves triglycerides, hydrolyzing triolein at a rate of 30 nmol mg-1 h-1, and this activity is stimulated by colipase and inhibited by sodium chloride. Conversely, commercially available porcine triglyceride lipase exhibits fatty acid ethyl ester synthase activity (1530 nmol mg-1 h-1) and hydrolyzes triolein at a rate of 23 nmol mg-1 h-1.(ABSTRACT TRUNCATED AT 250 WORDS)     

Production of diacylglycerols from glycerol monooleate and ethyl oleate through free and immobilized lipase-catalyzed consecutive reactions

The ability of free and immobilized lipase on the production of diacylglycerols (DAG) by transesterification of glycerol monooleate (GMO) and ethyl oleate was investigated. Among three free lipases such as lipase G (Penicillium cyclopium), lipase AK (Pseudomonas fluorescens) and lipase PS (Pseudomonas cepacia), lipase PS exhibited the highest DAG productivity, and the DAG content gradually increased up to 24 hours reaction and then remained steady. The comparative result for DAG productivity between free lipase PS and immobilized lipases (lipase PS-D and Lipozyme RM IM) during nine times of 24 hours reaction indicated that total DAG production was higher in immobilized lipase PS-D (183.5mM) and Lipozyme RM IM (309.5mM) than free lipase PS (122.0mM) at the first reaction, and that the DAG production rate was reduced by consecutive reactions, in which more sn-1,3-DAG was synthesized than sn-1,2-DAG. During the consecutive reactions, the activity of lipase PS was relatively steady by showing similar DAG content, whereas DAG production of lipase PS-D and Lipozyme RM IM was gradually decreased to 69.9 and 167.1mM at 9th reaction, respectively, resulting in 62% and 46% reduced production when compared with 1st reaction. Interestingly, from 7th reaction lipase PS produced more DAG than immobilized lipase PS-D, and exhibited a stable activity for DAG production. Therefore, the present study suggested that DAG productivity between GMO and ethyl oleate was higher in immobilized lipases than free lipases, but the activity was reduced with repeated uses.     

Enzymatic synthesis of fatty acid ethyl esters by utilizing camellia oil soapstocks and diethyl carbonate

This study was reported on a novel process for fatty acid ethyl esters preparation by transesterification and esterification from renewable low-cost feedstock camellia oil soapstocks and friendly acyl acceptor diethyl carbonate. The main components of product were 83.9% ethyl oleate, 8.9% ethyl palmitate, 4.7% ethyl linoleate and 2.1% ethyl stearate, which could be used as eco-friendly renewable resources or additives of industrial solvent and fossil fuel. The effects of molar ratio of diethyl carbonate to soapstocks oil, lipases, organic solvent, reaction temperature and time were investigated, and process conditions were optimized. The yield was up to 98.4% in solvent-free system with molar ratio of diethyl carbonate to soapstocks oil 3:1 and 5% Novozym 435 (based on the weight of soapstocks oil) at 50 °C and 180 rpm for 24 h. Moreover, there was no obvious loss in the yield after lipases were reused for 10 batches without treatment under optimized conditions.     

Effect of Solvents and Kinetic Parameters on Synthesis of Ethyl Propionate Catalysed by Poly (AAc-co-HPMA-cl-MBAm)-Matrix-Immobilized Lipase of Pseudomonas aeruginosa BTS-2.

Summary A purified alkaline thermo-tolerant bacterial lipase from Pseudomonas aeruginosa BTS-2 was immobilized on a poly (AAc-co-HPMA-cl-MBAm) hydrogel network. The hydrogel showed approximately 95% binding efficiency for lipase (specific activity 1.96 U mg⁻¹). The immobilized enzyme achieved 65.1% conversion of ethanol and propionic acid (100 mM each) into ethyl propionate in n-nonane at 65 °C in 9 h. When alkane of C-chain length lower than n-nonane was used as the organic solvent, the conversion of ethanol and propionic acid into ethyl propionate decreased with a decrease in the log P value of alkanes. The immobilized lipase retained approximately 30% of its original catalytic activity after five cycles of reuse for esterification of ethanol and propionic acid into ethyl propionate at temperature 65 °C in 3 h. Addition of a molecular sieve (3 ?) to the reaction mixture enhanced the formation of ethyl propionate to 89.3%. Moreover, ethanol and propionic acid when taken a molar ratio of 3:1 further promoted the conversion rate to 94%. However, an increase in the molar ratio of propionic acid with respect to ethanol resulted in a decline of ethyl propionate synthesis.