Evaluation of immobilized lipases on poly-hydroxybutyrate beads to catalyze biodiesel synthesis

Five microbial lipase preparations from several sources were immobilized by hydrophobic adsorption on small or large poly-hydroxybutyrate (PHB) beads and the effect of the support particle size on the biocatalyst activity was assessed in the hydrolysis of olive oil, esterification of butyric acid with butanol and transesterification of babassu oil (Orbignya sp.) with ethanol. The catalytic activity of the immobilized lipases in both olive oil hydrolysis and biodiesel synthesis was influenced by the particle size of PHB and lipase source. In the esterification reaction such influence was not observed. Geobacillus thermocatenulatus lipase (BTL2) was considered to be inadequate to catalyze biodiesel synthesis, but displayed high esterification activity. Butyl butyrate synthesis catalyzed by BTL2 immobilized on small PHB beads gave the highest yield (≈90 mmol L(-1)). In biodiesel synthesis, the catalytic activity of the immobilized lipases was significantly increased in comparison to the free lipases. Full conversion of babassu oil into ethyl esters was achieved at 72 h in the presence of Pseudozyma antarctica type B (CALB), Thermomyces lanuginosus lipase (Lipex(?) 100 L) immobilized on either small or large PHB beads and Pseudomonas fluorescens (PFL) immobilized on large PHB beads. The latter preparation presented the highest productivity (40.9 mg of ethyl esters mg(-1) immobilized protein h(-1)).     

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.     

Geranyl acetate synthesis catalyzed by Thermomyces lanuginosus lipase immobilized on electrospun polyacrylonitrile nanofiber membrane

Isolated Thermomyces lanuginosus lipase (TLL) was immobilized by different protocols on the polyacrylonitrile nanofibers membrane. The conditions for immobilization of TLL were optimized by investigating effect of protein concentration, time and temperature on the extent of immobilization. The effect of immobilization on the catalytic activity and stability of lipase was studied thoroughly. The immobilized TLL was used as biocatalyst for geranyl acetate synthesis with geraniol and vinyl acetate as substrates and their performance was compared with free enzyme. The TLL immobilized by physical adsorption shows higher transesterification and hydrolytic activities than that of covalently linked or native TLL. There was 32 and 9 fold increase in transesterification activity of TLL immobilized by adsorption and covalent bonding, while hydrolytic activity increases only by 3.6 and 1.8 fold respectively. The optimum conditions for immobilization in both the cases were immobilization time 90–150 min, temperature 45 °C and protein concentration of 2 mg/ml. The percentage conversion of ester was more than 90% and 66% in case of physically adsorbed and covalently bonded enzyme respectively as compared to native one. However, covalently immobilized TLL shows higher operational stability than native and physically adsorbed TLL.     

Enzymatic transesterification in a solvent-free system: synthesis of sn-2 docosahexaenoyl monoacylglycerol

Abstract

The enzymatic transesterification of docosahexaenoic acid (DHA) ethyl ester with glycerol was carried out by using several immobilized lipases in a solvent-free system. This reaction involves the initial formation of sn-2 docosahexaenyl monoacylglycerol. This DHA derivative is highly relevant for improving the bioavailability of DHA and it has received increasing interest in the field of nutrition. Three commercial lipases, from Rhizomucor miehei (RML), Alcaligenes sp. (AQ) and Candida antarctica-fraction B (CALB) were immobilized by interfacial adsorption on a commercial hydrophobic support (a methacrylate resin containing octadecyl groups, Sepabeads C-18) and tested for glycerolysis of DHA ethyl ester. In certain cases (e.g. immobilized CALB), the transesterification reaction continues to the formation of triacylglycerol (80%) by using a very high excess of DHA ethyl ester ((115 mmols versus 1.24 mmols of glycerol and high temperatures (50?°C). However, the same biocatalyst working at lower temperatures, 37?°C, synthetizes a 90% of sn-2 monoacylglycerol even in the presence of that a high excess of DHA ethyl ester. Interestingly, immobilized RML derivative synthesizes a 98% of sn-2 monoacylglyceride (2-MG) in 15?min at 37?°C with a 4% of immobilized biocatalyst. These high activity and regioselectivity under very mild reaction conditions are very interesting for the thermal oxidative stability of the omega-3 fatty acid as well as for the thermal stability of the biocatalyst. Using Normal Phase HPLC-ELSD and accurate commercial markers, the formation of the 2-MG was confirmed.     

Immobilization and stabilization of microbial lipases by multipoint covalent attachment on aldehyde-resin affinity: Application of the biocatalysts in biodiesel synthesis

Microbial lipase preparations from Thermomyces lanuginosus (TLL) and Pseudomonas fluorescens (PFL) were immobilized by multipoint covalent attachment on Toyopearl AF-amino-650M resin and the most active and thermal stable derivatives used to catalyze the transesterification reaction of babassu and palm oils with ethanol in solvent-free media. For this, different activating agents, mainly glutaraldehyde, glycidol and epichlorohydrin were used and immobilization parameters were estimated based on the hydrolysis of olive oil emulsion and butyl butyrate synthesis. TLL immobilized on glyoxyl-resin allowed obtaining derivatives with the highest hydrolytic activity (HA_der) and thermal stability, between 27 and 31 times more stable than the soluble lipase. Although PFL derivatives were found to be less active and thermally stables, similar formation of butyl butyrate concentrations were found for both TLL and PFL derivatives. The highest conversion into biodiesel was found in the transesterification of palm oil catalyzed by both TLL and PFL glyoxyl-derivatives.     

非水体系中脂肪酶催化合成乳酸乙基糖苷酯的工艺研究

在非水体系中 ,通过固定化脂肪酶催化合成一种新型α 羟基酸衍生物 乳酸糖苷酯。考察了常压下有机溶剂、酰基供体、不同种固定化酶、乙基糖苷的浓度、酶量和反应温度对反应的影响。研究表明在无溶剂体系中以乳酸丁酯作为酰基供体可有效地合成乳酸糖苷酯 ,固定化酶Novozym435和来源于Candida sp .菌株的细胞固定化酶 ,化学修饰的干酶粉均是合适的催化剂。最佳反应条件为 :酶浓度 75g L ,乙基葡萄糖苷的浓度为 0.4mol L ,温度为 70℃ ,转速 200r min ,反应 50h ,转化率可达 71%。在真空度为 0.09MPa的压力下 ,反应温度 65℃ ,酶浓度 75g L ,乙基葡萄糖苷 0.35mol L时 ,反应初速率可达到 607(mmol·L^-1·h^-1 ) ,40h后转化率可达到 90%。反应产物经过萃取法和硅胶柱层析方法分离 ,纯度达到 95 % (W/W)。     

Short chain fatty acid esters synthesis by commercial lipases in low-water systems and by resting microbial cells in aqueous medium

Thirteen commercial lipases in hexane and seventeen bacterial cell suspensions in aqueous media were screened for the production of ethyl valerate and ethyl butyrate. The highest esterifying activity was obtained with commercial Pancrealipase (Biozymes Inc.) and Candida rugosa lipase (Amano Enzyme Ltd) and with bacterial cell suspension from Pseudomonas fragi CRDA 446. Commercial enzymes gave molar conversion yield of 68% over 24 h as compared to 17% with whole cells in aqueous medium. However, a comparison of both sources of biocatalyst i.e. whole microbial cells and commercial lipases, based on the amount of ester produced per g of protein for a complete reaction, indicated similar activities. © Rapid Science Ltd. 1998     

Synthesis of the kyotorphin precursor benzoyl‐L‐tyrosine‐L‐argininamide with immobilized α‐chymotrypsin in sequential batch with enzyme reactivation

α‐Chymotrypsin was immobilized in activated agarose support and the stability of the biocatalyst was assessed in three polar organic solvents, namely, ethanol, diglyme, and acetonitrile. Ethanol was the solvent in which the stability of the enzyme was higher and was then selected to perform the synthesis of the kyotorphin derivative benzoyl‐tyrosine argininamide, evaluating enzyme reactivation after synthesis. Substrates for reaction were benzoyl tyrosine ethyl ester and argininamide, the reaction being performed under kinetic control. High conversion yield (85%) was obtained and the immobilized enzyme was successfully used in sequential batch reactor operation with enzyme reactivation after three batches. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:54–59, 2016     

Immobilization of porcine pancreatic lipase on poly-hydroxybutyrate particles for the production of ethyl esters from macaw palm oils and pineapple flavor

Poly-hydroxybutyrate particles (PHB) were used as support to immobilize porcine pancreatic lipase (PPL). The biocatalysts prepared were tested in the synthesis of pineapple flavor by esterification of butanol and butyric acid in heptane medium, and in the synthesis of ethyl esters by transesterification of macaw palm pulp (MPPO) and macaw palm kernel (MPKO) oils with ethanol in solvent-free systems. The effect of protein loading on the biocatalyst activity was assessed in olive oil hydrolysis. Maximum hydrolytic activity of 292.8 ± 8.60 IU/g was observed. Langmuir isotherm model was applicable to the adsorption of PPL on PHB particles. Maximum immobilized protein amount was 24.3 ± 1.70 mg/g. The optimal pH and temperature in hydrolysis reaction for the immobilized PPL were at pH 8.5 and 50 °C, while for the crude PPL extract were at pH 8.0 and 45 °C. Immobilized PPL exhibited full hydrolytic activity after 2 h of incubation in non-polar solvents. In esterification reaction, optimal conversion was around 93% after 2 h of reaction. After six esterification cycles, the biocatalyst retained 63% of its initial activity. The biocatalyst prepared attained transesterification yield of 50% after 48 h of reaction for MPKO and 35% after 96 h of reaction for MPPO.     

Two step ethanolysis: A simple and efficient way to improve the enzymatic biodiesel synthesis catalyzed by an immobilized–stabilized lipase from Thermomyces lanuginosus

In this study the immobilization and stabilization of a lipase from Thermomyces lanuginosus (TLL) on aldehyde-Lewatit (Lew-TLL) are described. TLL immobilization was rapid and over 90% of lipase activity was recovered after the immobilization. Lew-TLL was 10-fold more thermo stable than the commercial TLL preparation, Lipozyme TL-IM. The stabilized Lew-TLL was used for the enzymatic transesterification of ethanol and soybean oil. The transesterification was carried out following different strategies. First, with 7.5:1 molar ratio of ethanol:soybean oil, 15% immobilized enzyme and 4% water at 30 °C. In the presence of n-hexane, the transesterification reached 100% conversion, while in solvent-free system the yield was 75%. Second, at stoichiometric molar ratio, the yield was 70% conversion after 10 h of reaction in both systems. After this, transesterification was carried out by three stepwise additions of ethanol with a yield of 80% conversion, while a two step ethanolysis produced 100% conversion after 10 h of reaction in both solvent and solvent-free systems.     

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.     

Synthesis of functionalized polyethylenimine-grafted mesoporous silica spheres and the effect of side arms on lipase immobilization and application

In the present study, silicate mesoporous materials (MCM-41), MCM-41-grafted polyethylenimine (MCM-41@PEI), and succinated PEI containing amine, amide, and acid groups were successfully synthesized and characterized by Fourier transform infrared spectroscopy, thermogravimetric analysis, X-ray diffraction, scanning electron microscopy, transmission electron microscopy, Brunauer–Emmett–Teller analysis, and X-ray photoelectron spectroscopy. Thermomyces lanuginosa lipase (TLL) was then immobilized onto MCM-41 and polymer-grafted MCM-41 by physical adsorption. Besides, for enzyme immobilization via covalent bonding, glutaraldehyde (GLU), and hexamethylene diisocyanate (HMDI) were used as the bridges for binding the enzyme to supports. The best result was obtained with the immobilized lipase on MCM-41@PEI-GLU. In the study of the enzyme reusability, it was shown that about 83% of the initial activity could be retained after 12 cycles of uses. The immobilized lipase on the selected support was also applied for the synthesis of ethyl valerate. Following 24 h incubation in n-hexane and solvent free media, the esterification percentages were 79% and 67%, respectively.     

Immobilization of steapsin lipase on macroporous immobead-350 for biodiesel production in solvent free system

Commercially available steapsin lipase was immobilized on macroporous polymer beads (IB-350) and further investigated for biodiesel production under solvent free conditions. The fatty acid methyl ester (biodiesel) synthesis was carried out by the methanolysis of fresh and used cooking sunflower oil. The enzymatic reaction for biodiesel synthesis was optimized with various reaction parameters and the obtained reaction conditions were 1: 6 molar ratio (oil: methanol), 50 mg biocatalyst and 20% water content at 45°C for 48 h under solvent free conditions. It was observed that 94% of biodiesel was produced under the optimized reaction conditions. The four step addition of methanol at the interval of 12 h was found to be more effective. Moreover the biocatalyst was effectively reused for four consecutive recycles and was appreciably stable for 90 days. The results obtained highlight potential of immobilized steapsin lipase for biodiesel production.     

Immobilization of hog pancreas lipase in macroporous poly(vinyl alcohol)-cryogel carrier for the biocatalysis in water-poor media

Hog pancreas lipase was covalently attached to the beads of poly(vinyl alcohol)-cryogel – a macroporous hydrogel prepared by means of freeze-thaw technique. The immobilized biocatalyst thus obtained was examined in the reaction of enantioselective hydrolysis of the ethyl ester of N-benzylidene derivative of DL-phehylalanine in the medium of acetonitrile (contained 5 vol.% of water without any buffers). Eighty-three %-enantiomeric excess of the l-amino acid was reached after 144 h. Virtually the same result was obtained in the repeated use of the same immobilized biocatalyst after its 6-months-storing in a refrigerator.     

Enhanced synthesis of isoamyl acetate using liquid-gas biphasic system by the transesterification reaction of isoamyl alcohol obtained from fusel oil

In this work, the transesterification reaction of isoamyl alcohol obtained from fusel oil and leading to the synthesis of isoamyl acetate was conducted simultaneously with in situ ethanol removal, which allows to shift the reaction equilibrium toward ester synthesis. The extracellular Aspergillus oryzae lipase was immobilized into calcium alginate. Effects of immobilization conditions on the loading efficiency and on the specific activity of entrapped lipase were investigated. The kinetic transfer of volatile reactants from the reactor was investigated using an experimentally first order kinetic model, in order to approve the feasibility of the liquid-gas system with continuous ethanol removal in the ester synthesis. The effects of the most influent parameters affecting the reaction have been also investigated using a Doehlert matrix design. The better operating conditions for isoamyl acetate synthesis were: a temperature of 68.5°C and a respective isoamyl alcohol and A. oryzae lipase concentration of 0.72 M and 2.39 g/L. At these conditions, the resulting reaction conversion and ethanol extraction yields were of 89.55 and 69.60%, respectively. The use of the fluidized bed reactor with continuous ethanol removal has allowed to improve the reaction conversion which was two times than the conversion higher obtained in batch reactor. Furthermore, under the optimized conditions in the fluidized bed reactor, the reaction conversion and the ethanol extraction yields were increased by 44.8 and 36.2%, respectively.     

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.     

Application of multi-component reaction for covalent immobilization of two lipases on aldehyde-functionalized magnetic nanoparticles; production of biodiesel from waste cooking oil

Lipase from Rhizomucor miehei (RML) and Thermomyces lanuginosa lipase (TLL) were immobilized on silica core-shell magnetic nanoparticles (Fe₃O₄@SiO₂) produced by coating Fe₃O₄ core with silica shell. The nanoparticles were functionalized with aldehyde groups followed by immobilization of RML and TLL by using a multi-component reaction in an extremely mild condition. Rapid immobilization of both enzymes (1.5−12 h) with high immobilization yields (81–100%) was observed. The maximum loading capacity of the support was determined to be 81 mg for RML and 97 mg for TLL. The thermal stability of the immobilized derivatives of RML and TLL were greatly improved by retaining 54 and 97 % of their initial activities at 65 °C, respectively. The immobilized preparations were used to produce biodiesel by transesterification of waste cooking oil. In an optimization study, Response Surface Methodology (RSM) and a central composite rotatable design (CCRD) were used to study the effect of amount of biocatalyst, temperature, reaction time, water adsorbent (wt.%) and ratio of t-butanol to oil (wt.%) on the yield of biodiesel production. Biodiesel production yield by immobilized TLL reached 93.1 % under optimal conditions while the maximum yield for RML was 57.5 %. Both immobilized derivatives showed high reusability after 5 cycles of the reaction.     

Short chain flavour esters synthesis by microbial lipases

Summary The peparative synthesis of 35 short chain flavour esters by lipases fromMucor miehi, Aspergillus sp.,Candida rugosa andRhizopus arrhizus was investigated in organic media. Acetic, propionic, butyric, valeric and caproic acids, as well as methanol, ethanol, butanol, i-pentanol, hexanol, citronellol and geraniol were used as substrates. Most of the esters were synthesized in good yield by at least one of the lipase preparations tested. Different conversion yields were observed according to the lipase specificity toward the acid or the alcohol moiety of the ester. Methyl- and ethyl acetates were also produced by changing the organic solvent. Enzymatic catalysis in organic solvent is thought to be a valuable method for preparative synthesis of flavour esters.     

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.     

Enzymatic synthesis of glycerides from DHA-enriched PUFA ethyl ester by glycerolysis under vacuum

Pseudomonas lipase immobilized on CaCO₃ powder was used for the glycerolysis of n−3 polyunsaturated fatty acid ethyl esters to prepare nutritionally valuable glycerides. The initial ethyl ester contained 65 or 99% docosahexaenoic acid ethyl ester (DHAEE) which is very unstable and readily oxidized. The process performance was intensified by: (1) using Pseudomonas lipase which has good specificity for docosahexaenoic acid (DHA), (2) shifting the reaction equilibrium by evaporation of the resulted ethanol under vacuum and (3) enhancing the enzyme operational stability by immobilization on CaCO₃ powder. Under these conditions, over 90% conversion of DHAEE was achieved in 5 h and the oxidative deterioration of DHA was avoided. The final product contained 53% partial glyceride and, thus, had good emulsifying power. The catalyst was reused 5 times showing a very good stability in this system. Other lipases were tried for this reaction and different glyceride compositions were obtained depending on the enzyme specificity for the 1(3)-position of glycerol.