Characteristics of immobilized lipase-catalyzed hydrolysis of olive oil of high concentration in reverse phase system

Candida rugosa lipase immobilized by adsorption on swollen Sephadex LH-20 could almost completely hydrolyze 60% (v/v) olive oil in isooctane. Kinetic analysis of the lipase-catalyzed hydrolysis reaction was found to be possible in this system. Amount of fatty acids produced was linearly proportional to the enzyme concentration of 720 mug/g wet gel. The specific enzyme activity was 217 units/mg protein at 60% (v/v) olive oil concentration. When the initial rate is plotted versus concentration of olive oil, this system did not follow Michaelis-Menten kinetics. Maximum activity was obtained at pH 7, but optimum temperature shifted towards higher one with the increase of olive oil concentration. Among the various chemical compounds tested, Hg(2+) and Fe(2+) inhibited the lipase seriously. As the concentration of olive oil increased, the rate of the hydrolysis also increased, but degree of the hydrolysis was observed to decrease. The supply of water from the inside of the gel to the surface of the gel was the main factor for the control of the rate of hydrolysis in batch hydrolysis. The immobilized lipase was used to hydrolyze olive oil two times. Achievement of chemical equilibrium took a longer time with the addition of water and the degree of hydrolysis decreased in the second consecutive trial. After the second hydrolysis trial, the gels were regenerated in a packed column first by eluting out both residual fatty acids around the gel particles and the accumulated glycerol with ethanol and then with 0.05M phosphate buffer, pH 7. The immobilized lipase on the regenerated gel showed the same hydrolysis activity as the original one.     

Effect of solvents on hydrolysis of olive oil by immobilized lipase in reverse phase system

Summary Lipase fromCandida rugosa was immobilized by adsorption on three supports which could contain water available for the hydrolysis of olive oil in a reverse phase system. To select the most suitable solvent for this system, the effect of organic solvents on the stability and catalytic activity of immobilized lipase for the hydrolysis reaction has been examined. The results revealed that isooctane was superior to any other solvents tested in this study for enzymatic fat splitting in a reverse phase system. Also the effect of the solvent polarity on the hydrolysis of olive oil has been examined in detail using various organic solvents mixed with an equivolume of isooctane. It was found that the hydrolysis of olive oil by immobilized lipase was markedly affected by the polarity of reaction solvents.     

Numerical simulation and deacidification of nanomagnetic enzyme conjugate in a liquid–solid magnetic fluidized bed

The conventional deacidification method is difficult to achieve a better refining effect due to the high acid value in the rice bran crude oil, and the enzymatic esterification deacidification method can effectively reduce the acid value without generating chemical waste. In this study, the free lipase was immobilized on a magnetic polymer carrier Fe₃O₄/SiOx-g-P (GMA: glycidyl methacrylate) to obtain a immobilized lipase with a particle size of 105.30 ± 1.1 nm and an enzyme activity of 6580 ± 9.6 PLU/g (PLU: enzyme activity unit). Based on the batch deacidification process parameters, a multi-stage magnetic fluidized bed continuous circulation deacidification system was designed, and then the motion law of nanomagnetic immobilized lipase particles in liquid–solid magnetic fluidized bed was simulated by computer. When the iterative step was 5 × 10⁻⁵ s, the open porosity of the porous plate was 35.0%, the rice bran oil flow rate was 3.0 mm/s, and the magnetic field strength was 25.0 mT, which was beneficial to the deacidification reaction of rice bran oil. Under the conditions of magnetic immobilized lipase dosage of 4.0%, the phytosterol dosage of 22.0%, the molecular sieve dosage of 10%, the esterification temperature of 78.0 °C and the FFA (free fatty acid) content in rice bran oil decreased to 1.5%, after 48 h of reaction. The conversion rate is 92.8%, which provides a theoretical basis for the subsequent guidance of magnetic fluidized bed enzymatic continuous deacidification.     

Stability of the lipase immobilized on DEAE-Sephadex for continuous lipid hydrolysis in organic solvent

Summary Continuous hydrolysis reaction was carried out in glass-column by using lipase fromCandida rugosa immobilized on DEAE-Sephadex A50. Substrate olive oil dissolved in hydrophobic organic solvent (isooctane) was supplied into the reactor with a concurrent stream of aqueous buffer. Stability of the immobilized enzyme was greatly increased in higher substrate concentration. Glyccrol added in the aqueous stream showed stabilizing effect against the organic solvent; half life was extended from 220 hrs to 450 hrs by 15% glycerol supplemented at 30°C.     

Hydrolysis of olive oil catalyzed by surfactant-coated<Emphasis Type="Italic">Candida rugosa</Emphasis> lipase in a hollow fiber membrane reactor

In this study, we invetigated the hydrolysis of olive oil catalyzed by a surfactant-coatedCandida rugosa lipase in a hydrophilic polyacrylonitrile hollow fiber membrane reactor and then compared the results to those using the native lipase. The organic phase was passed through the hollow inner fibers of the reactor and consisted of either the coated lipase and olive oil dissolved in isooctane or the coated lipase dissolved in pure olive oil. The aqueous phase was pumped through the outer space. After 12 h and with conditions of 30°C, 0.12 mg enzyme/mL and 0.62 M olive oil, the substrate conversion of the coated lipase reached 60%. This was twice the conversion for the same amount of native lipase that was pre-immobilized on the membrane surface. When using pure olive oil, after 12 h the substrate conversion of the coated lipase was 50%. which was 1.4 times higher than that of the native lipase.     

Enantioselective synthesis of (S)‐naproxen using immobilized lipase on chitosan beads

S‐naproxen by enantioselective hydrolysis of racemic naproxen methyl ester was produced using immobilized lipase. The lipase enzyme was immobilized on chitosan beads, activated chitosan beads by glutaraldehyde, and Amberlite XAD7. In order to find an appropriate support for the hydrolysis reaction of racemic naproxen methyl ester, the conversion and enantioselectivity for all carriers were compared. In addition, effects of the volumetric ratio of two phases in different organic solvents, addition of cosolvent and surfactant, optimum pH and temperature, reusability, and inhibitory effect of methanol were investigated. The optimum volumetric ratio of two phases was defined as 3:2 of aqueous phase to organic phase. Various water miscible and water immiscible solvents were examined. Finally, isooctane was chosen as an organic solvent, while 2‐ethoxyethanol was added as a cosolvent in the organic phase of the reaction mixture. The optimum reaction conditions were determined to be 35 °C, pH 7, and 24 h. Addition of Tween‐80 in the organic phase increased the accessibility of immobilized enzyme to the reactant. The optimum organic phase compositions using a volumetric ratio of 2‐ethoxyethanol, isooctane and Tween‐80 were 3:7 and 0.1% (v /v/v), respectively. The best conversion and enantioselectivity of immobilized enzyme using chitosan beads activated by glutaraldehyde were 0.45 and 185, respectively.     

Pretreatment of coconut mill effluent using celite‐immobilized hydrolytic enzyme preparation from Staphylococcus pasteuri and its impact on anaerobic digestion

Biological treatment of oil and grease (O&G)‐containing industrial effluents has long been a challenging issue. Practically feasible avenues to bring down their O&G load and enhance treatability are desired. In one such endeavour, the partially purified lipase from Staphylococcus pasteuri COM‐4A was immobilized on celite carrier and applied for the enzymatic hydrolysis of unsterilized coconut oil mill effluent. In batch hydrolysis experiments, optimum conditions of 1% (w/v) immobilized lipase beads, one in four effluent dilution, and a contact time of 30 h resulted in 46% and 24% increase in volatile fatty acids and long‐chain fatty acids and a concomitant 52% and 32% decrease in O&G and chemical oxygen demand (COD) levels, respectively. Batch anaerobic biodegradation trials with this prehydrolyzed effluent showed 89%, 91%, and 90% decrease in COD, proteins, and reducing sugars, respectively. These results were validated in a hybrid stirred tank—upflow anaerobic sludge blanket reactor. Average COD and O&G reductions effected by the hybrid reactor were found to be 89% and 88%, whereas that by the control reactor without enzymatic hydrolysis were only 60% and 47%, respectively. A maximum of 0.86 L methane gas was generated by the hybrid reactor per gram of VS added. Hence, this celite‐immobilized crude lipase, sourced from a native laboratory isolate, seems to be a workable alternative to commercial enzyme preparations for the management of lipid‐rich industrial effluents. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1249–1258, 2015     

Continuous hydrolysis of olive oil by immobilized lipase in organic solvent

Lipase (EC 3.1.1.3) from Candida rugosa was immobilized with DEAE-Sephadex A50, Sephadex G50, Sephadex LH-20, Amberlite IRA94, and Amberlite XAD-7. The enzye immobilized with DEAE-Sephadex A50 was found to be most effective for continuous hydrolysis of olive oil in isooctane. For the continuous reaction, 0.2 g of dry immobilized enzyme was swollen with predetermined amount of water, and packed in a glass column reactor. When the organic solvent (Isooctane) containing olive oil substrate was cocurrently fed with aqueous buffer, the two phases were evenly distributed throughout the packed bed without surfactant supplement or prior mixing of the two phases. A small amount of the surfactant (AOT) was used only in packing procedure, and no additional surfactant was necessary thereafter. Effects of initial water content of the swollen gel, buffer types, and strength were examined in the continuous reaction. Our results suggest that the operational half-life was affected by desorption of the bound enzyme. Under the conditions of 20% olive oil in isooctane and 25 mM triethanolamine buffer (pH 7.0), operational half life was 220 h at 30 degrees C. The reactor was also operable with n-hexane, but the operational stability of the immobilized enzyme in n-hexane was only half of that in isooctane. Our results indicate that various enzyme carrier having hydrophilic or amphiphilic properties could be used for two-phase continuous reaction in packed-bed column, reactor without any surfactant supply or prior dispersion of the two immiscible phases. (c) 1992 John Wiley & Sons, Inc.     

Lipase-mediated hydrolysis of blackcurrant oil

Four commercially available lipases, both free and immobilized, were tested for their ability to catalyze hydrolysis of blackcurrant (Ribes nigrum) oil using two different approaches. The lipase from Mucor miehei was studied free and immobilized in two different ways. The former series of enzymic reactions were performed in tap water at 40 degrees C, but the latter series of enzymic processes were carried out in mixtures of isooctane and phosphate buffer (in a typical 2/1 ratio of the components) at 30 degrees C. These conditions were optimized to increase and/or to maximize the yields of the products, which were priority targets in this study. A rate of hydrolysis and a selective preference of the hydrolytic enzymes towards fatty acids, with a special focus on enrichment of alpha-linolenic acid and/or gamma-linolenic acid, were studied. Higher rates of hydrolysis of the blackcurrant oil in the former series of reactions were observed with the immobilized lipase from Pseudomonas cepacia used as biocatalyst. In the latter approach, the most favorable results of the rate of hydrolysis of the target blackcurrant oil were achieved with the immobilized lipase from Mucor miehei employed as biocatalyst. Only three lipases, selected from a series of lipases tested during this investigation, displayed specificity towards alpha-linolenic acid and gamma-linolenic acid, i.e. the immobilized lipase from P. cepacia, lipase from M. miehei and lipase from P. fluorescens.     

Prediction of continuous reactors performance based on batch reactor deactivation kinetics data of immobilized lipase

Experiments on deactivation kinetics of immobilized lipase enzyme fromCandida cylindracea were performed in stirred batch reactor using rice bran oil as the substrate and temperature as the deactivation parameter. The data were fitted in first order deactivation model. The effect of temperature on deactivation rate was represented by Arrhenius equation. Theoretical equations were developed based on pseudo-steady state approximation and Michaelis-Menten rate expression to predict the time course of conversion due to enzyme deactivation and apparent half-life of the immobilized enzyme activity in PFR and CSTR under constant feed rate policy for no diffusion limitation and diffusion limitation of first order. Stability of enzyme in these continuous reactors was predicted and factors affecting the stability were analyzed.     

Hydrolysis of triglyceride by the whole cell of Pseudomonas putida 3SK in two-phase batch and continuous reactors systems

Batch and continuous hydrolysis of olive oil in an organic-aqueous two-phase system using the live whole cell of Pseudomonas putida 3SK as a source of a lipase is investigated. The strain was not only fully viable and grown well, but also produced extracellular lipase simultaneously. The degree of hydrolysis, depending on olive oil concentration in the solvents, was maximal at 13.5% (w/v) and decreased with the increase of the substrate concentration. At the optimal condition, a degree of hydrolysis higher than 95% was achieved with 24 h at 30 degrees C when the reaction was carried out in a two-phase batch stirred reactor. For long-term operation a continuous stirred reactor was designed. When the reaction was carried out in a continuous stirred reactor, the degree was hydrolysis reached 86% at a dilution rate of 0.2 h(-1). Satisfactory performance of a two-phase bioreactor was obtained in a long-term continous operation, which lasted for at least 30 days by feeding organic solvent containing olive oil and aqueous media separately. (c) 1994 John Wiley & Sons, Inc.     

Continuous hydrolysis of oil by immobilized lipase in a countercurrent reactor

Lipase from Pseudomonas fluorescens biotype I was immobilized by adsorption of anion exchange resin using glutaraldehyde to enhance the adsorption. The activity yield of the immobilized lipase was very low (below 1%) when lipase activity was measured using emulsion substrate. The activity yield was 10-70% when lipase activity was measured using non-emulsion substrate. Countercurrent reactors for hydrolysis of oil using non-emulsion substrate were studied. A fluidized bed reactor was found to be superior to a fixed bed one since in a fixed bed reactor the separation rate of the two layers was slow and the flow rate of the reactor had to be slower than the separation rate. A fluidized bed reactor system equipped with settling compartments and stirring compartments was devised. Continuous lipolysis at 60 degrees C and continuous separation of oily product and water soluble product were performed. After continuous operation for more than 3 months, 70% of the initial activity of the immobilized lipase was observed at the end of the reaction.     

Continuous glycerolysis of olive oil by Chromobacterium viscosum lipase immobilized in liposome in reversed micelles

Chromobacterium viscosum lipase which has adsorbed on liposome and solubilized in microemulsion droplets of glycerol containing a little amount of water could catalyze the glycerolysis of olive oil. Studies on the continuous glycerolysis of olive oil by the immobilized enzyme was done at 37 degrees C in continuous stirred vessel bioreactor with polysulfone membrane. The effect of the flow rate of substrate (olive oil) in isooctane on the conversion and composition of the outlet was investigated using high-performance liquid chromatography (HPLC). The conversion increased with decrease in the flow rate. And we studied the effect of water content in the glycerol-water-lipase solution on the glycerolysis reaction. The conversion to desirable products, mono- and di-olein, was improved without a substantial production of oleic acid at lower water concentrations, i.e., below 8.0% (w/v) which corresponds to a w(o) value of 0.97. At water concentration higher than 8.0% (w/v), the amount of free fatty acid was dramatically increased. Higher operational stability of the enzyme reactor, and the half-line of the enzyme continuous reaction was about 7 weeks.     

Lipase catalysed hydrolysis of ricebran oil by free and immobilised enzyme system in batch stirred reactor

A change of the reaction rate was observed for the lipasecatalysed hydrolysis of ricebran oil in a batch stirred tank reactor using immobilized lipase enzyme as compared to free enzyme. The reactor rate was observed to be controlled mainly by factors like temperature, pH, initial enzyme concentration, initial substrate concentration and initial products concentration.     

Production, purification and characterization of thermophilic lipase from Bacillus sp. THL027

A low-cost medium, MGRS, has been developed for growth and lipase production from Bacillus THL027 at 65 degrees C and pH 7.0. MGRS was composed of 2% (v/v) buffer solution (7.3% (w/v) Na(2)HPO(4), 3.2% (w/v) KH(2)PO(4), pH 7.2), 40 microg ml(-1) FeSO(4) and 40 microg ml(-1) MgSO(4), 0.1% (w/v) (NH(4))(2)SO(4) supplemented with 3% NaCl, 0.1% glucose, 1.0% rice bran oil and 0.5% (w/v) rice bran. The lipase was purified 2.6-fold to apparent homogeneity by ultrafiltration and gel filtration chromatography. Its molecular mass was 69 kDa. The purified enzyme was characterized for its general physical properties.     

Lipase-catalyzed hydrolysis of olive oil in chemically-modified AOT/isooctane reverse micelles in a hollow fiber membrane reactor

The hydrolysis of olive oil catalyzed by Candida rugosa lipase in sodium bis(2-ethylhexyl)sulfosuccinate (AOT)/isooctane and the synthetic sodium bis(2-ethylhexyl polyoxyethylene)sulfosuccinate (MAOT)/isooctane reverse micellar systems was investigated in a polysulfone hollow fiber membrane reactor with recycle of the reaction mixture. Lipase was completely retained by the membrane while olive oil and oleic acid freely passed through. The retention of reverse micelles depended on W ₀ (molar ratio of water to surfactant). At an olive oil concentration of 0.23 mol l^–1 the final substrate conversion in the MAOT micellar system was about 1.4 times of that in the AOT micellar system.     

Lipase applications in oil hydrolysis with a case study on castor oil: a review

Lipase (triacylglycerol acylhydrolase) is a unique enzyme which can catalyze various types of reactions such as hydrolysis, esterification, alcoholysis etc. In particular, hydrolysis of vegetable oil with lipase as a catalyst is widely studied. Free lipase, lipase immobilized on suitable support, lipase encapsulated in a reverse micelle and lipase immobilized on a suitable membrane to be used in membrane reactor are the most common ways of employing lipase in oil hydrolysis. Castor oil is a unique vegetable oil as it contains high amounts (90%) of a hydroxy monounsaturated fatty acid named ricinoleic acid. This industrially important acid can be obtained by hydrolysis of castor oil. Different conventional hydrolysis processes have certain disadvantages which can be avoided by a lipase-catalyzed process. The degree of hydrolysis varies widely for different lipases depending on the operating range of process variables such as temperature, pH and enzyme loading. Immobilization of lipase on a suitable support can enhance hydrolysis by suppressing thermal inactivation and estolide formation. The presence of metal ions also affects lipase-catalyzed hydrolysis of castor oil. Even a particular ion has different effects on the activity of different lipases. Hydrophobic organic solvents perform better than hydrophilic solvents during the reaction. Sonication considerably increases hydrolysis in case of lipolase. The effects of additives on the same lipase vary with their types. Nonionic surfactants enhance hydrolysis whereas cationic and anionic surfactants decrease it. A single variable optimization method is used to obtain optimum conditions. In order to eliminate its disadvantages, a statistical optimization method is used in recent studies. Statistical optimization shows that interactions between any two of the following pH, enzyme concentration and buffer concentration become significant in presence of a nonionic surfactant named Span 80.     

Immobilization of Candida rugosa lipase by cross-linking with glutaraldehyde followed by entrapment in alginate beads

Candida rugosa lipase was immobilized by first cross-linking with glutaraldehyde and then entrapping in calcium alginate beads. The presence of 2-propanol during cross-linking markedly improved the enzyme activity and activity recovery. Maximal enzyme activity (2.1?mmol?h^?1?g^?1 immobilized conjugate, wet weight) and activity recovery (117%) were observed at 30% (v/v) 2-propanol for hydrolysis of olive oil, which were 1.7 and 2.0 times higher than those of the immobilized enzyme prepared in the absence of 2-propanol. The half-life of the immobilized lipase prepared by entrapment after cross-linking in 30% 2-propanol was 1.6 times higher than that prepared by entrapment of the native lipase without cross-linking and 2-propanol pretreatment. The enantioselectivity of the former was 11 times higher than that of the latter for hydrolysis of racemic ketoprofen ethyl ester.     

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)).     

Ester hydrolyses in reversed micelles using lipase

Lipases are enzymes which require a favourable reaction system for efficient catalysis of their hydrophobic substrates and reversed micellar environment is one such medium which offers many advantages. Hydrolytic studies of esters of paranitrophenol and glycerol using imidazole and four fungal lipases are studied in AOT/isooctane reversed micelles. The effect of water and surfactant concentration on the hydrolysis of rice bran oil is investigated and the overall potential of the reversed micellar system for hydrolytic reactions is assessed.