Production of lipase in a fermentor using a mutant strain of Corynebacterium species: its partial purification and immobilization

Extracellular Corynebacterium lipase was produced using a 2.5 L Chemap fermentor using 1300 ml fermentation medium at temperature 33 degrees C, agitator speed 50 rpm, aeration rate 1 VVM having KLa 16.21 hr(-1). Crude lipase was purified by salting out method followed by dialysis and immobilized using calcium alginate gel matrix followed by glutaraldehyde cross linking Purification process increased specific activity of enzyme from 2.76 to 114.7 IU/mg. Activity of immobilized enzyme was 107.31 IU/mg. Optimum temperature for purified and immobilized enzyme activity were 65 degrees and 50 degrees C respectively. Optimum pH was 8.0 in both the cases, Km and Vmax value for purified lipase were 111.1 micromol/min and 14.7% respectively. Ca2+ (5 mM) was found to be stimulator for enzyme activity. Immobilized lipase retained 68.18% of the original activity when stored for 40 days.     

Glutaraldehyde activation of polymer Nylon-6 for lipase immobilization: enzyme characteristics and stability

An extracellular alkaline lipase of a thermo tolerant Bacillus coagulans BTS-3 was immobilized onto glutaraldehyde activated Nylon-6 by covalent binding. Under optimum conditions, the immobilization yielded a protein loading of 228 microg/g of Nylon-6. Immobilized enzyme showed maximum activity at a temperature of 55 degrees C and pH 7.5. The enzyme was stable between pH 7.5-9.5. It retained 88% of its original activity at 55 degrees C for 2h and also retained 85% of its original activity after eight cycles of hydrolysis of p-NPP. Kinetic parameters Km and Vmax were found to be 4mM and 10 micromol/min/ml, respectively. The influence of organic solvents on the catalytic activity of immobilized enzyme was also evaluated. The bound lipase showed enhanced activity when exposed to n-heptane. The substrate specificity of immobilized enzyme revealed more efficient hydrolysis of higher carbon length (C-16) ester than other ones.     

Preparation and characterization of kappa-carrageenan immobilized urease

Urease was encapsulated within kappa-carrageenan beads. Various parameters, such as amount of kappa-carrageenan and enzyme activity, were optimized for the immobilization of urease. Immobilized urease was thoroughly characterized for pH, temperature, and storage stabilities and these properties were compared with the free enzyme. The free urease activity quickly decreased and the half time of the activity decay was about 3 days at 4 degrees C. The immobilized urease remained very active over a long period of time and this enzyme lost about 70.43% of its orginal activity over the period of 26 days for storage at 4 degrees C. The Michaelis constant (Km) and maximum reaction velocity (Vmax) were calculated from Lineweaver-Burk plots for both free and immobilized enzyme systems. Vmax = 227.3 U/mg protein, Km = 65.6 mM for free urease and Vmax = 153.9 U/mg protein, Km = 96.42 mM for immobilized urease showed a moderate decrease of enzyme specific activity and change of substrate affinity.     

Some properties of free and immobilized alpha-amylase from Penicillium griseofulvum by solid state fermentation

Alpha-amylase was produced from Penicillium griseofulvum by an SSF technique. Alpha-amylase was immobilized on Celite by an adsorption method. Various parameters, such as effect of pH and temperature, substrate concentration, operational and storage stability, ability to hydrolyze starch and products of hydrolysis were investigated; these findings were compared with the free enzyme. The activity yield of immobilization was 87.6%. The optimum pH and temperature for both enzymes were 5.5 degrees C and 40 degrees C, respectively. The thermal, and the operational and storage stabilities of immobilized enzyme were better than that of the free enzyme. Km and Vmax were calculated from Lineweaver-Burk plots for both enzymes. Km values were 9.1 mg mL(-1) for free enzyme, and 7.1 mg mL(-1) for immobilized enzyme. The Vmax of the immobilized enzyme was approximately 40% smaller than that of the free enzyme. The hydrolysis ability of the free and immobilized enzyme were determined as 99.3% and 97.9%, respectively. Hydrolysis products of the a-amylase from P. griseofulvum were maltose, unidentified oligosaccharides, and glucose.     

Conformational changes in human urokinase induced by a specific reduction of disulfide bond in Cys-194-Cys-222 associated with exhibition of enzymatic activity

The mechanism of action of hepatic triacylglycerol lipase (EC 3.1.1.3) was examined by comparing the hydrolysis of a water-soluble substrate, tributyrin, with that of triolein by hepatic triacylglycerol lipase purified from human post-heparin plasma. The hydrolyzing activities toward tributyrin and triolein were coeluted from heparin-Sepharose at an NaCl concentration of 0.7 M. The maximal velocity of hepatic triacylglycerol lipase (Vmax) for tributyrin was 17.9 mumol/mg protein per h and the Michaelis constant (Km) value was 0.12 mM, whereas the Vmax for triolein was 76 mumol/mg per h and the Km value was 2.5 mM. The hydrolyses of tributyrin and triolein by hepatic triacylglycerol lipase were inhibited to similar extends by procainamide, NaF, Zn2+, Cu2+, Mn2+, SDS and sodium deoxycholate. Triolein hydrolysis was inhibited by the addition of tributyrin. Triolein hydrolysis was also inhibited by the addition of dipalmitoylphosphaidylcholine vesicles. In contrast, the additions of triolein emulsified with Triton X-100 and dipalmitoylphosphatidylcholine vesicles enhanced the rate of tributyrin hydrolysis by hepatic triacylglycerol lipase. In the presence of dipalmitoylphosphatidylcholine, the Vmax and Km values of hepatic triacylglycerol lipase for tributyrin were 41 mumol/mg protein per h and 0.12 mM, respectively, indicating that the enhancement of hepatic triacylglycerol lipase activity for tributyrin by dipalmitoylphosphatidycholine vesicles was mainly due to increase in the Vmax. The enhancement of hepatic triacylglycerol lipase activity for tributyrin by phospholipid was not correlated with the amount of tributyrin associated with the phospholipid vesicles. On Bio-Gel A5m column chromatography, glycerol tri[1-14C]butyrate was not coeluted with triolein emulsion, and hepatic triacylglycerol lipase activity was associated with triolein emulsion even in the presence of 2 mM tributyrin. These results suggest that hepatic triacylglycerol lipase has a catalytic site for esterase activity and a separate site for lipid interface recognition, and that on binding to a lipid interface the conformation of the enzyme changes, resulting in enhancement of the esterase activity.     

Preparation of cross-linked enzyme aggregates by using bovine serum albumin as a proteic feeder

Addition of bovine serum albumin (BSA) as a proteic feeder facilitates obtaining cross-linked enzyme aggregates (CLEAs) in cases where the protein concentration in the enzyme preparation is low and/or the enzyme activity is vulnerable to the high concentration of glutaraldehyde required to obtain aggregates. CLEAs of Pseudomonas cepacia lipase and penicillin acylase were prepared. CLEA of lipase prepared in the presence of BSA retained 100% activity whereas CLEA prepared without BSA retained only 0.4% activity of the starting enzyme preparation. Lipase CLEA showed 12-fold increase in activity over free enzyme powder when the CLEA was used in transesterification of tributyrin. For the transesterification of Jatropha oil, while free enzyme powder required 8 h and 50 mg lipase to obtain 77% conversion, CLEA required only 6 h and 6.25 mg lipase to obtain 90% conversion. In the case of penicillin acylase, 86% activity could be retained in CLEA prepared with BSA whereas CLEA made without BSA retained only 50% activity. CLEA prepared without BSA lost 20% activity after 8 h at 45 degrees C whereas CLEA with BSA retained full activity. CLEA prepared with BSA showed Vmax/Km of 36.3 min-1 whereas CLEA prepared without BSA had Vmax/Km of 17.4 min-1 only. Scanning electron microscopy analysis showed that CLEAs prepared in the presence of BSA were less amorphous and closer in morphology to CLEAs of other enzymes described in the literature.     

脂肪酶的固定化及其性质研究

采用吸附与交联相结合的方法国定化脂肪酶,研究了脂肪酶固定化的工艺条件,并考察了固定化脂肪酶的催化性能和稳定性。试验结果表明,WA20树脂固定化脂肪酶的最适条件是：酶液pH7．0、给酶量300IU／g树脂、固定时间8h,所得固定化脂肪酶的活力约为165IU／g树脂;固定化酶稳定性较高,在冰箱内贮存6个月活力没有下降,操作半衰期约为750h,而未用戌二醛文联的固定化脂肪酶操作半衰期仅约290h;固定化脂肪酶催化橄榄油水解的最适条件是：PH8．0、温度55℃、底物浓度60％（V／V）、搅拌转速500r／m。     

Enhancing performance of lipase immobilized on methyl-modified silica aerogels at the adsorption and catalysis processes: Effect of cosolvents

Hydrophobic silica aerogels modified with methyl group were applied as support to immobilize Candida rugosa lipase (CRL). At the adsorption process, different alcohols were used to intensify the immobilization of CRL. The results showed that n-butanol wetting the hydrophobic support prior to contacting with enzyme solution could promote lipase activity, but the adsorption quantity onto the support decreased. Based on this, a novel immobilization method was proposed: the support contacted with enzyme solution without any alcohols, and then the immobilized enzymes were activated by 90% (V) n-butanol solution. The experimental results showed that this method could keep high adsorption quantity (413.0 mg protein/g support) and increase the lipase specific activity by more than 50%. To improve the stability of immobilized lipase, the support after adsorption was contacted with n-octane to form an oil layer covering the immobilized lipases, thus the leakage can be decreased from over 30–4% within 24 h. By utilizing proper cosolvents, a high enzyme activity and loading capacity as well as little loss of lipase was achieved without covalent linkage between the lipase and the support. This is known to be an excellent result for immobilization achieved by physical adsorption only.     

Preparation and application of poly(N,N-dimethylacrylamide-co-acrylamide) and poly(N-isopropylacrylamide-co-acrylamide)/kappa-Carrageenan hydrogels for immobilization of lipase

In the present of this study, two novel polymeric matrixes that are poly(N,N-dimethylacrylamide-co-acrylamide) and poly(N-isopropylacrylamide-co-acrylamide)/kappa-Carrageenan was synthesized and applied for immobilization of lipase. For the immobilization of enzyme, two different immobilization procedures have been carried out via covalently binding and entrapment methods. On the free and immobilized enzymes activities, optimum pH, temperature, storage and thermal stability was investigated. The optimum temperature for free, covalently immobilized and entrapped enzymes was found to be 30, 35 and 30 degrees C, respectively. Optimum pH for both free and immobilized enzymes was also observed at pH 8. Maximum reaction rate (Vmax) and Michaelis-Menten constant (Km) were determined for free and immobilized lipases. Furthermore, the reuse numbers of immobilized enzymes also studied. It was observed that after 40th use in 5 days, the retained activities for covalently immobilized and entrapped lipases were found as 39% and 22%, respectively. Storage and thermal stability of enzyme was also increased by as a result of immobilization procedures.     

Immobilization of Amaranthus leaf oxalate oxidase on alkylamine glass

A membrane bound oxalate oxidase from leaves of Amaranthus spionsus has been partially purified and immobilized on alkylamine glass with a yield of 9.2 mg protein/g support. The enzyme retained 99.4% of initial activity of free enzyme after immobilization. There was no change in the optimum pH (3.5) and Vmax but the temperature for maximum activity was slightly decreased (35 degrees C) and energy of activation (Ea) and Km for oxalate were increased after immobilization. The immobilized enzyme preparation was stable for 6 months, when stored in distilled water at 4 degrees C. Presence of Cl- did not affect the activity of immobilized enzyme.     

Improvement of the functional properties of a thermostable lipase from alcaligenes sp. via strong adsorption on hydrophobic supports

Lipase QL from Alcaligenes sp. is a quite thermostable enzyme. For example, it retains 75% of catalytic activity after incubation for 100 h at 55 °C and pH 7.0. Nevertheless, an improvement of the enzyme properties was intended via immobilization by covalent attachment to different activated supports and by adsorption on hydrophobic supports (octadecyl-sepabeads). This latter immobilization technique promotes the most interesting improvement of enzyme properties: (a) the enzyme is hyperactivated after immobilization: the immobilized preparation exhibits a 135% of catalytic activity for the hydrolysis of p-nitrophenyl propionate as compared to the soluble enzyme; (b) the thermal stability of the immobilized enzyme is highly improved: the immobilized preparation exhibits a half-life time of 12 h when incubated at 80 °C, pH 8.5 (a 25-fold stabilizing factor regarding to the soluble enzyme); (c) the optimal temperature was increased from 50 °C (soluble enzyme) up to 70 °C (hydrophobic support enzyme immobilized preparations); (d) the enantioselectivity of the enzyme for the hydrolysis of glycidyl butyrate and its dependence on the experimental conditions was significantly altered. Moreover, because the enzyme becomes reversibly but very strongly adsorbed on these highly hydrophobic supports, the lipase may be desorbed after its inactivation and the support may be reused. Very likely, adsorption occurs via interfacial activation of the lipase on the hydrophobic supports at very low ionic strength. On the other hand, all the covalent immobilization protocols used to immobilize the enzyme hardly improved the properties of the lipase.     

Immobilization of Lipase from Rhizopus Niveus: A Way to Enhance its Synthetic Activity in Organic Solvent

Lipase (EC 3.1.1.3) from Rhizopus niveus was immobilized by physical adsorption on various carriers, including different types of Celite, Spherosil and Duolite. After the enzyme immobilization, the recovered hydrolytic and synthetic activities on the different carriers were then determined. The results showed that the highest synthetic activity was obtained when Duolite XAD 761 was used as the carrier. However the recovered hydrolytic activity after the immobilization on this resin was relatively low although this carrier showed the best protein loading capacity. The highest recovered hydrolytic activity was observed when the lipase was immobilized on Celite Hyflo-Supercel using an immobilization buffer adjusted to pH 4. The comparison of the free and immobilized lipase specific activities suggest that the immobilization on Celite Hyflo-Supercel, Spherosil XOA 200 and silica has enhanced the lipase hydrolytic activity. On the other hand, the use of the lipase immobilized on Duolite XAD 761 as biocatalyst of synthetic reaction, compared to that of the free enzyme, allows the reaction initial velocity to be increased 12.2-fold. In addition, the synthetic activity of the lipase immobilized on Duolite XAD 761 was shown to be maximum at a water activity in the range of 0.32-0.52.     

A novel support for the immobilization of lipase and the effects of the details of its preparation on the hydrolysis of triacylglycerides

Summary The lipase from Candida cylindracea was immobilized by its adsorption on the internal surface of hydrophobic microporous poly(styrene-divinylbenzene) supports prepared by the concentrated emulsion polymerization method. The prepared supports have a surface area of the order of 200 m²/g. The immobilized enzyme catalyst is used for the hydrolysis of triacylglycerides. The effects of the amounts of surfactant and divinylbenzene used in the preparation of the hydrophobic support on the adsorption capacity for lipase and on the activity of the immobilized lipase have been investigated. The activity of the immobilized enzyme per enzyme molecule can be higher than that of the free lipase.     

Poly(styrene-divinylbenzene) beads surface functionalized with di-block polymer grafting and multi-modal ligand attachment: performance of reversibly immobilized lipase in ester synthesis

Fibrous poly(styrene-b-glycidylmethacrylate) brushes were grafted on poly(styrene–divinylbenzene) (P(S–DVB)) beads using surface-initiated atom transfer radical polymerization. Tetraethyldiethylenetriamine (TEDETA) ligand was incorporated on P(GMA) block. The ligand attached beads were used for reversible immobilization of lipase. The influences of pH, ionic strength, and initial lipase concentration on the immobilization capacities of the beads have been investigated. Lipase adsorption capacity of the beads was about 78.1 mg/g beads at pH 6.0. The K _m value for immobilized lipase was about 2.1-fold higher than that of free enzyme. The thermal, and storage stability of the immobilized lipase also was increased compared to the native lipase. It was observed that the same support enzyme could be repeatedly used for immobilization of lipase after regeneration without significant loss in adsorption capacity or enzyme activity. A lipase from Mucor miehei immobilized on styrene–divinylbenzene copolymer was used to catalyze the direct esterification of butyl alcohol and butyric acid.     

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.     

Lipase hydration state in the gas phase: sorption isotherm measurements and inverse gas chromatography

The adsorption of water and substrate on immobilized Candida antarctica lipase B was studied by performing adsorption isotherm measurements and using inverse gas chromatography (IGC). Water adsorption isotherm of the immobilized enzyme showed singular profile absorption incompatible with the Brunauer-Emmet-Teller model, probably due to the hydrophobic nature of the support, leading to very low interactions with water. IGC allowed determining the evolution with water thermodynamic activity (a(W)) of both dispersive surface energies and acidity and basicity constants of immobilized enzyme. These results showed that water molecules progressively covered immobilized enzyme, when increasing a(W), leading to a saturation of polar groups above a(W) 0.1 and full coverage of the surface above a(W) 0.25. IGC also enabled relevant experiments to investigate the behavior of substrates under a(W) that they will experience, in a competitive situation with water. Results indicated that substrates had to displace water molecules in order to adsorb on the enzyme from a(W) values ranging from 0.1 to 0.2, depending on the substrate. As the conditions used for these adsorption studies resemble the ones of the continuous enzymatic solid/gas reactor, in which activity and selectivity of the lipase were extensively studied, it was possible to link adsorption results with particular effects of water on enzyme properties.     

Adsorption immobilization of alkaline lipase]

A polyamide with the covalently coupled phosphatidyl ethanolamine was used for affinity adsorption of an alkaline lipase from Pseudomonas aeruginosa. The immobilization resulted in increase of the enzyme specific activity. Some properties of native and adsorbed enzyme were compared. The temperature optima, heat and pH stability, KM and Vmax values were determined for both native and immobilized enzymes.     

Kinetics and stability of immobilized chicken liver xanthine dehydrogenase.

Xanthine dehydrogenase (EC 1.2.1.37) was isolated from chicken livers and immobilized by adsorption to a Sepharose derivative, prepared by reaction of n-octylamine with CNBr-activated Sepharose 4B. Using a crude preparation of enzyme for immobilization it was observed that relatively more activity was adsorbed than protein, but the yield of immobilized activity increased as a purer enzyme preparation was used. As more activity and protein were bound, relatively less immobilized activity was recovered. This effect was probably due to blocking of active xanthine dehydrogenase by protein impurities. The kinetics of free and immobilized xanthine dehydrogenase were studied in the pH range 7.5-9.1. The Km and V values estimated for free xanthine dehydrogenase increase as the pH increase; the K'm and V values for the immobilized enzyme go through a minimum at pH 8.1. By varying the amount of enzyme activity bound per unit volume of gel, it was shown that K'm is larger than Km are result of substrate diffusion limitation in the pores of the support material. Both free and immobilized xanthine dehydrogenase showed substrate activation at low concentrations (up to 2 microM xanthine). Immobilized xanthine dehydrogenase was more stable than the free enzyme during storage in the temperature range of 4-50 degrees C. The operational stability of immobilized xanthine dehydrogenase at 30 degrees C was two orders of magnitude smaller than the storage stability, t 1/2 was 9 and 800 hr, respectively. The operational stability was, however, better than than of immobilized milk xanthine oxidase (t 1/2 = 1 hr). In addition, the amount of product formed per unit initial activity in one half-life, was higher for immobilized xanthine dehydrogenase than for immobilized xanthine oxidase. Unless immobilized milk xanthine oxidase can be considerable stabilized, immobilized chicken liver xanthine dehydrogenase is more promising for application in organic synthesis.     

Evaluation of cellulose-binding domain fused to a lipase for the lipase immobilization

A cellulose-binding domain (CBD) fragment of a cellulase gene of Trichoderma hazianum was fused to a lipase gene of Bacillus stearothermophilus L1 to make a gene cluster for CBD-BSL lipase. The specific activity of CBD-BSL lipase for oil hydrolysis increased by 33% after being immobilized on Avicel (microcrystalline cellulose), whereas those of CBD-BSL lipase and BSL lipase decreased by 16% and 54%, respectively, after being immobilized on silica gel. Although the loss of activity of an enzyme immobilized by adsorption has been reported previously, the loss of activity of the CBD-BSL lipase immobilized on Avicel was less than 3% after 12 h due to the irreversible binding of CBD to Avicel.     

Co-immobilization of lipase, glycerol kinase, glycerol-3-phosphate oxidase and peroxidase onto alkylamine glass beads through glutaraldehyde coupling

A method for co-immobilizing lipase from porcine pancreas, glycerol kinase (GK) from Cellulomonas spp., glycerol-3-phosphate oxidase (GPO) from Aerococcus viridans and peroxidase from horseradish onto zirconia-coated alkylamine glass beads through glutaraldehyde coupling has been described. The co-immobilized enzymes retained 71.4% of initial specific activity with a conjugation yield of 43.6 mg/g support. The optimum pH and Km for triolein increased, while Vmax was decreased slightly, but incubation temperature for maximum activity remained unaltered after co-immobilization. The co-immobilized enzymes showed increased thermal and storage stabilities in cold, compared to their native form. Among the various metal salts tested, only CuSO4 caused inhibition of both free and co-immobilized enzymes. The co-immobilized enzymes showed better suitability over mixture of individually immobilized enzymes in determination of serum triglyceride.