Kinetics of lipase-catalyzed hydrolysis of palm oil in lecithin/izooctane reversed micelles

Candida rugosa lipase has been used to investigate the hydrolysis of palm oil in a lecithin/isooctane reversed micellar system. The reaction obeys Michaelis-Menten kinetics for the initial conditions. Kinetic parameters such as maximum rate and Michaelis constant (K _m) were determined for lipase-catalyzed hydrolysis in n-hexane and isooctane. According to the K _m values, the enzyme affinity towards the substrate was increased in isooctane. The maximum degree of hydrolysis was generally decreased as the initial substrate concentration was increased. This may suggest that the hydrolysis in lecithin reversed micelles should be regarded as a one-substrate first-order reversible reaction. It is shown in this study that the proposed one-substrate first-order kinetic model can serve for the precise prediction of the degree of hydrolysis for a known reaction time or vice versa, when the initial substrate concentration is less than 0.325 mol/dm³. A disagreement with this model was found when the initial substrate concentration was higher than approximately 0.3 mol/dm³. This may be due to the effects of the products on lipase activity or even to the conversion of the reversed micellar system to other systems. Received: 16 May 1997 / Received revision: 22 October 1997 / Accepted: 24 October 1997     

Activity of Pseudomonas cepacia lipase in organic media is greatly enhanced after immobilization on a polypropylene support

The purified lipase from Pseudomonas cepacia was used as free and immobilized enzyme preparation for hydrolysis of p-nitrophenyl palmitate (pNPP) and p-nitrophenyl acetate (pNPA) in organic media. The free enzyme was mixed with bovine serum albumin and lyophilized. Immobilization was on porous polypropylene. Conditions where diffusional limitations of the substrate were not limiting the reaction rate were defined. The specific activity of the lipase was greatly enhanced upon immobilization: 16.5- and 7.8-fold for pNPP and pNPA respectively. Both the free and immobilized lipases followed Michaelis–Menten kinetics in organic solvent despite the heterogeneity (solid/liquid) of the reaction mixture. For pNPP, the activation factor upon immobilization came mainly from a reduction in K _m, app while k _cat was increased for pNPA. Received: 30 January 1997 / Accepted: 14 February 1997     

Production of d-amino acids using immobilized d-hydantoinase from lentil, Lens esculenta, seeds

d-Hydantoinase from the lentil, Lens esculenta, seed is quite unstable, and has been immobilized on Diethyl amino ethyl (DEAE) cellulose by an adsorption and cross-linking method. The immboilized d-hydantoinase exhibited 80% enzyme activity and contained 86% protein. The immobilization of the enzyme preparation does not change its optimum pH, temperature or affinity constant, but increases its shelf-life, thermostability and stability in various organic solvents. This immobilized d-hydantoinase can be used effectively for the production of d-amino acids from the corresponding hydantoins and may therefore be of use in the chemical and pharmaceutical industries. Received: 28 April 1998 / Received last revision: 10 July 1998 / Accepted: 10 July 1998     

Properties of free and immobilised lipase from Burkholderia cepacia in organic media

The purified lipase from Burkholderia cepacia was immobilised on a porous polypropylene support and its biocatalytic properties were compared with those of the free enzyme in organic media. For both lipase preparations, the rate of p-nitrophenyl ester hydrolysis in n-heptane was not restricted by mass transfer limitations. The immobilisation changed neither the temperature at which the reaction rate was maximal, nor the activation energy of the reaction. The enzyme stability was slightly decreased (1.3-fold) upon immobilisation. Moreover, the immobilised enzyme displayed fewer variations of activity with fatty acid chain length. Interestingly, for all the different p-nitrophenyl esters used, the immobilised enzyme was more active (from 5.8- to 18.9-fold) than the free enzyme. Therefore, it would be very useful to use B. cepacia lipase immobilised onto porous polypropylene for applications in organic media, as it displayed high activities on a larger range of substrates. Received: 8 February 1999 / Received revision: 19 March 1999 / Accepted: 20 March 1999     

Purification, characterization and immobilization of an NADPH-dependent enzyme involved in the chiral specific reduction of the keto ester M, an intermediate in the synthesis of an anti-asthma drug, Montelukast, from Microbacterium campoquemadoensis (MB5614)

(S)(E)-2-{3-[3-[2-(7-chloro-2-quinolinyl)ethenyl]-phenyl]-3-hydroxypropyl} benzoic acid methyl ester,␣a key intermediate in the synthesis of the anti-asthma drug, Montelukast, was prepared from the corresponding ketone (keto ester M) by microbial transformation. The biotransforming organism, Microbacterium campoquemadoensis (MB5614), was discovered as a result of an extensive screening program and was used for the isolation and purification of the responsible enzyme. The enzyme is a soluble cytoplasmic protein which was purified as a complex with a low-molecular-mass molecule that had a visible-light absorption maximum at 460 nm. The purified enzyme has an apparent molecular mass of 60 kDa, when denatured, and is isolated in the native state as an oligomer. The isolated enzyme requires NADPH for its activity and reduces the keto ester M to the desired (S)-hydroxy ester with an enantiomeric excess greater than 95% at the optimum temperature of 30 °C and pH 8. The enzyme was immobilized on oxirane-activated acrylamide beads with some loss of activity, but it was fully active in a two-phase (water/hexane 25:75) solvent system, both as a free solution and in an immobilized form. Received: 31 October 1997 / Received revision: 8 January 1998 / Accepted: 24 January 1998     

Transformation of indole and quinoline by Desulfobacterium indolicum (DSM 3383)

Degradation of indole and quinoline by Desulfobacterium␣indolicum was studied in batch cultures. The first step in the degradation pathway of indole and quinoline was a hydroxylation at the 2 position to oxindole and 2-hydroxyquinoline respectively. These hydroxylation reactions followed saturation kinetics. The kinetic parameters for indole were an apparent maximum specific transformation rate (V _Amax) of 263 μmol mg total protein⁻¹ day⁻¹ and an apparent half-saturation constant (K _Am) of 139 μM. The V _Amax for quinoline was 170 μmol mg total protein⁻¹ day⁻¹ and K _Am was 92 μM. Oxindole inhibited indole hydroxylation whereas 2-hydroxyquinoline stimulated quinoline hydroxylation. An adaptation period of approximately 20 days was required before transformation of 2-hydroxyquinoline in cultures previously grown on quinoline. Indole and quinoline were hydroxylated with a lag phase shorter than 4 h in a culture adapted to ethanol. Chloramphenicol inhibited the hydroxylation of indole and quinoline in ethanol-adapted cells, indicating an inducible enzyme system. Chloramphenicol had no effect on the hydroxylation of indole in quinoline-adapted cells or on the hydroxylation of quinoline in indole-adapted cells. This indicated that it was the same inducible enzyme system that hydroxylated indole and quinoline. Received: 16 July 1996 / Received revision: 23 September 1996 / Accepted: 29 September 1996     

Immobilization of Candida rugosa lipase on sporopollenin from Lycopodium clavatum

Sporopollenin is a natural polymer obtained from Lycopodium clavatum, which is highly stable with constant chemical structure and has high resistant capacity to chemical attack. In this study, immobilization of lipase from Candida rugosa (CRL) on sporopollenin by adsorption method is reported for the first time. Besides this, the enzyme adsorption capacity, activity and thermal stability of immobilized enzyme have also been investigated. It has been observed that under the optimum conditions (Spo-E_(0.3)), the specific activity of the immobilized lipase on the sporopollenin by adsorption was 16.3 U/mg protein, which is 0.46 times less than that of the free lipase (35.6 U/mg protein). The pH and temperature of immobilized enzyme were optimized, which were 6.0 and 40 °C respectively. Kinetic parameters V_max and K_m were also determined for the immobilized lipase. It was observed that there is an increase of the K_m value (7.54 mM) and a decrease of the V_max value (145.0 U/mg-protein) comparing with that of the free lipase.     

Immobilization and characterisation of a lipase from a new source, Bacillus sp. ITP-001

A new source of lipase from Bacillus sp. ITP-001 was immobilized by physical adsorption on the polymer poly(3-hydroxybutyrate-co-hydroxyvalerate) (PHBV) in aqueous solution. The support and immobilized lipase were characterised, compared to the lyophilised lipase, with regard to the specific surface area, adsorption–desorption isotherms, pore volume (Vp) and size (dp) by nitrogen adsorption, differential scanning calorimetry, thermogravimetric analysis, chemical composition analysis, Fourier transform infrared spectroscopy and biochemical properties. The immobilized enzyme displayed a shift in optimum pH towards the acidic side with an optimum at pH 4.0, whereas the optimum pH for the free enzyme was at pH 7.0; the optimum temperature of activity was 80 and 37 °C for the free and immobilized enzyme, respectively. The inactivation rate constant for the immobilized enzyme at 37 °C was 0.0038 h^?1 and the half-life was 182.41 h. The kinetic parameters obtained for the immobilized enzyme gave a Michaelis–Menten constant (K _m) of 49.10 mM and a maximum reaction velocity (V _max) of 205.03 U/g. Furthermore, the reuse of the lipase immobilized by adsorption allowed us to observe that it could be reused for 10 successive cycles, duration of each cycle (1 h), maintaining 33 % of the initial activity.     

Cloning and expression of a gene encoding cyanidase from Pseudomonas stutzeri AK61

The gene coding for cyanidase, which catalyzes the hydrolysis of cyanide to formate and ammonia, was cloned from chromosomal DNA of Pseudomonas stutzeri AK61 into Escherichia coli. The cyanidase gene consisted of an open reading frame of 1004 bp, and it was predicted that cyanidase was composed of 334 amino acids with a calculated molecular mass of 37 518 Da. The amino acid sequence of cyanidase showed a 35.1% and 26.4% homology to aliphatic nitrilase from Rhodococcus rhodochrous K22 and cyanide hydratase from Fusarium lateritium, respectively. A unique cysteine residue of aliphatic nitrilase, which was suggested to play an essential role in the catalytic activity, was conserved in cyanidase. The active form of cyanidase was successfully expressed by a DNA clone containing the cyanidase gene in E.coli. Its productivity was approximately 230 times larger than that of P. stutzeri AK61. The characteristics of the expressed cyanidase, including optimum pH, optimum temperature, Michaelis constant (K _m) for cyanide and specific activity, were similar to those of the native enzyme from P. stutzeri AK61. Received: 24 October 1997 / Received last revision: 17 March 1998 / Accepted: 20 March 1998     

α-Chymotrypsin immobilized on ferromagnetic particles coated with titanium oxide: Production and catalytic characterization

Immobilization of α-chymotrypsin on magnetic particles with stable coat with titanium oxides as a main constituent allowed the biocatalytic system to be quickly and qualitatively separated into the components after completion of the enzymatic reaction. X-ray phase analysis demonstrated that the coat of magnetic particles is composed mainly of titanium dioxide in brookite modification. The maximal capacity of the particles amounted to 0.3 mg protein/mg particles. It was demonstrated that the reaction catalyzed by immobilized α-chymotrypsin proceeds in a kinetic mechanism due to a high dispersion of the ferromagnetic particles. The catalytic constant (25 s⁻¹) andK _M (0.17 mM) for the immobilized enzyme for the hydrolysis of N-acetyl-L-tyrosine ethyl ester are comparable to the corresponding characteristics for the free enzyme.     

Possible Involvement of Cysteine and Histidine Residues in the (NH4 + + Na+)-Activated ATPase of an Anaerobic Alkaliphile, Amphibacillus xylanus

Effect of various inhibitors on the (NH₄ ⁺ + Na⁺)-activated ATPase of an anaerobic alkaliphile, Ep01(a strain of Amphibacillus xylanus), was examined. Among the chemicals tested, the enzyme was drastically inactivated by p-chloromercuribenzoic acid and diethyl pyrocarbonate. The ATPase activity of the enzyme, which was inactivated by p-chloromercuribenzoic acid and diethyl pyrocarbonate, was remarkably restored by β-mercaptoethanol and hydroxylamine, respectively, suggesting the involvement of cysteine and histidine residues in the enzyme activity. Analysis of the inhibition kinetics by diethyl pyrocarbonate indicated that modification of a single histidine residue per ATPase molecule was sufficient to inactivate the enzyme. Received: 2 June 1997 / Accepted: 7 July 1997     

Silanized palygorskite for lipase immobilization

Lipase from Candida lipolytica has been immobilized on 3-aminopropyltriethoxysilane-modified palygorskite support. Scanning electron micrographs proved the covalently immobilization of C. lipolytica lipase on the palygorskite support through glutaraldehyde. Using an optimized immobilization protocol, a high activity of 3300 U/g immobilized lipase was obtained. Immobilized lipase retained activity over wider ranges of temperature and pH than those of the free enzyme. The optimum pH of the immobilized lipase was at pH 7.0–8.0, while the optimum pH of free lipase was at 7.0. The retained activity of the immobilized enzyme was improved both at lower and higher pH in comparison to the free enzyme. The immobilized enzyme retained more than 70% activity at 40 °C, while the free enzyme retained only 30% activity. The immobilization stabilized the enzyme with 81% retention of activity after 10 weeks at 30 °C whereas most of the free enzyme was inactive after a week. The immobilized enzyme retains high activity after eight cycles. The kinetic constants of the immobilized and free lipase were also determined. The K_m and V_max values of immobilized lipase were 0.0117 mg/ml and 4.51 μmol/(mg min), respectively.     

Production and properties of a dextransucrase from Leuconostoc mesenteroides IBT-PQ isolated from ‘pulque’, a traditional Aztec alcoholic beverage

Dextransucrase was produced from a Leuconostoc mesenteroides isolated from pulque, a traditional Aztec alcoholic beverage produced from agave juice containing sucrose as the main carbon source. Almost all the dextransucrase activity (87%) was associated with the cells, and was unusually high (1.04 U mg⁻¹ of cells). The culture medium composition was optimized through a Box-Behnken method resulting in a process yielding 2.2 U ml⁻¹ of insoluble glucosyltransferase activity. The enzyme had a molecular weight of 166 kDa. Optimal temperature was 35°C with a half-life of 137 min at the same temperature. As with dextransucrase from the industrial strain L. mesenteroides NRRL B-512F, the enzyme showed Michaelis–Menten kinetic behavior with excess substrate inhibition (K _m and K _i values of 0.026 M and 1.23 M respectively); produced soluble linear dextran with glucose molecules linked mainly in α(1–6) with branching in α(1–3) in a proportion of 4:1 as shown by NMR studies; and produced a high yield of isomalto-oligosaccharides in the presence of maltose. Received 4 February 1998/ Accepted in revised form 25 July 1998     

Cometabolic biodegradation of methyl t-butyl ether by Pseudomonas aeruginosa grown on pentane

A bacterial strain identified as Pseudomonas aeruginosa was isolated from a soil consortium able to mineralize pentane. P. aeruginosa could metabolize methyl t-butyl ether (MTBE) in the presence of pentane as the sole carbon and energy source. The carbon balance for this strain, grown on pentane, was established in order to determine the fate of pentane and the growth yield (0.9 g biomass/g pentane). An inhibition model for P. aeruginosa grown on pentane was proposed. Pentane had an inhibitory effect on growth of P. aeruginosa, even at a concentration as low as 85 μg/l. This resulted in the calculation of the following kinetic parameters (μ_max = 0.19 h⁻¹, K _s = 2.9 μg/l, K _i = 3.5 mg/l). Finally a simple model of MTBE degradation was derived in order to predict the quantity of MTBE able to be degraded in batch culture in the presence of pentane. This model depends only on two parameters: the concentrations of pentane and MTBE. Received: 16 July 1998 / Received revision: 11 November 1998 / Accepted 31 November 1998     

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.     

Purification and properties of a thermoactive and thermostable pullulanase from Thermococcushydrothermalis, a hyperthermophilic archaeon isolated from a deep-sea hydrothermal vent

The extremely thermophilic archaeon Thermococcus hydrothermalis, isolated from a deep-sea hydrothermal vent in the East Pacific Rise at 21°N, produced an extracellular pullulanase. This enzyme was purified 97-fold to homogeneity from cell-free culture supernatant. The purified pullulanase was composed of a single polypeptide chain having an estimated molecular mass of 110 kDa (gel filtration) or 128 kDa (sodium dodecyl sulfate/polyacryl amide gel electrophoresis). The enzyme showed optimum activity at pH 5.5 and 95 °C. The thermostability and the thermoactivity were considerably increased in the presence of Ca²⁺. The enzyme was activated by 2-mercaptoethanol and dithiothreitol, whereas N-bromosuccinimide and α-cyclodextrin were inhibitors. This enzyme was able to hydrolyze, in addition to the α-1,6-glucosidic linkages in pullulan, α-1,4-glucosidic linkages in amylose and soluble starch, and can therefore be classified as a type II pullulanase or an amylopullulanase. The purified enzyme displayed Michaelis constant (K _m) values of 0.95 mg/ml for pullulan and 3.55 mg/ml for soluble starch without calcium and, in the presence of Ca²⁺, 0.25 mg/ml for pullulan and 1.45 mg/ml for soluble starch. Received: 19 November 1997 / Received revision: 9 March 1998 / Accepted: 14 March 1998     

Substrate selectivity of various lipases in the esterification of cis- and trans-9-octadecenoic acid

The substrate selectivity of numerous commercially available lipases from microorganisms, plants and animal tissue towards 9-octadecenoic acids with respect to the cis/trans configuration of the CC double bond was examined by the esterification of cis- and trans-9-octadecanoic acid (oleic and elaidic acid respectively) with n-butanol in n-hexane. A great number of lipases studied, e.g. those from Pseudomonas sp., porcine pancreas or Carica papaya, were unable to discriminate between the isomeric 9-octadecenoic acids. However, lipases from Candida cylindracea and Mucor miehei catalysed the esterification of oleic acid 3–4 times faster than the corresponding reaction of elaidic acid and therefore have a high preference for the cis isomer. Of all biocatalysts examined, only recombinant lipases from Candidaantarctica favoured elaidic acid as substrate. While the preference of Candida antarctica lipase B for the trans isomer was quite low, Candida antarctica lipase A had an extraordinary substrate selectivity and its immobilized enzyme preparation [Chirazyme L-5 (3) from Boehringer] esterified elaidic acid about 15 times faster than oleic acid. Received: 29 October 1998 / Received revision: 18 December 1998 / Accepted: 21 December 1998     

Kinetic models for phycocyanin production by high cell density mixotrophic culture of the microalga Spirulina platensis

Phycocyanin production by high cell density cultivation of Spirulina platensis in batch and fed-batch modes in 3.7-L bioreactors with a programmed stepwise increase in light intensity program was investigated. The results showed that the cell density in fed-batch culture (10.2 g L⁻¹) was 4.29-fold that in batch culture (2.38 g L⁻¹), and the total phycocyanin production in the fed-batch culture (0.795 g L⁻¹) was 3.05-fold that in the batch culture (0.261 g L⁻¹). An unstructured kinetic model to describe the microalga culture system including cell growth, phycocyanin formation, as well as glucose consumption was proposed. The data fitted the models well (r ² > 0.99). Furthermore, based on the kinetic models, the potential effects of light limitation and photoinhibition on cell growth and phycocyanin formation can be examined in depth. The models demonstrated that the optimal light intensity for mixotrophic growth of Spirulina platensis in batch or fed-batch cultures using a 3.7-L bioreactor was 80160 μE m⁻² s⁻¹, and the stepwise increase in light intensity can be replaced by a constant light intensity mode. Received 28 July 1998/ Accepted in revised form 8 October 1998     

High alcohol production by repeated batch fermentation using an immobilized osmotolerant Saccharomyces cerevisiae

A repeated batch fermentation system was used to produce ethanol using an osmotolerant Saccharomyces cerevisiae (VS₃) immobilized in calcium alginate beads. For comparison free cells were also used to produce ethanol by repeated batch fermentation. Fermentation was carried for six cycles with 125, 250 or 500 beads using 150, 200 or 250 g glucose L⁻¹ at 30°C. The maximum amount of ethanol produced by immobilized VS₃ using 150 g L⁻¹ glucose was only 44 g L⁻¹ after 48 h, while the amount of ethanol produced by free cells in the first cycle was 72 g L⁻¹. However in subsequent fed batch cultures more ethanol was produced by immobilized cells compared to free cells. The amount of ethanol produced by free cells decreased from 72 g L⁻¹ to 25 g L⁻¹ after the fourth cycle, while that of immobilized cells increased from 44 to 72 g L⁻¹. The maximum amount of ethanol produced by immobilized VS₃ cells using 150, 200 and 250 g glucose L⁻¹ was 72.5, 93 and 87 g ethanol L⁻¹ at 30°C. Journal of Industrial Microbiology & Biotechnology (2000) 24, 222–226. Received 16 September 1999/ Accepted in revised form 22 December 1999     

A novel method for characterisation of microbial growth kinetics on volatile organic compounds

A novel method for the determination of microbial growth kinetics on hydrophobic volatile organic compounds (VOC) has been developed. A stirred tank reactor was operated as a fed-batch system to which the VOC was continuously fed via the gas phase, assuring a constant VOC concentration in the mineral medium. A flow of air was saturated with the VOC, and then mixed with a further flow of air, to obtain a predetermined VOC concentration. Thus, different VOC concentrations in the mineral medium could be obtained by altering the VOC concentration in the feed gas. The growth kinetics of Xanthobacter autotrophicus GJ10 on 1,2-dichloroethane (DCE) and of Pseudomonas sp. strain JS150 on MonoChloroBenzene (MCB) were assessed using this method. The growth of strain JS150 was strongly inhibited at MCB concentrations higher than 160 mg l⁻¹, and the results were fitted using a piecewise function. The growth kinetics of strain GJ10 were described by the Luong model where maximum growth rate μ_max = 0.12 h⁻¹, substrate saturation constant K _S = 7.8 mg l⁻¹, and maximum substrate concentration S _m (above which growth is completely inhibited) = 1080 mg l⁻¹. Varying nitrogen and oxygen flows enabled the effect of oxygen concentration on the growth kinetics of Pseudomonas JS150 to be determined. Received: 30 November 1998 / Received revision: 19 March 1999 / Accepted: 20 March 1999