Nucleation and growth of microbial lipase crystals from clarified concentrated fermentation broths

Bulk crystallization is emerging as a new industrial operation for protein recovery. Characterization of bulk protein crystallization is more complex than protein crystallization for structural study where single crystals are grown in flow cells. This is because both nucleation and crystal growth processes are taking place while the supersaturation falls. An algorithm is presented to characterize crystallization using the rates of the two kinetic processes, nucleation and growth. The values of these rates allow ready comparison of the crystallization process under different operating conditions. The crystallization, via adjustment to the isoelectric pH of a fungal lipase from clarified fermentation broth, is described for a batch stirred reactor. A maximum nucleation rate of five to six crystals formed per microliter of suspension per second and a high power dependency ( approximately 11) on the degree of supersaturation were found. The suspended protein crystals were found to grow at a rate of up to 15-20 nm/s and also to exhibit a high power dependency ( approximately 6) of growth rate on the degree of supersaturation.     

Lipase from marine Aspergillus awamori BTMFW032: production, partial purification and application in oil effluent treatment

Marine fungus BTMFW032, isolated from seawater and identified as Aspergillus awamori, was observed to produce an extracellular lipase, which could reduce 92% fat and oil content in the effluent laden with oil. In this study, medium for lipase production under submerged fermentation was optimized statistically employing response surface method toward maximal enzyme production. Medium with soyabean meal-0.77% (w/v); (NH(4))(2)SO(4)-0.1m; KH(2)PO(4)-0.05 m; rice bran oil-2% (v/v); CaCl(2)-0.05 m; PEG 6000-0.05% (w/v); NaCl-1% (w/v); inoculum-1% (v/v); pH 3.0; incubation temperature 35°C and incubation period-five days were identified as optimal conditions for maximal lipase production. The time course experiment under optimized condition, after statistical modeling, indicated that enzyme production commenced after 36 hours of incubation and reached a maximum after 96 hours (495.0 U/ml), whereas maximal specific activity of enzyme was recorded at 108 hours (1164.63 U/mg protein). After optimization an overall 4.6-fold increase in lipase production was achieved. Partial purification by (NH(4))(2)SO(4) precipitation and ion exchange chromatography resulted in 33.7% final yield. The lipase was noted to have a molecular mass of 90 kDa and optimal activity at pH 7 and 40°C. Results indicated the scope for potential application of this marine fungal lipase in bioremediation.     

Production of a Pseudomonas lipase in n-alkane substrate and its isolation using an improved ammonium sulfate precipitation technique

Among the various lipidic and non-lipidic substances, normal alkanes within the chain lengths of C-12 to C-20 served as the best carbon substrates for the production of extracellular lipase by Pseudomonas species G6. Maximum lipase production of 25 U/ml of the culture broth was obtained by using n-hexadecane as the sole carbon substrate. The optimum pH of 8 and temperature of 34 + 1 degrees C were demonstrated for the production of lipase in n-hexadecane substrate. The optimum concentration of iron, which played a critical role on the lipase production, was found to be 0.25 mg/l. Lipase production could be enhanced to nearly 2.4-fold by using tributyrin at a concentration of 0.05% (v/v) in the culture medium. High recovery of the lipase protein (83%) from the culture broth was achieved by treating the culture supernatant with Silicone 21 Defoamer followed by ammonium sulfate (60% saturation) fractionation.     

Mechanical stability of immobilized biocatalysts (CLECs) in dilute agitated suspensions

Cross-linked enzyme crystals (CLECs) are a novel form of immobilized biocatalyst designed for application in industrial biotransformation processes. In this work we have investigated the mechanical stability of agitated CLEC suspensions in relation to the design and scale-up of bioconversions carried out in stirred-tank reactors. By careful control of the crystallization conditions yeast alcohol dehydrogenase I (YADHI) microcrystals of different size were first prepared having either an hexagonal (approximately 12 microm) or rod-shaped (approximately 4.6 microm) morphology. These were then cross-linked with glutaraldehyde to form CLECs. The rate of breakage of the CLEC suspensions was subsequently measured in a rotating disk shear device (total volume, 11 mL) by monitoring the change in crystal size distribution with time. This device is designed to mimic the shear and energy dissipation rates found in a range of process scale equipment and may be used to study the mechanical stability of any immobilized biocatalyst preparation. Experiments were performed as a function of the speed and duration of disk rotation, CLEC concentration (0.26-2.5 mg.mL(-1)) and energy dissipation rate (2.2 x 10(3) to 6.8 x 10(5) W.kg(-1)). No breakage of the rod-shaped CLECs was observed over the entire range of experimental conditions investigated. Breakage of the larger hexagonal-shaped CLECs did occur, however, at energy dissipation rates, epsilon(max), above 1.0 x 10(5) W.kg(-1), where the calculated length scale of turbulence was around 2.0 microm. Based on visual observation of the sheared CLEC suspensions and models of crystal breakage, it was concluded that breakage of the hexagonal-shaped CLECs occurred due to shear induced attrition. Measurement of the catalytic activity of both the hexagonal and rod-shaped CLECs showed no significant change in activity before and after shearing.     

Crystallization and preliminary X-ray study of horse pancreatic lipase

Horse (Equus caballus) pancreatic lipase (EC 3.1.1.3) has been crystallized using the hanging drop method of vapour diffusion at 20 degrees C. The best crystals were grown from an 8 mg/ml solution in 10 to 20% (w/v) polyethylene glycol 8000, 10 mM-MgCl2, 0.1 M-NaCl, 0.1 M-Mes buffer (pH 5.6). They reach dimensions of 0.8 mm x 0.4 mm x 0.6 mm. X-ray examination of the lipase crystals shows that they are orthorombic with a space group P2(1)2(1)2(1). Their cell dimensions are a = 79.8 A, b = 97.2 A c = 145.3 A. Two molecules per asymmetric unit give a Vm value of 2.82 A3/dalton (56% water content). Lipase crystals strongly diffract to at least 1.8 A resolution. Some molecular properties of horse lipase compared to those of the better-known porcine enzyme are also presented.     

Studies on Crystalline Growth of MoFe Protein from a nifZ Deleted Strain of Azotobacter vinelandii

Under a given condition of crystallization, dark brown short rhombohedron crystals could be obtained from ΔnifZ MoFe protein purified from a nifZ deleted mutant strain of Azotobacter vinelandii Lipmann. Systematic studies on the effect of concentrations of PEG 8000,MgCl2, NaCl,Tris and buffer pH on the crystallization and crystal growth of the protein showed that the protein could not be crystallized in lower concentrations of the chemicals and lower buffer pH. A large amount of smaller crystals of the protein appeared in a week with gradual increasing in the chemical concentrations and pH≥8.0. When the chemical concentrations were further increased, the time for crystallization was increased and a few high grade crystals of larger size were formed. If the concentrations of the chemicals were continuously increased, many crystals with smaller size, and, sometimes of poor quality appeared again and eventually ceased to produce any crystals. The optimal concentration for each of the above mentioned chemicals varies with other variable factors. Only one bigger crystal (both of the longest two sides: 0.16 mm) could be obtained in a hanging drop of protein sample when the concentrations of PEG 8000, MgCl2, NaCl,Tris and protein were kept at 1.86%, 300 mmol/L, 400 mmol/L, 53 mmol/L and 4.64 g/L , respectively, with Tris buffer pH 8.2.     

Protein purification by bulk crystallization: the recovery of ovalbumin

Crystallization is used industrially for the recovery and purification of many inorganic and organic materials. However, very little is reported on the application of bulk crystallization for proteins. In this work, ovalbumin was selected as a model protein to investigate the feasibility of using bulk crystallization for the recovery and purification of proteins. A stirred 1-L seeded batch crystallizer was used to obtain the crystal growth kinetics of ovalbumin in ammonium sulfate solutions at 30 degrees C. The width of the metastable region, in which crystal growth can occur without any nucleation, is equivalent to a relative supersaturation of about 20. The bulk crystallizations were undertaken within this range (using initial relative supersaturations less than 10) and nucleation was not observed. The ovalbumin concentration in solution was measured by UV absorbance and checked by crystal content measurement. Crystal size distributions were measured both by using a Malvern Mastersizer and by counting crystals through a microscope. The crystal growth rate was found to have a second-order dependence upon the ovalbumin supersaturation. While there is no discernible effect of ammonium sulfate concentration at pH 4.90, there is a slight effect at higher pH values. Overall the effect of ammonium sulfate concentration is small compared to the effect of pH, for which there is a 10-fold increase in the growth rate constant, k(Gsigma) over the range pH 4.6-5.4. To demonstrate the degree of purification which can be achieved by bulk crystallization, ovalbumin was crystallized from a solution containing conalbumin (80,000 Da) and lysozyme (14, 600 Da). After one crystallization and a crystal wash, ovalbumin crystals were produced with a protein purity greater than 99%. No contamination by the other proteins was observed when using overloaded sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) stained with Coomassie blue stain and only trace amounts of lysozyme were observed using a silver stain. The presence of these other proteins in solution did not effect the crystal growth rate constant, k(Gsigma). The study demonstrates the feasibility of using bulk crystallization for the recovery and purification of ovalbumin. It should be readily applicable to other protein systems. (c) 1995 John Wiley & Sons, Inc.     

Performance of cross-linked enzyme crystals of engineered halohydrin dehalogenase HheG in different chemical reactor systems

Halohydrin dehalogenase HheG is an industrially interesting biocatalyst for the preparation of different β-substituted alcohols starting from bulky internal epoxides. We previously demonstrated that the immobilization of different HheG variants in the form of cross-linked enzyme crystals (CLECs) yielded stable and reusable enzyme immobilizes with increased resistance regarding temperature, pH, and the presence of organic solvents. Now, to further establish their preparative applicability, HheG D114C CLECs cross-linked with bis-maleimidoethane have been successfully produced on a larger scale using a stirred crystallization approach, and their application in different chemical reactor types (stirred tank reactor, fluidized bed reactor, and packed bed reactor) was systematically studied and compared for the ring opening of cyclohexene oxide with azide. This revealed the highest obtained space-time yield of 23.9 kg_product g_CLEC⁻¹ h⁻¹ L_{reactor volume}⁻¹ along with the highest achieved product enantiomeric excess [64%] for application in a packed-bed reactor. Additionally, lyophilization of those CLECs yielded a storage-stable HheG preparation that still retained 67% of initial activity (after lyophilization) after 6 months of storage at room temperature.     

Interaction of ribonuclease A with aqueous 2-methyl-2,4-pentanediol at pH 5.8.

The interactions between ribonuclease A and solvent components in aqueous 2-methyl-2,4-pentanediol (MPD) have been investigated by differential refractometry and light scattering at pH 5.8, i.e., conditions similar to those used to crystallize the protein from this solvent system. Application of multicomponent thermodynamic theory shows that, at all solvent compositions up to 50% (v/v) MPD, the protein is preferentially hydrated; i.e., addition of ribonuclease to the mixed solvent leads to an increase in the chemical potential of MPD. This unfavorable thermodynamic interaction leads to phase separation, probably caused by local salting out of the MPD by the charges on the surface of the protein molecule. A parallel examination by circular dichroism (CD) has shown that the CD spectrum of ribonuclease in 50% MPD is indistinguishable from that in dilute buffer.     

Crystallization of Ca2+-ATPase in detergent-solubilized sarcoplasmic reticulum

Microcrystalline arrays of Ca2+-transporting ATPase (EC 3.6.1.38) develop in detergent-solubilized sarcoplasmic reticulum upon exposure to 10-20 mM CaCl2 at pH 6.0 for several weeks at 2 degrees C, in a crystallization medium that preserves the ATPase activity for several months. Of 48 detergents tested, optimal crystallization was obtained with Brij 36T, Brij 56, and Brij 96 at a detergent:protein weight ratio of 4:1 and with octaethylene glycol dodecyl ether at a ratio of 2:1. Similar Ca2+-induced crystalline arrays were obtained with the purified or delipidated Ca2+-ATPase of sarcoplasmic reticulum but at lower detergent:protein ratios. The crystals are stabilized by fixation with glutaraldehyde and persist even after the removal of phospholipids by treatment with phospholipases A or C and by extraction with organic solvents. The crystals obtained so far can be used only for electron microscopy, but ongoing experiments suggest that under similar conditions large ordered arrays may develop that are suitable for x-ray diffraction analysis.     

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.     

诱变选育脂肪酶高产菌株及其脂肪酶固定化

以紫外和微波复合诱变选育脂肪酶产生菌 Rhizopus sp. RXF12,获得高产突变株RZ13,其脂肪酶摇瓶发酵单位是出发株的2.62倍。菌株经多次传代,遗传性状稳定。对RZ13菌株的发酵条件进行了正交优化,在25 ℃、pH 8.0的条件下,接入5 %(v/v)的RZ13菌株单孢子悬液 (107个/ml) 振荡培养84 h,达到RZ13菌株最佳产酶状态,脂肪酶活可达95.08 U/ml。考察了脂肪酶性质,在低于40 ℃,pH 7.0~9.0范围内脂肪酶活稳定。经载体筛选及固定化过程优化,选用镁铝水滑石25℃吸附4 h,对RZ13脂肪酶进行了固定化。结果表明,固定化酶的最适作用温度为35~55℃,pH为7.5~9.0,较游离酶的均有较大扩展。     

Instrumental assay of microbial lipase at constant pH

A rapid, accurate method with high sensitivity and reproducibility, and having the advantage of a short incubation period under constant pH, has been developed for routine measurement of microbial lipase. Assembled from readily available and economical instrumental components, the apparatus includes a pH meter, a thermoelectric heating and stirring device, a motor-driven burette, and an automatic recorder. The reaction mixture, consisting of 5 ml of a 10% olive oil-gum arabic emulsion, 2 ml of 3 m NaCl, 2 ml of sodium taurocholate (15 mg/ml) of 0.075 m CaCl(2), 5 ml of water, and 1 ml of enzyme solution, was adjusted to pH 8.0 and 37 C. The pH was maintained at a constant value by automatic addition of 0.01 n NaOH during the incubation period, which usually lasted 5 min. A lipase unit, derived from the use of this technique, may be defined as the number of microequivalents of acid liberated per minute under the specified conditions. The method was sensitive to 0.01 units. Various organisms tested produced 0.17 to 1.32 units per ml of the cell filtrate. An Arrhenius plot for staphylococcal lipase yielded 14,500 cal for function A (energy of activation).     

Stability and activity of cross-linking enzyme crystals of cyclodextrin glucanotransferase isolated from Bacillus macerans

Recently, a new technique using cross-linking enzyme crystals (CLECs) was introduced in the field of enzyme technology. CLECs are solid crystalline particles which are insoluble in both water and organic solvents. Chemical cross-linking of the enzyme crystals preserves the catalytic activity even in harsh conditions such as at high temperature, at extreme pH, in organic solvents, and in the presence of proteases and radical chemicals. CLECs of cyclodextrin glucanotransferase (CGTase) could be useful biocatalysts because they were stable at elevated temperature, in organic solvents, and in the presence of enzyme inactivation surfactant. They also maintained their activity against protein-digesting enzyme.     

Expression, purification, and aggregation studies of His-tagged thermoalkalophilic lipase from Bacillus thermocatenulatus

The His-tagged lipase BTL2 from Bacillus thermocatenulatus was expressed in Escherichia coli and purified to homogeneity by a simple, one-step purification protocol using immobilized metal affinity chromatography. The success of protein separation and purification was pH-dependent and increased with decreasing pH. The purified BTL2 lipase showed a strong tendency to aggregate upon concentration, which prevented a reproducible crystallization. Aggregation studies using dynamic light-scattering (DLS) analysis were performed to improve the purification and concentration of BTL2 lipase. Different chemical classes of additives were tested to manipulate the aggregation behaviour of BTL2 lipase with the aim of obtaining a monodisperse sample to use for crystallization. For the process of concentration of BTL2 lipase in monomeric form, the alcohol 2-propanol and the ionic detergent dodecyl dimethylamine-N-oxide (LDAO) were found to be necessary. For the concentrated lipase, the availability of 5% 2-propanol was sufficient to hold the lipase in monomeric form and no additional detergent was needed.     

Effects of solutes on the formation of crystalline sheets of the Ca(2+)-ATPase in detergent-solubilized sarcoplasmic reticulum.

The Ca(2+)-ATPase crystals formed in detergent solubilized sarcoplasmic reticulum (SR) at 2 degrees C in a crystallization medium of 0.1 M KCl, 10 mM K-Mops (pH 6.0), 3 mM MgCl2, 3 mM NaN3, 5 mM DTT, 25 IU/ml Trasylol, 2 micrograms/ml 1,6-di-tert-butyl-p-cresol, 20% glycerol and 20 mM CaCl2 (J. Biol. Chem. 263, 5277 and 5287 (1988)) contain highly ordered sheets of ATPase molecules, that associate into large multilamellar stacks (greater than 100 layers). When the crystallization is performed in the same medium but in the presence of 40% glycerol at low temperature the stacking is reduced to 4-5 layers and the average diameter of the crystalline sheets is increased from less than 1 micron to 2-3 microns. Glycerol and low temperature presumably reduce stacking by interfering with the interactions between the hydrophilic headgroups of Ca(2+)-ATPase molecules in adjacent lamellae, while not affecting or promoting the ordering of ATPase molecules within the individual sheets. Electron diffraction patterns could be regularly obtained at 8 A and occasionally at 7 A resolution on crystals formed in 40% glycerol, either at 2 degrees C or at -70 degrees C. In the same media but in the absence of glycerol, polyethyleneglycol 1450, 3000 and 8000 (1-8%) induced the formation of ordered crystalline arrays containing 10-12 layers that were similar to those obtained in 40% glycerol. Replacement of 40% glycerol with 10-50% glucose or supplementation of the standard crystallization medium with polyethyleneglycol (PEG 3000 or 8000; 1, 2, 5 and 8%) had no beneficial effect on the order of crystalline arrays compared with media containing 40% glycerol.     

Optimization of medium for lipase production by Acinetobacter haemolyticus from healthy human skin

A lipase producing Acinetobacter haemolyticus TA106 was isolated from healthy human skin of tribal population. The maximum activity of 55 U/ml was observed after medium optimization using the "one variable at a time" and the statistical approaches. The optimal composition of the medium was determined as (% w/v or v/v): tryptone--1, yeast extract--0.5, sodium chloride-1, olive oil-1, Tween-80 1, manganese sulphate--5 mM, sucrose--1, pH-7. It was found that maximum production occurred in late log phase, i.e., after 72 h and at 200 rpm. From factorial design and statistical analysis, it was found that pH, temperature, salt, inoculum density and aeration significantly affected the lipase production. It was also noted that inoculum density of 3% (v/v), sucrose (1% w/v) and manganese sulphate (5 mM) displayed maximum lipase activity of 55 U/ml by conventional as well as statistical method. Optimization studies also indicated the increase in specific activity from 0.2 U/mg to 6.7 U/mg.     

Effects of pH on protein-protein interactions and implications for protein phase behavior

The effects of pH on protein interactions and protein phase behavior were investigated by measuring the reduced second osmotic virial coefficient (b2) for ovalbumin and catalase, and the aggregate and crystal solubilities for ovalbumin, beta-lactoglobulin A and B, ribonuclease A and lysozyme. The b2 trends observed for ovalbumin and catalase show that protein interactions become increasingly attractive with decreasing pH. This trend is in good agreement with ovalbumin phase behavior, which was observed to evolve progressively with decreasing pH, leading to formation of amorphous aggregates instead of gel bead-like aggregates, and spherulites instead of needle-like crystals. For both acidic and basic proteins, the aggregate solubility during protein salting-out decreased with decreasing pH, and contrary to what is commonly believed, neither aggregate nor crystal solubility had a minimum at the isoelectric point. beta-Lactoglobulin B was the only protein investigated to show salting-in behavior, and crystals were obtained at low salt concentrations in the vicinity of its isoelectric point. The physical origin of the different trends observed during protein salting-in and salting-out is discussed, and the implications for protein crystallization are emphasized.     

Electron microscope observations on Ca2+-ATPase microcrystals in detergent-solubilized sarcoplasmic reticulum

Crystalline arrays of Ca2+-ATPase molecules develop in detergent-solubilized sarcoplasmic reticulum during incubation for several weeks at 2 degrees C under nitrogen in a medium of 0.1 M KCl, 10 mM K-3-(N-morpholino)propanesulfonate, pH 6.0, 3 mM MgCl2, 20 mM CaCl2, 20% glycerol, 3 mM NaN3, 5 mM dithiothreitol, 25 IU/ml Trasylol, 2 micrograms/ml 1,6-di-tert-butyl-p-cresol, 2 mg/ml protein, and 2-4 mg of detergent/mg of protein. Electron microscopy of sectioned, negatively stained, freeze-fractured, and frozen-hydrated Ca2+-ATPase crystals indicates that they consist of stacked lamellar arrays of Ca2+-ATPase molecules. Prominent periodicities of ATPase molecules within the lamellae arise from a centered rectangular lattice of dimensions 164 x 55.5 A. The association of lamellae into three-dimensional stacks is assumed to involve interactions between the exposed hydrophilic headgroups of ATPase molecules, that is promoted by glycerol and 20 mM Ca2+. Similar Ca2+-induced crystals were observed with purified or purified and delipidated Ca2+-ATPase preparations at lower detergent/protein ratios. Cross-linking of Ca2+-ATPase crystals with glutaraldehyde protects the structure against conditions such as low Ca2+, high pH, elevated temperature, SH group reagents, high concentration of detergents, and removal of phospholipids by extraction with organic solvents that disrupt unfixed preparations.     

Crystallization and preliminary X-ray crystallographic analysis of Mirabilis antiviral protein.

Mirabilis antiviral protein is a single-chain ribosome-inactivating protein purified from the tuberous root of Mirabilis jalapa L. We obtained several forms of crystals of the protein by the hanging drop vapor diffusion method, but most of these crystals were not suitable for X-ray crystallography. After refining the growth conditions, crystals of crystallographic quality were grown in 20-microliters droplets of an equi-volume mixture of 1.5% (w/v) protein solution and a reservoir solution containing 49 to 50% (w/v) ammonium sulfate and 50 mM-ammonium citrate (pH 5.4) at room temperature. Addition of 2 mM-adenine sulfate reduced twinning and "crystal shower". The resulting trigonal crystals diffract beyond 2.5 A resolution using a rotating anode X-ray generator. The space group was determined to be P3(1)21 or P3(2)21 (a = b = 103.9.A, c = 134.6 A, alpha = beta = 90 degrees, gamma = 120 degrees) based on their precession photography of h0l and hk0 zones. There seems to be three monomers in an asymmetric unit for VM = 2.51 A3/Da.