Immobilized glucose oxidase on different supports for biotransformation removal of glucose from oligosaccharide mixtures

Four immobilized forms of glucose oxidase (GOD) were used for biotransformation removal of glucose from its mixture with dextran oligosaccharides. GOD was biospecifically bound to Concanavalin A-bead cellulose (GOD-ConA-TBC) and covalently to triazine-bead cellulose (GOD-TBC). Eupergit C and Eupergit CM were used for preparation of other two forms of immobilized GOD: GOD-EupC and GOD-EupCM. GOD-ConA-TBC and GOD-EupC exhibited the best operational and storage stabilities. pH and temperature optima of these two immobilized enzyme forms were broadened and shifted to higher values (pH 7 and 35 °C) in comparison with those of free GOD. The decrease of V_max values after immobilization was observed, from 256.8 ± 7.0 μmol min⁻¹ mg_GOD⁻¹ for free enzyme to 63.8 ± 4.2 μmol min⁻¹ mg_GOD⁻¹ for GOD-ConA-TBC and 45 ± 2.7 μmol min⁻¹ mg_GOD⁻¹ for GOD-EupC, respectively. Depending on the immobilization mode, the immobilized GODs were able to decrease the glucose content in solution to 3.8–15.6% of its initial amount The best glucose conversion, was achieved by an action of GOD-EupCM on a mixture of 100 g dextran with 9 g of glucose (i.e. 98.7% removal of glucose).     

Preparative-scale kinetic resolution of racemic styrene oxide by immobilized epoxide hydrolase

Epoxide hydrolase from Aspergillus niger was immobilized onto the modified Eupergit C 250 L through a Schiff base formation. Eupergit C 250 L was treated with ethylenediamine to introduce primary amine groups which were subsequently activated with glutaraldehyde. The amount of introduced primary amine groups was 220 μmol/g of the support after ethylenediamine treatment, and 90% of these groups were activated with glutaraldehyde. Maximum immobilization of 80% was obtained with modified Eupergit C 250 L under the optimized conditions. The optimum pH was 7.0 for the free epoxide hydrolase and 6.5 for the immobilized epoxide hydrolase. The optimum temperature for both free and immobilized epoxide hydrolase was 40 °C. The free epoxide hydrolase retained 52 and 33% of its maximum activity at 40 and 60 °C, respectively after 24 h preincubation time whereas the retained activities of immobilized epoxide hydrolase at the same conditions were 90 and 75%, respectively. Immobilized epoxide hydrolase showed about 2.5-fold higher enantioselectivity than that of free epoxide hydrolase. A preparative-scale (120 g/L) kinetic resolution of racemic styrene oxide using immobilized preparation was performed in a batch reactor and (S)-styrene oxide and (R)-1-phenyl-1,2-ethanediol were both obtained with about 50% yield and 99% enantiomeric excess. The immobilized epoxide hydrolase was retained 90% of its initial activity after 5 reuses.     

Comparative biochemical characterization of soluble and chitosan immobilized β-galactosidase from Kluyveromyces lactis NRRL Y1564

An investigation was conducted on the production of β-galactosidase (β-gal) by different strains of Kluyveromyces, using lactose as a carbon source. The maximum enzymatic activity of 3.8 ± 0.2 U/mL was achieved by using Kluyveromyces lactis strain NRRL Y1564 after 28 h of fermentation at 180 rpm and 30 °C. β-gal was then immobilized onto chitosan and characterized based on its optimal operation pH and temperature, its thermal stability and its kinetic parameters (K_m and V_max) using o-nitrophenyl β-d-galactopyranoside as substrate. The optimal pH for soluble β-gal activity was found to be 6.5 while the optimal pH for immobilized β-gal activity was found to be 7.0, while the optimal operating temperatures were 50 °C and 37 °C, respectively. At 50 °C, the immobilized enzyme showed an increased thermal stability, being 8 times more stable than the soluble enzyme. The immobilized enzyme was reused for 10 cycles, showing stability since it retained more than 70% of its initial activity. The immobilized enzyme retained 100% of its initial activity when it was stored at 4 °C and pH 7.0 for 93 days. The soluble β-gal lost 9.4% of its initial activity when it was stored at the same conditions.     

A comparison of the kinetic properties of free and immobilized Aspergillus oryzae β-galactosidase

The objective of this work was to compare the properties of free and immobilized β-galactosidase (Aspergillus oryzae), entrapped in alginate–gelatin beads and cross-linked with glutaraldehyde. The free and immobilized forms of the enzyme showed no decrease in enzyme activity when incubated in buffer solutions in pH ranges of 4.5–7.0. The kinetics of lactose hydrolysis by the free and immobilized enzymes were studied at maximum substrate concentrations of 90 g/L and 140 g/L, respectively, a temperature of 35 °C and a pH of 4.5. The Michaelis–Menten model with competitive inhibition by galactose fit the experimental results for both forms. The K_m and V_m values of the free enzyme were 52.13 ± 2.8 mM and 2.56 ± 0.3 g_glucose/L min mg_enzyme, respectively, and were 60.30 ± 3.3 mM and 1032.07 ± 51.6 g_lactose/min m³_catalyst, respectively, for the immobilized form. The maximum enzymatic activity of the soluble form of β-galactosidase was obtained at pH 4.5 and 55 °C. Alternatively, the immobilized form was most active at pH 5.0 at 60 °C. The free and immobilized enzymes presented activation energies of 6.90 ± 0.5 kcal/mol and 7.7 ± 0.7 kcal/mol, respectively, which suggested that the immobilized enzyme possessed a lower resistance to substrate transfer.     

Copper,zinc superoxide dismutase of Curcuma aromatica is a kinetically stable protein

This study details on cloning and characterization of Cu,Zn superoxide dismutase (Ca–Cu,Zn SOD) from a medicinally important plant species Curcuma aromatica. Ca–Cu,Zn SOD was 692 bp with an open reading frame of 459 bp. Expression of the gene in Escherichia coli cells followed by purification yielded the enzyme with K_m of 0.047 ± 0.008 μM and V_max of 1250 ± 24 units/mg of protein. The enzyme functioned (i) across a temperature range of −10 to +80 °C with temperature optima at 20 °C; and (ii) at pH range of 6–9 with optimum activity at pH 7.8. Ca–Cu,Zn SOD retained 50% of the maximum activity after autoclaving, and was stable at a wide storage pH ranging from 3 to 10. The enzyme tolerated varying concentrations of denaturating agent, reductants, inhibitors, trypsin, was fairly resistant to inactivation at 80 °C for 180 min (k_d, 6.54 ± 0.17 × 10⁻³ min⁻¹; t_1/2, 106.07 ± 2.68 min), and had midpoint of thermal transition (T_m) of 70.45 °C. The results suggested Ca–Cu,Zn SOD to be a kinetically stable protein that could be used for various industrial applications.     

Immobilization of alkaline serine endopeptidase from Bacillus licheniformis on SBA-15 and MCF by surface covalent binding

An industrial enzyme, alkaline serine endopeptidase, was immobilized on surface modified SBA-15 and MCF materials by amide bond formation using carbodiimide as a coupling agent. The specific activities of free enzyme and enzyme immobilized on SBA-15 and MCF were studied using casein (soluble milk protein) as a substrate. The highest activity of free enzyme was obtained at pH 9.5 while this value shifted to pH 10 for SBA-15 and MCF immobilized enzyme. The highest activity of immobilized enzymes was obtained at higher temperature (60 °C) than that of the free enzyme (55 °C). Kinetic parameters, Michaelis–Menten constant (K_m) and maximum reaction velocity (V_max), were calculated as K_m = 13.375, 11.956, and 8.698 × 10^?4 mg/ml and V_max = 0.156, 0.163 and 0.17 × 10^?3 U/mg for the free enzyme and enzyme immobilized on SBA-15 and MCF, respectively. The reusability of immobilized enzyme showed 80% of the activity retained even after 15 cycles. Large pore sized MCF immobilized enzyme was found to be more promising than the SBA-15 immobilized enzyme due to the availability of larger pores of MCF, which offer facile diffusion of substrate and product molecules.     

Immobilization of α-galactosidase on galactose-containing polymeric beads

Industrial application of α-galactosidase requires efficient methods to immobilize the enzyme, yielding a biocatalyst with high activity and stability compared to free enzyme. An α-galactosidase from tomato fruit was immobilized on galactose-containing polymeric beads. The immobilized enzyme exhibited an activity of 0.62 U/g of support and activity yield of 46%. The optimum pH and temperature for the activity of both free and immobilized enzymes were found as pH 4.0 and 37 °C, respectively. Immobilized α-galactosidase was more stable than free enzyme in the range of pH 4.0–6.0 and more than 85% of the initial activity was recovered. The decrease in reaction rate of the immobilized enzyme at temperatures above 37 °C was much slower than that of the free counterpart. The immobilized enzyme shows 53% activity at 60 °C while free enzyme decreases 33% at the same temperature. The immobilized enzyme retained 50% of its initial activity after 17 cycles of reuse at 37 °C. Under same storage conditions, the free enzyme lost about 71% of its initial activity over a period of 7 months, whereas the immobilized enzyme lost about only 47% of its initial activity over the same period. Operational stability of the immobilized enzyme was also studied and the operational half-life (t_1/2 was determined as 6.72 h for p-nitrophenyl α-d-galactopyranoside (PNPG) as substrate. The kinetic parameters were determined by using PNPG as substrate. The K_m and V_max values were measured as 1.07 mM and 0.01 U/mg for free enzyme and 0.89 mM and 0.1 U/mg for immobilized enzyme, respectively. The synthesis of the galactose-containing polymeric beads and the enzyme immobilization procedure are very simple and also easy to carry out.     

Reversible immobilization of catalase on fibrous polymer grafted and metal chelated chitosan membrane

Poly(itaconic acid) grafted and/or Fe(III) ions incorporated chitosan membranes were used for reversible immobilization of catalase (from bovine liver) via adsorption. The influences of pH and initial catalase concentration on the immobilization capacities of the CH-g-poly(IA) and CH-g-poly(IA)-Fe(III) membranes have been investigated in a batch system. Maximum catalase adsorption onto CH-g-poly(IA) and CH-g-poly(IA)-Fe(III) membrane were found to be 6.3 and 37.8 mg/g polymer at pH 5.0 and 6.5, respectively. The CH-g-poly(IA)-Fe(III) membrane with high catalase adsorption capacity was used in the rest of the study. The K_m value for immobilized catalase on CH-g-poly(IA)-Fe(III) (25.8 mM) was higher about 1.6-fold than that of free enzyme (13.5 mM). Optimum operational temperature was observed at 40 °C, a 5 °C higher than that of the free enzyme and was significantly broader. The optimum operational pH was same for both free and immobilized catalase (pH 7.0). Thermal stability was found to increase with immobilization. Free catalase lost all its activity within 20 days whereas immobilized catalase lost 23% of its activity during the same incubation period. It was observed that the same support enzyme can be repeatedly used for immobilization of catalase after regeneration without significant loss in adsorption capacity or enzyme activity. In addition, the CH-g-poly(IA)-Fe(III) membrane prepared in this work showed promising potential for various biotechnological applications.     

Continuous degradation of maltose by enzyme entrapment technology using calcium alginate beads as a matrix

Maltase from Bacillus licheniformis KIBGE-IB4 was immobilized within calcium alginate beads using entrapment technique. Immobilized maltase showed maximum immobilization yield with 4% sodium alginate and 0.2 M calcium chloride within 90.0 min of curing time. Entrapment increases the enzyme–substrate reaction time and temperature from 5.0 to 10.0 min and 45 °C to 50 °C, respectively as compared to its free counterpart. However, pH optima remained same for maltose hydrolysis. Diffusional limitation of substrate (maltose) caused a declined in V_max of immobilized enzyme from 8411.0 to 4919.0 U ml^?1 min^?1 whereas, K_m apparently increased from 1.71 to 3.17 mM ml^?1. Immobilization also increased the stability of free maltase against a broad temperature range and enzyme retained 45% and 32% activity at 55 °C and 60 °C, respectively after 90.0 min. Immobilized enzyme also exhibited recycling efficiency more than six cycles and retained 17% of its initial activity even after 6th cycles. Immobilized enzyme showed relatively better storage stability at 4 °C and 30 °C after 60.0 days as compared to free enzyme.     

Immobilization of glycolate oxidase from Medicago falcata on magnetic nanoparticles for application in biosynthesis of glyoxylic acid

Glycolate oxidase was isolated from Medicago falcata Linn. after a screening from 13 kinds of C₃ plant leaves, with higher specific activity than the enzyme from spinach. The M. falcata glycolate oxidase (MFGO) was partially purified and then immobilized onto hydrothermally synthesized magnetic nanoparticles via physical adsorption. The magnetic nanoparticles were characterized with scanning electron microscope (SEM), transmission electron microscopy (TEM) and Fourier transform infrared (FT-IR) spectroscopy. The maximum load of MFGO was 56 mg/g support and the activity recovery was 45%. Immobilization of MFGO onto magnetic nanoparticles enhanced the enzyme stability, and the optimum temperature was significantly increased from 15 °C to 30 °C. The immobilized biocatalyst was successfully used in a batch reactor for repeated oxidization of glycolic acid to synthesize glyoxylic acid, retaining ca. 70% of its initial activity after 4 cycles of reaction at 30 °C for nearly 70 h, and its half-life was calculated to be 117 h.     

Immobilisation of CGTase for continuous production of long-carbohydrate-chain alkyl glycosides: Control of product distribution by flow rate adjustment

Bacillus macerans cyclodextrin glycosyltransferase (CGTase) (EC 2.4.1.19) was covalently immobilised on Eupergit C and used in a packed-bed reactor to investigate the continuous production of long-carbohydrate-chain alkyl glycosides from α-cyclodextrin (α-CD) and n-dodecyl-(1,4)-β-maltopyranoside (C₁₂G₂β). The effects of buffer ion strength and pH, and enzyme loading on the immobilisation yield and the enzyme activity were evaluated. Approximately 98% of the protein and 33% of the total activity were immobilised. At pH 5.15, the enzymatic half-life was 132 min at 60 °C and 18 min at 70 °C. The immobilised enzyme maintained 60% of its initial activity after 28 days storage at 4 °C. The degree of conversion was controlled by simple regulation of the flow rate through the reactor, making it possible to optimise the product distribution. It was possible to achieve a yield of the primary coupling product n-dodecyl-(1,4)-β-maltooctaoside (C₁₂G₈β) of about 50%, with a ratio between the primary and the secondary coupling product of about 10. Thermoanaerobacter sp. CGTase (Toruzyme 3.0 L) immobilised on Eupergit C had good operational stability at 60 and 70 °C thus showing the advantages of using more thermostable enzymes in biocatalysis. However, this enzyme was unsuitable for the production of C₁₂G₈β due to extensive disproportionation reactions, giving a broad product range.     

Isolation and properties of β-xylosidase from Aspergillus niger GS1 using corn pericarp upon solid state fermentation

There is growing interest in developing high-yield and low-cost production of xylanolytic enzymes for industrial applications using agroindustrial byproducts. A native strain of Aspergillus niger GS1 was used to produce β-xylosidase (EC 3.2.1.37) on solid state fermentation using corn pericarp (CP) with innovative alkaline electrolyzed water (AEW) pretreatment at room temperature. β-xylosidase was purified by ammonium sulfate fractionation followed by anion exchange and hydrophobic interaction chromatographies. β-Xylosidase showed a molecular weight of 111 kDa, isoelectric point of 5.35 and specific activity of 386.7 U (mg protein)^?1, using p-nitrophenyl-β-d-xylopyranoside as substrate, at pH 5 and 60 °C, and optimal activity at pH 4.5. Optimal temperature was 65 °C, showing full activity after 1 h at 60 °C. Activity was reduced by 1 mM β-mercaptoethanol (55.6 ± 0.1%), and enhanced by 1 mM SDS (11.0 ± 0.03%). K_m and V_max were 6.1 ± 0.9 mM and 1364 ± 105 U (mg protein)^?1, respectively, whereas k_cat was 5.1 s^?1. A predominant α-helix (41%) was determined from circular dichroism on β-xylosidase, while thermal transition profiles produced a T_m of 54.1 ± 5.8 °C, enthalpy change for unfolding of 67.4 ± 6.7 kJ/mol, and onset temperature of 37 °C. Pre-treatment of CP using AEW is an ecologically friendly alternative to chemical and heat treatments for the production of relatively high levels of β-xylosidase.     

Effect of changing the nanoscale environment on activity and stability of nitrate reductase

Nitrate reductase (NR) is employed for fabrication of nitrate sensing devices in which the enzyme in immobilized form is used to catalyze the conversion of nitrate to nitrite in the presence of a suitable cofactor. So far, instability of immobilized NR due to the use of inappropriate immobilization matrices has limited the practical applications of these devices. Present study is an attempt to improve the kinetic properties and stability of NR using nanoscale iron oxide (nFe₃O₄) and zinc oxide (nZnO) particles. The desired nanoparticles were synthesized, surface functionalized, characterized and affixed onto the epoxy resin to yield two nanocomposite supports (epoxy/nFe₃O₄ and epoxy/nZnO) for immobilizing NR. Epoxy/nFe₃O₄ and epoxy/nZnO support could load as much as 35.8 ± 0.01 and 33.20 ± 0.01 μg/cm² of NR with retention of about 93.72 ± 0.50 and 84.81 ± 0.80% of its initial activity respectively. Changes in surface morphology and chemical bonding structure of both the nanocomposite supports after addition of NR were confirmed by scanning electron microscopy (SEM) and fourier transform infrared spectroscopy (FTIR). Optimum working conditions of pH, temperature and substrate concentration were ascertained for free as well as immobilized NR preparations. Further, storage stability at 4 °C and thermal stability between 25–50 °C were determined for all the NR preparations. Analytical applications of immobilized NR for determination of soil and water nitrates along with reusability data has been included to make sure the usefulness of the procedure.     

Immobilization of phytase on epoxy-activated Sepabead EC-EP for the hydrolysis of soymilk phytate

In this work, an active phytase concentrated extract from soybean sprout was immobilized on a polymethacrylate-based polymer Sepabead EC-EP which is activated with epoxy groups. The immobilized enzyme exhibited an activity of 0.1 U/g of carrier and activity yield of 64.7%. The optimum temperature and pH for the activity of both free and immobilized enzymes were found as 60 °C and pH 5.0, respectively. The immobilized enzyme was more stable than free enzyme in the range of pH 3.0–8.0 and more than 70% of the original activity was recovered. Both the enzymes completely retained nearly about 84% of their original activity at 65 °C. The K_m and V_max values were measured as 5 mM and 0.63 U/mg for free enzyme and 12.5 mM and 0.71 U/mg for immobilized enzyme, respectively. Free and immobilized soybean sprout phytase enzymes were also used in the biodegradation of soymilk phytate. The immobilized enzyme hydrolysed 92.5% of soymilk phytate in 7 h at 60 °C, as compared with 98% hydrolysis observed for the native enzyme over the same period of time. The immobilization procedure on Sepabead EC-EP is very cheap and also easy to carry out, and the features of the immobilized enzyme are very attractive that the potential for practical application is considerable.     

Hen egg white as a feeder protein for lipase immobilization

Enzyme stabilization via immobilization is one of the preferred processes as it provides the advantages of recovery and reusability. In this study, Thermomyces lanuginosus lipase has been immobilized through crosslinking using 2% glutaraldehyde and hen egg white, as an approach towards CLEA preparation. The immobilization efficiency and the properties of the immobilized enzyme in terms of stability to pH, temperature, and denaturants was studied and compared with the free enzyme. Immobilization efficiency of 56% was achieved with hen egg white. The immobilized enzyme displayed a shift in optimum pH towards the acidic side with an optimum at pH 4.0 whereas the pH optimum for free enzyme was at pH 6.0. The immobilized enzyme was stable at higher temperature retaining about 83% of its maximum activity as compared to the free enzyme retaining only 41% activity at 70 °C. The denaturation of lipase in free form was rapid with a half-life of 2 h at 60 °C and 58 min at 70 °C as compared to 12 h at 60 °C and 2 h at 70 °C for the immobilized enzyme. The effect of denaturants, urea and guanidine hydrochloride on the free and immobilized enzyme was studied and the immobilized enzyme was found to be more stable towards denaturants retaining 74% activity in 8 M urea and 98% in 6 M GndHCl as compared to 42% and 33% respectively in the case of free enzyme. The apparent K_m (2.08 mM) and apparent V_max (0.95 μmol/min) of immobilized enzyme was lower as compared to free enzyme; K_m (8.0 mM) and V_max (2.857 μmol/min). The immobilized enzyme was reused several times for the hydrolysis of olive oil.     

High hydrostatic pressure increased stability and activity of immobilized lipase in hexane

Lipases are important to high value product synthesis, modification, and enhancement. However, they are often unstable above 40 °C. While most current applications of high hydrostatic pressure (HHP) are for inactivating deleterious enzymes, there is evidence that HHP can stabilize and increase activity of some enzymes. This study examines the apparent kinetics of immobilized lipase-catalyzed synthesis of isoamyl acetate at HHP in hexane. HHP reduced thermal inactivation of lipase by up to 152% after 4 h at 80 °C and 400 MPa when compared to incubations at low pressure. No significant differences were found in activation energy (E_a) at different pressures, irrespectively of the pressurization and heating sequence, and were between 35.7 ± 3.5 and 47.8 ± 8.2 kJ mol^?1, depending on the method. In all methods utilized, activity at 63.5 and 80 °C at 400 MPa was greater (from about 20 to 96% increase) than at low pressure. Activity increased by 110% at low pressure versus a 239% increase at 350 MPa when the temperature was increased from 40 to 80 °C. Increasing pressure up to 350 MPa increased lipase activity while pressures greater than 350 MPa maintained or decreased lipase activity. Activation volume (ΔV^≠) appeared negative between ambient pressure and 200 MPa in contrast to a positive ΔV^≠ between 300 and 600 MPa. Apparent ΔV^≠ was 14.3 ± 1.7 or 15.2 ± 2.2 cm³ mol^?1 at 40 or 80 °C, respectively, between 300 and 500 MPa.     

Enhanced d-hydantoinase activity performance via immobilized cobalt ion affinity membrane and its kinetic study

Various immobilized metal ions affinity membranes (IMAMs) were prepared from the regenerated cellulose membrane (RC membrane) and chelated with various metal ions such as Co²⁺, Ni²⁺, Cu²⁺ and Zn²⁺. The D-hydantoin-hydrolyzing enzyme (DHTase) harboring a poly-His tagged residue was used as a model protein to be immobilized on the prepared IMAMs through the direct metal–protein interaction forces. The adsorption isotherm and the kinetic parameters V_max, K_m,app of DHTase on IMAMs were studied. The cobalt ions chelated IMAM (Co-IMAM) was found to yield the highest specific activity of DHTase. Under the immobilization condition, the cobalt ion chelated amount was 161.4 ± 4.7 μmol/disk with a DHTase activity of 4.1 ± 0.1 U/disk. As compared to the free DHTase, the immobilized DHTase membrane could achieve a broader pH tolerance and higher thermal stability. In addition, 98% of the residual activity could be retained for 7-times repeated use. Only little activity loss was observed within 36-day storage at 4 °C. This is the first report concerning about using cobalt ion as the effective chelated metal ion for simultaneous purification and immobilization operation.     

Effect of heating rate on pDNA production by E. coli

The effects of heating rate (HR) on the performance of two-phase (batch followed by fed-batch) high cell-density cultivations (HCDC) of E. coli DH5α for the production of plasmid DNA (pDNA) were investigated. Optimal temperatures for the HCDC, as selected from shake flask experiments at constant temperatures between 30 and 45 °C, were 35 °C for biomass accumulation in the batch phase and 42 °C for inducing pDNA replication during the fed-batch. In HCDC the temperature was increased at HR of 0.025, 0.05, 0.10 and 0.25 °C/min and the performance of the cultivations were compared to a HCDC run at constant temperature (35 °C). Compared to constant 35 °C, heat-induced HCDC accumulated up to 50% less biomass within the same cultivation time and acetate and glucose accumulated to high concentrations. The overall specific productivity (Q_P) and average pDNA yield (Y_p/x) in HCDC at 35 °C were 0.22 ± 0.02 mg/g h and 5.3 ± 0.00 mg/g, respectively. Such parameters were maximum at a HR of 0.05 °C/min, reaching 0.56 ± 0.06 mg/g h and 9.3 ± 0.6 mg/g, respectively. At HR above 0.5 °C/min, Y_p/x remained relatively constant, whereas Q_P tended to decrease. The supercoiled pDNA fraction remained around 80% at all HR. Bioreactors were equipped with a capacitance/conductivity probe. In all cases biomass concentration correlated closely with the capacitance signal and acetate and glucose accumulation was accompanied by an increase in the conductivity signal. Thus, it was possible to calculate acetate and biomass concentrations, as well as μ, from online capacitance and conductivity signals using estimators. Altogether, in this study it was shown that it is possible to maximize pDNA productivity by choosing an appropriate HR and that relevant parameters can be estimated by capacitance/conductivity signals, which are useful for better process control and development.     

Characterization of functionally active immobilized carbonic anhydrase purified from sheep blood lysates

Carbonic anhydrase (CA) catalyzes the reversible reaction of hydration of CO₂ to bicarbonate and the dehydration of bicarbonate back to CO₂. Sequestration of CO₂ from industrial processes or breathing air may require a large amount of highly active and stable CA. Therefore, the objectives of the present study were to purify large amounts of CA from a cheap and easily accessible source of the enzyme and to characterize the enzymatic and kinetic properties of soluble and immobilized enzyme. We recovered 80% of pure enzyme with a specific activity of 4870 EU/mg protein in a single step using sheep blood lysates from slaughter house waste products and CA specific inhibitor affinity chromatography. Since affinity pure CA showed both anhydrase and esterase activities, we measured the esterase activities for enzymology. The Michaelis–Menten constant, K_M, pH optimum, activation energy, and thermal stability of soluble enzymes were 8 × 10^?2 M, 7.3 pH, 7.3 kcal/mol and 70 °C, respectively.The immobilization of the enzyme to Affigel-10 was very efficient and 83% of purified enzyme was immobilized. The immobilized enzyme showed a K_M of 5 × 10^?2 M and activation energy of 8.9 kcal/mol, suggesting a better preference of substrate for immobilized enzyme in comparison to soluble enzyme. In contrast to soluble enzyme, immobilized enzyme showed relatively higher activity at pH 6–8. From these results, we concluded that a shift in pH profile toward acidic pH is due to modification of lysine residues involved in the immobilization process. The immobilized enzyme was stable at higher temperatures and showed highest activity at 80 °C. The activity of immobilized enzyme in a flow reactor at 0.5–2.2 ml/min flow rate was unaffected. Collectively, results from the present study suggested the application of blood lysate waste from animal slaughterhouses for purification of homogeneous enzyme for CO₂ capture in a flow reactor.     

Structure of dihydropyrimidinase from Sinorhizobium meliloti CECT4114: New features in an amidohydrolase family member

The recombinant dihydropyrimidinase from Sinorhizobium meliloti CECT4114 (SmelDhp) has been characterised and its crystal structure elucidated at 1.85 Å. The global architecture of the protein is reminiscent of that of the amidohydrolase superfamily, consisting of two domains; an (α/β)₈ TIM-like barrel domain, where the catalytic centre is located, and a smaller β-sheet sandwich domain of unknown function. The c-terminal tails of each subunit extend toward another monomer in a swapping-like manner, creating a hydrogen bond network which suggests its implication in protein oligomerisation. Mutational and structural evidence suggest the involvement of a conserved tyrosine in the reaction mechanism of the enzyme. SmelDhp presents both hydantoinase and dihydropyrimidinase activities, with higher affinity for the natural six-membered ring substrates. For the five-membered ring substrates, affinity was greater for those with aliphatic and apolar groups in the 5th carbon atom, with the highest rates of hydrolysis for d-5-methyl and d-5-ethyl hydantoin (k_cat/K_m = 2736 ± 380 and 944 ± 52 M^?1 s^?1, respectively). The optimal conditions for the enzyme activity were found to be 60 °C of temperature at pH 8.0. SmelDhp retains 95% of its activity after 6-hour preincubation at 60 °C. This is the first dihydropyrimidinase used for the hydrolytic opening of non-natural 6-monosubstituted dihydrouracils, which may be exploited for the production of β-amino acids.