Refolding of Npro fusion proteins

The autoprotease N^pro significantly enhances expression of fused peptides and proteins and drives the formation of inclusion bodies during protein expression. Upon refolding, the autoprotease becomes active and cleaves itself specifically at its own C‐terminus releasing the target protein with its authentic N‐terminus. N^pro wild‐type and its mutant EDDIE, respectively, were fused N‐terminally to the model proteins green fluorescent protein, staphylococcus Protein A domain D, inhibitory peptide of senescence‐evasion‐factor, and the short 16 amino acid peptide pep6His. In comparison with the N^pro wild‐type, the tailored mutant EDDIE displayed an increased rate constant for refolding and cleavage from 1.3 × 10^?4 s^?1 to 3.5 × 10^?4 s^?1, and allowed a 15‐fold higher protein concentration of 1.1 mg/mL when studying pep6His as a fusion partner. For green fluorescent protein, the rate constant was increased from 2.4 × 10^?5 s^?1 to 1.1 × 10^?4 s^?1 when fused to EDDIE. When fused to small target peptides, refolding and cleavage yields were independent of initial protein concentration, even at high concentrations of 3.9 mg/mL, although cleavage rates were strongly influenced by the fusion partner. This behavior differed from conventional 1st order refolding kinetics, where yield strongly depends on initial protein concentration due to an aggregation reaction of higher order. Refolding and cleavage of EDDIE fusion proteins follow a monomolecular reaction for the autoproteolytic cleavage over a wide concentration range. At high protein concentrations, deviations from the model assumptions were observed and thus smaller rate constants were required to approximate the data. Biotechnol. Bioeng. 2009; 104: 774–784 © 2009 Wiley Periodicals, Inc.     

Dieckol,a SARS-CoV 3CLpro inhibitor,isolated from the edible brown algae Ecklonia cava

SARS-CoV 3CL^pro plays an important role in viral replication. In this study, we performed a biological evaluation on nine phlorotannins isolated from the edible brown algae Ecklonia cava. The nine isolated phlorotannins (1–9), except phloroglucinol (1), possessed SARS-CoV 3CL^pro inhibitory activities in a dose-dependently and competitive manner. Of these phlorotannins (1–9), two eckol groups with a diphenyl ether linked dieckol (8) showed the most potent SARS-CoV 3CL^pro trans/cis-cleavage inhibitory effects (IC₅₀s = 2.7 and 68.1 μM, respectively). This is the first report of a (8) phlorotannin chemotype significantly blocking the cleavage of SARS-CoV 3CL^pro in a cell-based assay with no toxicity. Furthermore, dieckol (8) exhibited a high association rate in the SPR sensorgram and formed extremely strong hydrogen bonds to the catalytic dyad (Cys145 and His41) of the SARS-CoV 3CL^pro.     

Refolding and purification of recombinant human granulocyte colony-stimulating factor using hydrophobic interaction chromatography at a large scale

High level expression of recombinant human granulocyte colony-stimulating factor (rhG-CSF) in Escherichia coli (E. coli) usually forms insoluble and inactive aggregates, i.e. inclusion bodies. In the present work, high performance hydrophobic interaction chromatography (HPHIC) was applied to the refolding of rhG-CSF, which was solubilized by 8.0 mol L^?1 urea from the inclusion bodies. First a laboratorial scale column (10 mm × 20 mm I.D.) was employed to study the refolding process. Several factors, including concentration of ammonium sulfate, pH of the mobile phase and flow rate, were investigated in details. The results indicated that the rhG-CSF produced by E. coli could be successfully refolded with simultaneous purification by using HPHIC. The refolding process was further scaled up by using a large column (50 mm × 200 mm I.D.). 200 mL of rhG-CSF solution solubilized by 8.0 mol L^?1 urea, with a total amount of protein around 1.6 g, could be loaded onto the large column at one time. Under these conditions, the obtained rhG-CSF had a specific activity of 2.3 × 10⁸ IU mg^?1 and a purity of 95.4%, the mass recovery during the purification was 36.9%. This work might have great impact on practical production of rhG-CSF, and it also shed a light on protein refolding using liquid chromatography at large scales.     

Synthesis,modification and docking studies of 5-sulfonyl isatin derivatives as SARS-CoV 3C-like protease inhibitors

The Severe Acute Respiratory Syndrome (SARS) is a serious life-threatening and strikingly mortal respiratory illness caused by SARS-CoV. SARS-CoV which contains a chymotrypsin-like main protease analogous to that of the main picornavirus protease, 3CL^pro. 3CL^pro plays a pivotal role in the viral replication cycle and is a potential target for SARS inhibitor development. A series of isatin derivatives as possible SARS-CoV 3CL^pro inhibitors was designed, synthesized, and evaluated by in vitro protease assay using fluorogenic substrate peptide, in which several showed potent inhibition against the 3CL^pro. Structure–activity relationship was analyzed, and possible binding interaction modes were proposed by molecular docking studies. Among all compounds, 8k₁ showed most potent inhibitory activity against 3CL^pro (IC₅₀ = 1.04 μM). These results indicated that these inhibitors could be potentially developed into anti-SARS drugs.     

Native-State Heterogeneity of β2-Microglobulin as Revealed by Kinetic Folding and Real-Time NMR Experiments

The kinetic folding of β₂-microglobulin from the acid-denatured state was investigated by interrupted-unfolding and interrupted-refolding experiments using stopped-flow double-jump techniques. In the interrupted unfolding, we first unfolded the protein by a pH jump from pH 7.5 to pH 2.0, and the kinetic refolding assay was carried out by the reverse pH jump by monitoring tryptophan fluorescence. Similarly, in the interrupted refolding, we first refolded the protein by a pH jump from pH 2.0 to pH 7.5 and used a guanidine hydrochloride (GdnHCl) concentration jump as well as the reverse pH jump as unfolding assays. Based on these experiments, the folding is represented by a parallel-pathway model, in which the molecule with the correct Pro32 cis isomer refolds rapidly with a rate constant of 5–6 s^? 1, while the molecule with the Pro32 trans isomer refolds more slowly (pH 7.5 and 25 °C). At the last step of folding, the native-like trans conformer produced on the latter pathway isomerizes very slowly (0.001–0.002 s^? 1) into the native cis conformer. In the GdnHCl-induced unfolding assays in the interrupted refolding, the native-like trans conformer unfolded remarkably faster than the native cis conformer, and the direct GdnHCl-induced unfolding was also biphasic, indicating that the native-like trans conformer is populated at a significant level under the native condition. The one-dimensional NMR and the real-time NMR experiments of refolding further indicated that the population of the trans conformer increases up to 7–9% under a more physiological condition (pH 7.5 and 37 °C).     

Metal ion dependence of DNA cleavage by SepMI and EhoI restriction endonucleases

Most of type II restriction endonucleases show an absolute requirement for divalent metal ions as cofactors for DNA cleavage. While Mg²⁺ is the natural cofactor other metal ions can substitute it and mediate the catalysis, however Ca²⁺ (alone) only supports DNA binding. To investigate the role of Mg²⁺ in DNA cleavage by restriction endonucleases, we have studied the Mg²⁺ and Mn²⁺ concentration dependence of DNA cleavage by SepMI and EhoI. Digestion reactions were carried out at different Mg²⁺ and Mn²⁺ concentrations at constant ionic strength. These enzymes showed different behavior regarding the ions requirement, SepMI reached near maximal level of activity between 10 and 20 mM while no activity was detected in the presence of Mn²⁺ and in the presence of Ca²⁺ cleavage activity was significantly decreased. However, EhoI was more highly active in the presence of Mn²⁺ than in the presence of Mg²⁺ and can be activated by Ca²⁺. Our results propose the two-metal ion mechanism for EhoI and the one-metal ion mechanism for SepMI restriction endonuclease. The analysis of the kinetic parameters under steady state conditions showed that SepMI had a K_m value for pTrcHisB DNA of 6.15 nM and a V_max of 1.79 × 10^?2 nM min^?1, while EhoI had a K_m for pUC19 plasmid of 8.66 nM and a V_max of 2 × 10^?2 nM min^?1.     

Fluoroquinolones stimulate the DNA cleavage activity of topoisomerase IV by promoting the binding of Mg2 + to the second metal binding site

BackgroundFluoroquinolones target bacterial type IIA topoisomerases, DNA gyrase and topoisomerase IV (Topo IV). Fluoroquinolones trap a topoisomerase–DNA covalent complex as a topoisomerase–fluoroquinolone–DNA ternary complex and ternary complex formation is critical for their cytotoxicity. A divalent metal ion is required for type IIA topoisomerase-catalyzed strand breakage and religation reactions. Recent studies have suggested that type IIA topoisomerases use two metal ions, one structural and one catalytic, to carry out the strand breakage reaction.MethodsWe conducted a series of DNA cleavage assays to examine the effects of fluoroquinolones and quinazolinediones on Mg^2 +-, Mn^2 +-, or Ca^2 +-supported DNA cleavage activity of Escherichia coli Topo IV.ResultsIn the absence of any drug, 20–30 mM Mg^2 + was required for the maximum levels of the DNA cleavage activity of Topo IV, whereas approximately 1 mM of either Mn^2 + or Ca^2 + was sufficient to support the maximum levels of the DNA cleavage activity of Topo IV. Fluoroquinolones promoted the Topo IV-catalyzed strand breakage reaction at low Mg^2 + concentrations where Topo IV alone could not efficiently cleave DNA.Conclusions and general significanceAt low Mg^2 + concentrations, fluoroquinolones may stimulate the Topo IV-catalyzed strand breakage reaction by promoting Mg^2 + binding to metal binding site B through the structural distortion in DNA. As Mg^2 + concentration increases, fluoroquinolones may inhibit the religation reaction by either stabilizing Mg^2 + at site B or inhibition the binding of Mg^2 + to site A. This study provides a molecular basis of how fluoroquinolones stimulate the Topo IV-catalyzed strand breakage reaction by modulating Mg^2 + binding.     

Proteomics analysis of proteins in green alga Haematococcus lacustris (Chlorophyceae) expressed under combined stress of nitrogen starvation and high irradiance

This study is aimed at identifying the proteins that are up-regulated during astaxanthin accumulation in Haematococcus lacustris. For this H. lacustris cells were cultivated in photobioreactors under normal light irradiance of 40 μE m^?2 s^?1 for 6 days and then induced to accumulate astaxanthin for 3 days further by exposure to continuous high irradiance of 200 μE m^?2 s^?1 with fluorescent lamps as light source after the cells reached the stationary phase in a nitrogen-depleted condition. Under this condition, the average astaxanthin content per cell increased from 91 mg/l up to 406 mg/l after 3 days of induction. The proteomics data from a two-dimensional electrophoretic comparison demonstrated that a combination of nitrogen source depletion and 1 h high light have significantly changed the pattern of protein expression in H. lacustris. A total of 49 protein spots were picked after 1 h of stress induction. They consisted of 13 down-regulated proteins and 36 up-regulated proteins. Fifteen proteins which had highly up-regulated expression were further analyzed by matrix assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI-TOF-MS). The results will point toward interesting proteins that can be pursued for further analysis of astaxanthin biosynthesis pathway.     

Methanol vapor biofiltration coupled with continuous production of recombinant endochitinase Ech42 by Pichia Pastoris

Methanol biofiltration using methylotrophic microorganisms has been previously reported by various authors. In a previous study, a modified strain of Pichia pastoris was tested for the ability to produce endochitinase (Ech42) when coupled with methanol vapor biodegradation in batch tests. The next challenge was to validate the process in a continuous system. Thus, in the present study, a biofilter packed with perlite and inoculated with P. pastoris transformed with the plasmid pPIC-ech42 was used for methanol vapor biofiltration and the continuous production of recombinant endochitinase (Ech42) for 60 days. The maximum elimination capacity (EC) of methanol obtained was 1320 g m^?3 h^?1 at a loading rate of 1465 g m^?3 h^?1. The extracellular protein production rate in the leachate was 2360 μg h^?1 with a chitinase enzymatic activity of 123 U L^?1. The protein content on the biofilm samples was negligible, indicating the effectiveness of the overall process and of P. pastoris to excrete proteins. The carbon balance indicated that 81% of the consumed methanol was mineralized and 5.8% was incorporated into biomass. The results of this study and the economic balance underscore the promising application of linking methanol vapor biofiltration to the continuous production of recombinant proteins.     

Cometabolic degradation of dibenzofuran by Comamonas sp. MQ

In this study, strain MQ belonging to the genera Comamonas was used to cometabolically degrade dibenzofuran (DBF) with naphthalene, phenanthrene, benzene, toluene, biphenyl and nitrobenzene, respectively, for the first time. Strain MQ could cometabolically degrade DBF in the growing system using naphthalene as a substrate and the K_i value of strain MQ on naphthalene and DBF was 90.26 mg L^?1 and 68.34 mg L^?1, respectively. The degradation rate of DBF by naphthalene-cultivated strain MQ cells (0.080 mmol L^?1 h^?1) was 1.05, 1.11, 1.13, 1.18 and 1.27-fold higher than that cultivated by phenanthrene, benzene, toluene, biphenyl and nitrobenzene, respectively. Examination of metabolites indicated that naphthalene-cultivated strain MQ cells degraded DBF to 2-hydroxy-4-(3′-oxo-3′H-benzofuran-2′-yliden)but-2-enoic acid (HOBB) and subsequently to salicylic acid via the lateral dioxygenation and meta cleavage pathway. In contrast, biphenyl-cultivated strain MQ cells degraded DBF to monohydroxydibenzofuran through the lateral dioxygenation without meta cleavage pathway. These results suggested that strain MQ could be useful in the bioremediation of environments contaminated by heterocyclic compounds mixtures with polycyclic aromatic hydrocarbons.     

Biodegradation of Tapis blended crude oil in marine sediment by a consortium of symbiotic bacteria

Biodegradation rate and the high molecular weight hydrocarbons are among the important concerns for bioremediation of crude oil. Inoculation of a non-oil-degrading bacterium as supplementary bacteria increased oil biodegradation from 57.1% to 63.0% after 10 days of incubation. Both the oil-degrading bacteria and the non-oil-degrading bacteria were isolated from Malaysian marine environment. Based on the 16S rDNA sequences, the oil-degrading bacteria was identified as Pseudomonas pseudoalcaligenes (99% similarity) while the non-oil-degrading bacterium was Erythrobacter citreus (99% similarity). E. citreus does not grow on crude oil enriched medium under present experimental condition but it withstands 5000 mg kg^?1 Tapis blended crude oil in sediment. Under optimal condition, the oil-degrading bacterium; P. pseudoalcaligenes, alone utilized 583.3 ± 3.8 mg kg^?1 (57.1%) at the rate of 3.97 × 10^?10 mg kg^?1 cell^?1 day^?1 Tapis blended crude oil from 1000 mg kg^?1 oil-contaminated sediment. Inoculation of E. citreus as the supplementary bacteria to P. pseudoalcaligenes enhanced biodegradation. The bacterial consortium degraded 675.8 ± 18.5 mg kg^?1 (63.0%) Tapis blended crude oil from the 1000 mg kg^?1 oil-contaminated sediment. Biodegradation rate of the bacterial consortium increased significantly to 4.59 × 10^?10 mg kg^?1 cell^?1 day^?1 (p = 0.02). Improvement of the oil degradation by the bacterial consortium was due to the synergetic reaction among the bacterial inoculants. There are two implications: (1) E. citreus may have a role in removing self-growth-inhibiting compounds of P. pseudoalcaligens. (2) P. pseudoalcaligenes degraded Tapis blended crude oil while E. citreus competes for the partially degraded hydrocarbons by P. pseudoalcaligenes. P. pseudoalcaligenes forced to breakdown more hydrocarbons to sustain its metabolic requirement. The bacterial consortium degraded 78.7% of (C₁₂–C₃₄) total aliphatic hydrocarbons (TAHs) and 74.1% of the 16 USEPA prioritized polycyclic aromatic hydrocarbons.     

Purification and efficient refolding process for recombinant tissue-type plasminogen activator derivative (reteplase) using glycerol and Tranexamic acid

In this study, a novel and economic method for refolding and purifying recombinant tissue plasminogen activator derivative (r-PA; reteplase) was developed. Reteplase with nine disulfide bonds in its complex structure is expressed in the form of inclusion bodies in Escherichia coli and requires tedious dissolving and refolding processes to achieve its biological activity. Among the different refolding additives that were evaluated, glycerol and tranexamic acid (Txa) were found to be more effective in increasing the refolding yield of reteplase. Using response surface methodology, a solution containing 3.5 M urea, 33% (v/v) glycerol, and 400 mM Txa was found to give the highest refolding yield. The synergic effect of urea, glycerol, and Txa under optimum conditions for a reteplase concentration of 25 μg ml⁻¹ resulted in a high refolding yield of 76.41%. Increased reteplase concentration in the refolding buffer was achieved using the pulse-fed method. In the pulse-fed method, a refolding yield of 49.53% was achieved for a final reteplase concentration of 300 μg ml⁻¹. Using Txa as a novel refolding aid for reteplase instead of ionic amino acids like l-Arginine allowed to purify the refolded reteplase directly by cation-exchange chromatography with high purity.     

A FRET-based assay for the discovery of West Nile Virus NS2B-NS3 protease inhibitors

The West Nile Virus (WNV) has been a worldwide epidemic since the early 1990s. Currently there are no therapeutic treatments for WNV infections. One particular avenue of treatment is inhibition of the NS2B-NS3 protease, an enzyme that is crucial for WNV replication. In our effort to increase the number of NS2B-NS3 protease inhibitors, we report a novel FRET-based high throughput assay for the discovery of WNV NS2B-NS3 protease inhibitors. For this assay, a FRET-based peptide substrate was synthesized and kinetically characterized with the NS2B-NS3 protease. The new substrate exhibits a K_m of 3.35 ± 0.31 μM, a k_cat of 0.0717 ± 0.0016 s^?1 and a k_cat/K_m of 21,400 ± 2000 M^?1 s^?1.     

Reactivation of immobilized penicillin G acylase: Influence of cosolvents and catalytic modulators

Reactivation of penicillin G acylase immobilized in glyoxyl-agarose after inactivation was studied with the purpose of increasing the lifespan of the biocatalyst by simple and reproducible strategies, considering unfolding–refolding and direct incubation in reactivation media. Reactivation yields were increased with respect to the control (fully aqueous medium) when cosolvents were added to the reactivation medium at concentrations below 50% (v/v). Best results were obtained with 30% (v/v) ethyleneglycol (EG) in both reactivation strategies. An increase in reactivation yield from 36.0 to 62.8% was obtained using the unfolding–refolding strategy, while an increase from 50.0 to 68.4% was obtained by direct incubation in aqueous media with respect to control. Catalytic modulators were also included in the reactivation medium: competitive inhibitors (phenylacetic acid and 2-thienylacetic acid) caused a reduction while non-competitive (7-ADCA and 6-APA) caused an increase in reactivation yield. Combining cosolvent and catalytic modulators, best results in both strategies were obtained with 30% (v/v) EG plus 100 mM 7-ADCA, where an increase in reactivation yield from 36.0 to 96.0% and from 50.0 to 98.0% was achieved with unfolding–refolding and direct incubation in reactivation media respectively. Apparent reactivation rate was higher in the case of direct incubation in reactivation media, best results being obtained when using 100 mM 7-ADCA and 30% (v/v) EG, with an increase with respect to the control (fully aqueous medium with no modulator) from 0.309 h^?1 to 1.129 h^?1, while for unfolding–refolding strategy increase was only from 0.124 h^?1 to 0.384 h^?1. Results indicate that direct incubation is a better strategy for penicillin G acylase reactivation and opens up the possibility of significantly increasing the operational lifespan of the biocatalyst by operating the reactor with repeated cycles of reaction and reactivation.     

Synthesis of thermo-sensitive copolymer with affinity butyl ligand and its application in lipase purification

In this study, thermo-sensitive N-alkyl substituted polyacrylamide polymer P_NNB was synthesized by using N-hydroxymethyl acrylamide(NHAM), N-isopropyl acrylamide (NIPA) and butyl acrylate (BA) as monomers, and its low critical solution temperature (LCST) was controlled to be 28 °C. The recovery of the thermo-sensitive polymer was over 98%. Butanol as a hydrophobic ligand was covalently attached onto polymer P_NNB and butyl ligand density was 80 μmol g^?1 polymer. The affinity polymer was used for purification of lipase from crude material. Optimized condition was pH 7.0, 35 °C adsorption temperature, 120 min adsorption time and 0.5 mg ml^?1 initial concentration of lipase. The adsorption isotherm accords with a typical Langmuir isotherm. The maximum adsorption capacity (Q_m) of the affinity polymer for lipase was 24.8 mg g^?1polymer. The affinity copolymer could be recycled by temperature-inducing precipitation and there was only about 6% loss of adsorption capacity after five recyclings. Specific activity of lipase was improved from 14 IU mg^?1 to 506 IU mg^?1 protein, and its recovery achieved 82%. The affinity polymer is suitable for the purification of target proteins from the crude material with large volume and dilute solution.     

Refolding,purification and characterization of an organic solvent-tolerant lipase from Serratia marcescens ECU1010

Expression of recombinant proteins as inclusion bodies in bacteria is one of the most efficient ways to produce cloned proteins, as long as the inclusion bodies can be successfully refolded. In this study, the different parameters were investigated and optimized on the refolding of denatured lipase. The maximum lipase activity of 5000 U/L was obtained after incubation of denatured enzyme in a refolding buffer containing 20 mM Tris–HCl (pH 7.0), 1 mM Ca²⁺ at 20 °C. Then, the refolded lipase was purified to homogeneity by anion exchange chromatography. The purified refolded lipase was stable in broad ranges of temperatures and pH values, as well as in a series of water-miscible organic solvents. In addition, some water-immiscible organic solvents, such as petroleum ether and isopropyl ether, could reduce the polarity and increase the nonpolarity of the refolding system. The results of Fourier transform infrared (FT-IR) microspectroscopy were the first to confirm that lipase refolding could be further improved in the presence of organic solvents. The purified refolded lipase could enantioselectively hydrolyze trans-3-(4-methoxyphenyl) glycidic acid methyl ester [(±)-MPGM]. These features render the lipase attraction for biotechnological applications in the field of organic synthesis and pharmaceutical industry.     

Purification,kinetic and thermodynamic characterization of soluble acid invertase from sugarcane (Saccharum officinarum L.)

We report for the first time kinetic and thermodynamic properties of soluble acid invertase (SAI) of sugarcane (Saccharum officinarum L.) salt sensitive local cultivar CP 77-400 (CP-77). The SAI was purified to apparent homogeneity on FPLC system. The crude enzyme was about 13 fold purified and recovery of SAI was 35%. The invertase was monomeric in nature and its native molecular mass on gel filtration and subunit mass on SDS-PAGE was 28 kDa. SAI was highly acidic having an optimum pH lower than 2. The acidic limb was missing. Proton transfer (donation and receiving) during catalysis was controlled by the basic limb having a pKa of 2.4. Carboxyl groups were involved in proton transfer during catalysis. The kinetic constants for sucrose hydrolysis by SAI were determined to be: k_m = 55 mg ml^?1, k_cat = 21 s^?1, k_cat/k_m = 0.38, while the thermodynamic parameters were: ΔH* = 52.6 kJ mol^?1, ΔG* = 71.2 kJ mol^?1, ΔS* = ?57 J mol^?1 K^?1, ΔG*_E–S = 10.8 kJ mol^?1 and ΔG*_E–T = 2.6 kJ mol^?1. The kinetics and thermodynamics of irreversible thermal denaturation at various temperatures 53–63 °C were also determined. The half -life of SAI at 53 and 63 °C was 112 and 10 min, respectively. At 55 °C, surprisingly the half -life increased to twice that at 53 °C. ΔG*, ΔH* and ΔS* of irreversible thermal stability of SAI at 55 °C were 107.7 kJ mol^?1, 276.04 kJ mol^?1 and 513 J mol^?1K^?1, respectively.     

Glucose isomerase production on a xylan-based medium by Bacillus thermoantarcticus

Effects of medium components on intracellular glucose isomerase (GI) production were investigated by Bacillus thermoantarcticus. The highest GI activity was obtained as 1630 U dm^?3 in the medium containing (g dm^?3): 10.6, birchwood-xylan; 5.6, yeast extract; 5.9 (NH₄)₂SO₄ at T = 55 °C in 33 cm^?3 shake-flasks. When birchwood-xylan was replaced with oat spelt- or beechwood-xylan, GI activity decreased to 1372 and 1308 U dm^?3, respectively. Effects of pH at uncontrolled-pH (pH_UC = 6.0) and controlled-pH (pH_C = 6.0) operations, and oxygen transfer at the air inlet rate of 0.5 vvm and agitation rates of 300, 500 and 700 min^?1, were investigated in 3.0 dm³ bioreactor system with 1.65 dm³ working volume in the designed medium. The highest GI activity was attained at 500 min^?1, 0.5 vvm, pH_UC = 6 as 1840 U dm^?3 where cell concentration was 2.3 g dm^?3. The use of agricultural waste xylan, as the carbon source resulted in concomitant production of xylanase and GI. The highest xylanase activity was attained as 9300 U dm^?3 at 500 min^?1 and 0.5 vvm. K_La varied between 0.008–0.033 s^?1 whereas the highest oxygen uptake rate was 0.002 mmol dm^?3 s^?1. Initially biochemical reaction limitations were effective; thereafter, mass transfer resistances became more effective.     

Kinetic analysis for suicide-substrate inactivation of microperoxidase-11: A modified model for bisubstrate enzymes in the presence of reversible inhibitors

Kinetics of microperoxidase-11 (MP-11) as a heme–peptide enzyme model in oxidation reaction of guaiacol (AH) by hydrogen peroxide was studied in the presence of amino acids, taking into account the inactivation of MP-11 during reaction by its suicide substrate, H₂O₂. Reliability of the kinetic equation was evaluated by non-linear mathematical fitting. Fitting of experimental data into a new integrated kinetic relation showed a close match between the kinetic model and the experimental data. Indeed, it was found that the mechanism of suicide-peroxide inactivation of MP-11 in the presence of amino acids is different from MP-11 and/or horseradish peroxidase. In this mechanism, amino acids compete with hydrogen peroxide for the sixth co-ordination position of iron atom in the heme group through a competitive inhibition mechanism.The proposed model can successfully determine the kinetic parameters including inactivation by hydrogen peroxide as well as the inhibitory rate constants by the amino acid inhibitor.Kinetic parameters of inactivation including the initial activity of MP-11, α₀, the apparent inactivation rate constant, k_i and the apparent inhibition rate constant for cysteine, k_I were obtained 0.282 ± 0.006 min^?1, 0.497 ± 0.013 min^?1 and 1.374 ± 0.007 min^?1 at [H₂O₂] = 1.0 mM, 27 °C, phosphate buffer 5.0 mM, pH 7.0. Results showed that inactivation and inhibition of microperoxidase as a peroxidase model enzyme occurred simultaneously even at low concentrations of hydrogen peroxide (0.4 mM). This kinetic analysis based on the suicide-substrate inactivation of microperoxidase-11, provides a tool and model for studying peroxidase models in the presence of reversible inhibitors. The introduced inhibition procedure can be used in designing activity tunable and specific protected enzyme models in the hidden and reversibly inhibited forms, which do not undergo inactivation.