Integrated enzyme purification and immobilization processes with immobilized metal affinity adsorbents

Silica-based immobilized metal affinity chromatography adsorbents with various ligand densities were prepared for the purification and immobilization of poly(His)-tagged d-hydantoinase (DHTase). An adsorbent with a ligand density of 13.0 μmol Cu²⁺/g gel exhibiting the optimal selectivity and a capacity of 1.4 mg/g gel toward the poly(His)-tagged enzyme was identified. The adsorbent was used for the one-step purification of His-tagged enzymes from crude cell lysate with a purity above 90%. The silica-based affinity adsorbents are particularly well suited for industrial scale operations due to their robustness. A packed-bed bioreactor with the DHTase-loaded adsorbents was used for the continuous conversion of d,l-p-hydroxyphenylhydantoin (d,l-HPH) to N-carbamoyl-d-hydroxyphenylglycine, an intermediate for the production of d-hydroxylphenylglycine. Under optimal conditions, 60 °C and pH 8.0, a conversion of 60% was obtained at a residence time of 30 min. Upon extended operation, the catalytic activity of the biocatalysts declined significantly due to enzyme leakage and enzyme denaturation. The extent of enzyme leakage can be attenuated by crosslinking with glutaraldehyde. In this study, we successfully demonstrate that a packed-bed bioreactor containing silica-based IMAC adsorbents can be used for the direct purification and immobilization of poly(His)-tagged enzymes for biotransformation.     

Extraction of peroxidase from bitter gourd (Momordica charantia) by three phase partitioning with dimethyl carbonate (DMC) as organic phase

Three phase partitioning (TPP) is most renowned technique used for extraction and purification of natural products. In previous studies of TPP, t-butanol is mainly used as an organic phase. This is the first report that explores ability of dimethyl carbonate (DMC) in the field of TPP as an alternate solvent for t-butanol. In the present study TPP process with t-butanol and DMC as organic phase along with different salts was applied to waste bitter gourd powder to obtained peroxidase enzyme. DMC was found to be compatible with most of salts such as ammonium sulphate and sodium citrate and explored as more efficient solvent than t-butanol. This TPP system provides 4.84 fold purity of peroxidase enzyme at optimum source concentration of 0.15 g/mL, with a system comprising DMC as organic phase, sodium citrate (20%) as salt, agitation speed 120 rpm, pH 7, temperature 30 °C and extraction time of 3 h. Present study has aimed for extraction and separation of peroxidase from bitter gourd waste with TPP technique and ensures the scope of carbonated solvents in extraction and purification of proteins.     

Enhancing oxidation activity and stability of iso-1-cytochrome c and chloroperoxidase by immobilization in nanostructured supports

The immobilization of enzymes in inorganic materials has been widely used because it can produce an enhancement of the catalytic stability and enzymatic activity. In this article, the effect of the immobilization of iso-1-cytochrome c (CYC-Sc) from Saccharomyces cerevisiae and chloroperoxidase (CPO) from Caldariomyces fumago on the enzyme stability and catalytic oxidation of styrene was studied. The immobilization was carried out in three silica nanostructured supports with different pore size MCM-41 (3.3 nm), SBA-15 (6.4 nm) and MCF (12.1 nm). The adsorption parameters and leaching degree of immobilized enzymes were determined. Catalytic parameters of immobilized and free enzymes were determined at different temperatures (20–60 °C) and in different acetonitrile/water mixtures (15–85% of acetonitrile). The results show that there is low leaching of the enzymes in the three supports assayed and the adsorption capacity (q_max) was higher as the pore size of the support increased. The pore size also produces the enhancement of peroxidase activities on the styrene oxidation. Thus, CPO adsorption into SBA-15 and MCF showed remarkable thermal and solvent stabilities at 40 °C showing a total turnover numbers of 48,000 and 54,000 times higher than free CPO, respectively. The enhancement of activity and stability doubtless is interesting for the potential industrial use of peroxidases.     

Purification and characterization of recombinant Bacillus subtilis 168 catalase using a basic polypeptide from ribosomal protein L2

An efficient purification system for purifying recombinant Bacillus subtilis 168 catalase (KatA) expressed in Escherichia coli was developed. The basic region containing 252–273 amino acids derived from E. coli ribosomal protein L2 was used as an affinity tag while the small ubiquitin-like modifier (SUMO) was introduced as one specific protease cleavage site between the target protein and the purification tags. L2 (252–273)–SUMO fusion protein purification method can be effectively applied to purify the recombinant catalase using cation exchange resin. This purification procedure was used to purify the KatA and achieved a purification fold of 30.5, a specific activity of 48,227.2 U/mg and an activity recovery of 74.5%. The enzyme showed a Soret peak at 407 nm. The enzyme kept its activity between pH 5 and 10 and between 30 °C and 60 °C, with the highest activity at pH 8.0 and 37 °C. The enzyme displayed an apparent Km of 39.08 mM for hydrogen peroxide. These results agree well with the previous reports about B. subtilis catalase. L2 (252–273)–SUMO fusion protein purification technique provides a novel and effective fusion expression system for the production of recombinant proteins.     

Purification and characterization of a novel thermostable α-l-arabinofuranosidase (α-l-AFase) from Chaetomium sp.

The purification and characterization of an extracellular α-l-arabinofuranosidase (α-l-AFase) from Chaetomium sp. was investigated in this report. The α-l-AFase was purified to homogeneity with a purification fold of 1030. The purified α-l-AFase had a specific activity of 20.6 U mg^?1. The molecular mass of the enzyme was estimated to be 52.9 kDa and 51.6 kDa by SDS–PAGE and gel filtration, respectively. The optimal pH and temperature of the enzyme were pH 5.0 and 70 °C, respectively. The enzyme was stable over a broad pH range of 4.0–10.0 and also exhibited excellent thermostability, i.e., the residual activities reached 75% after treatment at 60 °C for 1 h. The enzyme showed strict substrate specificity for the α-l-arabinofuranosyl linkage. The K_m and V_max values for p-nitrophenyl (pNP)-α-l-arabinofuranoside were calculated to be 1.43 mM and 68.3 μmol min^?1 mg^?1 protein, respectively. Furthermore, the gene encoding α-l-AFase was cloned and sequenced and found to contain a catalytic domain belonging to the glycoside hydrolase (GH) family 43 α-l-AFase. The deduced amino acid sequence of the gene showed the highest identity (67%) to the putative α-l-AFase from Neurospora crassa. This is the first report on the purification, characterization and gene sequence of an α-l-AFase from Chaetomium sp.     

Biocatalytic synthesis of ethyl (R)-2-hydroxy-4-phenylbutyrate with Candida krusei SW2026: A practical process for high enantiopurity and product titer

Ethyl (R)-2-hydroxy-4-phenylbutyrate ((R)-HPBE), a key intermediate in the production of angiotensin-converting enzyme (ACE) inhibitors, was prepared by the microbial reduction of ethyl 2-oxo-4-phenylbutyrate (OPBE). Among 63 microorganisms tested, Candida krusei SW2026, for the first time, was proven to be a highly effective biocatalyst in this reduction process, leading to the (R)-enantiomer in 99.7% ee and 95.1% yield at 2.5 g/L of OPBE (under optimal conditions of 30 °C, pH 6.6, and in the presence of 5% glucose as co-substrate). In order to achieve higher product concentration with desired enantiopurity and yield for application in large-scale production, strategies such as substrate fed-batch and aqueous/organic biphasic system were successfully conducted in the biotransformation reaction. At 20 g/L of OPBE, the enantiomeric excess (ee), yield, and product concentration were enhanced to 97.4%, 82.0%, and 16.6 g/L, respectively, in water/dibutyl phthalate biphasic system, compared with 87.5%, 45.8%, and 9.2 g/L in aqueous medium. This study provides an attractive process of (R)-HPBE production for potential green chemistry applications.     

Upgrading the preparation of high-quality chitosan from Procambarus clarkii wastes over the traditional isolation of shrimp chitosan

Crustacean waste is one of the most severe issues, posing significant environmental and health risks. This study aims to improve managing marine waste by isolating chitosan from Procambarus clarkii by devising a new methodology, incorporating technical steps, e.g., washing, decolorization and deacetylation under a reflexive condenser and dialysis purification. A comparison was made between the prepared P. clarkii chitosan and four types of shrimp chitosans: commercial, high, low, and nano. The obtained chitosan has a low molecular weight and viscosity compared to the commercial shrimp chitosan used in various applications. P. clarkii chitosan was prepared in high quality from a cheap source, as its color and quality were better than those of the commercial shrimp chitosan. The new methodology has successfully extracted chitosan from P. clarkii in a good quality and high purity, achieving 89% deacetylation, high solubility, high purity, and medium molecular weight. Analysis of the different chitosan samples with Fourier transform infrared spectroscopy (FTIR), atomic force microscopy, Raman spectrum referred indicated high similarity between the chitosan different types, regardless of its source. The 3D image of P. clarkii showed the distance between the highest and most profound points of extracted chitosan is 728.94 nm, revealing homogeneous, smooth surfaces, apparently free of pores and cracks. FTIR and Raman spectrum of P. clarkii indicated various functional groups, e.g., alcohol, amines, amides, and phenols. These active groups are responsible for about 60% of the antioxidant activity of that product. Evaluating the quality traits indicated the excellence of the chitosan prepared from P. clarkii, especially in color, viscosity, and antioxidant activity, nominating it for different food applications.     

Preparation and characterization of mixed-mode magnetic adsorbent with p-amino-benzamidine ligand: Operated in a magnetically stabilized fluidized bed reactor for purification of trypsin from bovine pancreas

The magnetic beads were synthesized using glycidylmethacrylate (GMA) and methylmethacrylate (MMA) monomers. A multimodal ligand (i.e., p-amino-benzamidine) was covalently immobilized onto magnetic beads after glutaraldehyde activation, and consequently used for purification of the trypsin from bovine pancreas. The p-amino-benzamidine ligand immobilized magnetic beads were characterized by FTIR, VSM, SEM, and analytical methods. Trypsin adsorption experiments were investigated under different experimental conditions (i.e., medium pH, initial trypsin concentration, temperature, and ionic strength) in a batch system. Maximum trypsin adsorption capacity was found to be 75.9 ± 2.6 mg/g beads. Adsorbed trypsin was eluted by using (0.1 M acetate buffer, pH 3.0) with a 97% recovery. The purification factor of trypsin from crude pancreas extract was 8.7 folds. The purity of the eluted trypsin from p-amino-benzamidine functionalized magnetic beads was determined as 86% by HPLC. The method developed in this report was successfully applied for purification of the trypsin from crude pancreas extract in a magnetically stabilized fluidized bed reactor.     

Aqueous biphasic system for the partial purification of Bacillus subtilis carboxymethyl cellulase

Carboxymethyl cellulase (CMCase) hydrolyses cellulose into glucose and is useful in various industrial applications. Conventional CMCase purification methods are rather complicated and time-consuming; thus, a cost-effective strategy for CMCase recovery is on demand. Polyethylene-glycol (PEG)/sodium citrate aqueous biphasic system (ABS) was adopted in this study to investigate the effectiveness of the ABS in the recovery of extracellular Bacillus subtilis CMCase from fermentation broth. Comprehensive optimization steps were executed that took into consideration the ABS variables of PEG molecular weight, tie-line length (TLL), volume ratio (V_R), crude loading, pH and the addition of sodium chloride (NaCl). A CMCase recovery yield (Y_B) of 88.82% ± 0.69, a purification fold (P_F) of 4.8 and a partition coefficient (K) of 0.44 ± 0.03 were achieved from the bottom phase of the PEG 6000/citrate ABS with TLL of 42.16% (w/w), V_R of 0.29, 1% of (w/w) NaCl, pH 7.0, and 20% (w/w) crude loading. CMCase was mainly segregated to the salt-rich bottom phase because of the hydrophilicity of the enzyme surface. The highly effective recovery technique was further confirmed by SDS-PAGE analysis. Overall, the present study suggests that the ABS is a potential purification strategy for extracellular CMCase.     

A multi-tolerant low molecular weight mannanase from Bacillus sp. CSB39 and its compatibility as an industrial biocatalyst

Bacillus sp. CSB39, isolated from popular traditional Korean food (Kimchi), produced a low molecular weight, thermostable mannanase (MnCSB39); 571.14 U/mL using locust bean gum galactomannan as a major substrate. It was purified to homogeneity using a simple and effective two-step purification strategy, Sepharose CL-6B and DEAE Sepharose Fast Flow, which resulted in 25.47% yield and 19.32-fold purity. The surfactant-, NaCl-, urea-, and protease-tolerant monomeric protein had a mass of ∼30 kDa as analyzed by SDS-PAGE and galactomannan zymography. MnCSB39 was found to have optimal activity at pH 7.5 and temperature of 70 °C. The enzyme showed ˃55% activity at 5.0–15% (w/v) NaCl, and ˃93% of the initial activity after incubation at 37 °C for 60 min. Trypsin and proteinase K had no effect on MnCBS39. The enzyme showed ˃80% activity in up to 3 M urea. The N-terminal amino acid sequence, ALKGDGX, did not show identity with reported mannanases, which suggests the novelty of our enzyme. Activation energy for galactomannan hydrolysis was 26.85 kJmol⁻¹ with a K_cat of 142.58 × 10⁴ s⁻¹. MnCSB39 had K_m and V_max values of 0.082 mg/mL and 1099 ± 1.0 Umg⁻¹, respectively. Thermodynamic parameters such as ΔH, ΔG, ΔS, Q₁₀, ΔG_E-S, and ΔG_E-T supported the spontaneous formation of products and the high hydrolytic efficiency and feasibility of the enzymatic reaction, which strengthen its novelty. MnCSB39 activity was affected by metal ions, modulators, chelators, and detergents. Mannobiose was the principal end-product of hydrolysis. Bacillus subtilis CSB39 produced a maximum of 1524.44 U mannanase from solid state fermentation of 1 g wheat bran. MnCSB39 was simple to purify, was active at a wide pH and temperature range, multi-stress tolerant and catalyzes a thermodynamically possible reaction, characteristics that suggests its suitability for application as an industrial biocatalyst.     

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.     

Human growth hormone-specific aptamer identification using improved oligonucleotide ligand evolution method

LETEG is a method developed and used for the separation and purification of proteins employing a single-step ligand (aptamers) evolution in which aptamers are eluted with an increasing temperature gradient. Using recombinant human growth hormone (rhGH) as the test purification target, and after avoiding cross reactions of aptamers with Bacillus subtilis extracellular proteins by negative SELEX, the effects of time and pH on aptamer binding to rhGH were investigated. The highest binding efficiency of aptamers on rhGH-immobilized microparticles was obtained at pH 7.0. The aptamers that interacted with rhGH were eluted by a multi-stage step-up temperature gradient in ΔT = 10 °C increments within the range T = 55–95 °C; and the strongest affinity binding was disrupted at T = 85 °C where C_Apt = 0.16 μM was eluted. The equilibrium binding data obtained was described by a Langmuir-type isotherm; where the affinity constant was K_D = 218 nM rhGH. RhGH was separated from the fermentation broth with 99.8% purity, indicating that the method developed is properly applicable even for an anionic protein.     

Separation and purification of laccases from two different fungi using aqueous two-phase extraction

Selective purification still poses a challenge in the downstream processing of biomolecules such as proteins and especially enzymes. In this study a polyethylene glycol 3000 (PEG 3000)–phosphate aqueous two-phase system at 25 °C and pH 7 was successfully used for laccase purification and separation. Initially, the effect of phase forming components on enzyme activities in homogenous systems was studied. In the course of the extraction experiments tie lines, enzyme source, initial enzyme activities, phase ratio and sodium chloride concentrations were varied and their influence on the activity partitioning was determined. Partitioning results were validated using clear-native-PAGE and isoelectric focusing. Based on these results, the separation of laccases from Trametes versicolor and Pleurotus sapidus was investigated using the principle of superposition. Sodium chloride was used to adjust laccase partitioning in the applied aqueous two-phase system (ATPS). Finally, two modes of operation are proposed depending on the aim of the purification task. One mode with 0.133 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and without sodium chloride separates P. sapidus laccases from T. versicolor laccases with clearance factors of 5.23 and 6.45, respectively. The other mode of operation with 0.124 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and 0.013 g g⁻¹ of sodium chloride enables a partitioning of both laccases into the bottom phase of the ATPS resulting in a purification factor of 2.74 and 96% activity recovery.     

Pilot-scale production of human serum butyrylcholinesterase suitable for use as a bioscavenger against nerve agent toxicity

Human serum butyrylcholinesterase (Hu BChE) is currently the most appropriate candidate for the prophylaxis of humans against organophosphate (OP) nerve agent toxicity. It is estimated that a dose of 200 mg will protect a human against 2× LD₅₀ of soman, which means that gram quantities of enzyme are needed for human clinical studies. Toward this effort, we report the development of the first procedure that is suitable for the pilot-scale purification of Hu BChE from Cohn fraction IV-4 paste. This procedure involved resuspension of Cohn fraction IV-4 paste, followed by procainamide affinity and DEAE anion-exchange chromatography. The procedure yielded 6–7 g (4.3–5 million U) of purified enzyme from 80 kg of Cohn fraction IV-4 paste. The enzyme was >97% pure as judged by a specific activity of ∼700 U/mg and a major band with a subunit molecular weight of 85 kDa on SDS-PAGE. The high yield and purity obtained suggest that this manufacturing procedure is suitable for the pre-clinical production of Hu BChE.     

Enantioselective synthesis of ethyl-(S)-3-hydroxy-3-phenylpropanoate (S-HPPE) from ethyl-3-oxo-3-phenylpropanoate using recombinant fatty acid synthase (FAS2) from Kluyveromyces lactis KCTC 7133 in Pichia pastoris GS115

Various yeast strains were examined for the microbial reduction of ethyl-3-oxo-3-phenylpropanoate (OPPE) to ethyl-(S)-3-hydroxy-3-phenylpropanoate (S-HPPE), which is the chiral intermediate for the synthesis of a serotonin uptake inhibitor, Fluoxetine. Kluyveromyces lactis KCTC 7133 was found as the most efficient strain in terms of high yield (83% at 50 mM) and high optical purity ee > 99% of S-HPPE. Based on the protein purification, activity analysis and the genomic analysis, a fatty acid synthase (FAS) was identified as the responsible β-ketoreductase. To increase the productivity, a recombinant Pichia pastoris GS115 over-expressing FAS2 (α-subunit of FAS) of K. lactis KCTC7133 was constructed. In the optimized media condition, the recombinant P. pastoris functionally over-expressed the FAS2. Recombinant P. pastoris showed 2.3-fold higher reductase activity compared with wild type P. pastoris. With the recombinant P. pastoris, the 91% yield of S-HPPE was achieved at 50 mM OPPE maintaining the high optical purity of the product (ee > 99%).     

Characterization of a naringinase from Aspergillus oryzae 11250 and its application in the debitterization of orange juice

Naringinase plays a rather important role in reducing the bitterness of juice by hydrolyzing naringin. A novel extracellular naringinase was purified from Aspergillus oryzae 11250 cultured in the presence of orange peel. A 26.78-fold purification rate was achieved by salt-induced precipitation, followed by anion-exchange and gel filtration chromatography with 32% recovery and specific activity of 2194.62 units per mg protein (U/mg). The optimum pH and temperature for naringinase activity were 5.0 and 45 °C, respectively. This enzyme was stable at 30 °C for 5 h. The K_m and V_max of naringinase toward naringin determined by Lineweaver-Burk method were 1.60 ± 0.13 mM and 126.21 ± 5.52 μmol/(min mg), respectively. The enzyme activity was inhibited completely by Ag⁺ at 10 mM. Naringinase is capable of hydrolyzing naringin, neohesperidin, and some other glycosides. A supplement of 6 U/mL of this naringinase in citrus juice sufficiently removed naringin to relieve the bitterness of citrus juice. These properties make the enzyme an ideal candidate for commercial application in the debitterization of orange juice.     

Isolation and biochemical characteristics of a molecular form of epididymal acid phosphatase of boar seminal plasma

The fluid of boar epididymis is characterized by a high activity of acid phosphatase (AcP), which occurs in three molecular forms. An efficient procedure was developed for the purification of a molecular form of epididymal acid phosphatase from boar seminal plasma. We focused on the epididymal molecular form, which displayed the highest electrophoretic mobility. The purification procedure (dialysis, ion exchange chromatography, affinity chromatography and hydroxyapatite chromatography) used in this study gave more than 7000-fold purification of the enzyme with a yield of 50%. The purified enzyme was homogeneous by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE). The purified molecular form of the enzyme is a thermostable 50 kDa glycoprotein, with a pI value of 7.1 and was highly resistant to inhibitors of acid phosphatase when p-nitrophenyl phosphate was used as the substrate. Hydrolysis of p-nitrophenyl phosphate by the purified enzyme was maximally active at pH of 4.3; however, high catalytic activity of the enzyme was within the pH range of 3.5–7.0. Kinetic analysis revealed that the purified enzyme exhibited affinity for phosphotyrosine (K_m = 2.1 × 10⁻³ M) and was inhibited, to some extent, by sodium orthovanadate, a phosphotyrosine phosphatase inhibitor. The N-terminal amino acid sequence of boar epididymal acid phosphatase is ELRFVTLVFR, which showed 90% homology with the sequence of human, mouse or rat prostatic acid phosphatase.The purification procedure described allows the identification of the specific biochemical properties of a molecular form of epididymal acid phosphatase, which plays an important role in the boar epididymis.     

Purification of a laccase from fungus combs in the nest of Odontotermes formosanus

A new enzyme was isolated from the fungus combs in the nest of Odontotermes formosanus and identified as a laccase. The single laccase was purified with a purification factor of 16.83 by ammonium sulphate precipitation and anion exchange chromatography, to a specific activity of 211.11 U mg⁻¹. Its molecular mass was 65 kDa. The optimum pH value and temperature were 4.0 °C and 10 °C with ABTS as the substrate, respectively. The enzyme activity stabilized at temperatures between 10 °C and 30 °C and decreased rapidly when the temperature was above 30 °C. The V_max and K_m values were 3.62 μmol min⁻¹ mg⁻¹ and 119.52 μM, respectively. Ethanol concentration affected laccase activity, inhibiting 60% of enzyme activity at a concentration of 70%. Metal ions of Mg²⁺, Ba²⁺ and Fe²⁺ showed inhibition on enzyme activity of 17.2%, 5.3% and 9.4%, respectively, with the increase of metal ions concentration from 1 mM to 5 mM. Especially Fe²⁺ strongly inhibited enzyme activity up to 89% inhibition at a concentration of 1 mM.     

Expanded bed adsorption of an alkaline lipase from Pseudomona cepacia

An extracellular lipase was isolated from Pseudomona cepacia by expanded bed adsorption on an Amberlite 410 ion-exchange resin. Enzyme characterization and hydrodynamic study of a chromatography column were done. Enzyme purification was done at three condition of expanded bed height (H): at one and half (6 cm), at two (8 cm) and at three (12 cm) times the fixed bed height (H₀ = 4 cm). The results showed that the experimental data was fitted to the Richardson and Zaki equation, and the comparison between the experimental and calculated terminal velocities showed low relative error. In enzyme purification for better condition, a purification factor of about 80 times was found at 6 cm of expanded bed height, or 1.5 times of expansion degree. Purified lipase had an optimal pH and a temperature of 8 and 37 °C, respectively.     

Cost effective characterization process and molecular dynamic simulation of detergent compatible alkaline protease from Bacillus pumilus strain MP27

A psychrothermotolerant alkaline protease isolated from Bacillus pumilus MP27 with a molecular mass ∼53 kDa was isolated from Southern ocean water samples. It was partially purified by single step TPP with purity fold of 16.65. The enzyme was found to be widely stable within a range of temperature and pH, maintaining 52.25% of its activity at 50 °C and 92% at pH 12. The enzyme exhibited an exceptional activity along with tested detergents, showing 98% stability with SDS (10 mg/ml) and ̴ 99% stability with Tide detergent (7 mg/ml). Further, the alkaline protease gene of 1152 bp was successfully cloned in pGEM-T Easy vector in E. coli DH5α. The gene sequence was further translated, modeled and molecular dynamic simulation was performed. The modeled protein was highly unstable during the first 5 ns and therefore could not able to form bonds with the ligand after 1 ns of simulation.