Mathematical modeling of affinity ultrafiltration process

An affinity ultrafiltration process has been developed by exploiting affinity binding in conjunction with cross-flow filtration. The process was proven to possess high resolution, high recovery yield, and ease of scale-up. The process could purify trypsin from a trypsin-chymotrypsin mixture batchwise or continuously. Essential for applying this concept was the synthesis of a water-soluble high-molecular-weight polymer bearing m-aminobenzamidine, a strong and specific trypsin in hibitor. A mathematical model was also developed to describe the dynamic behavior of the newly developed purification process. The model was able to predict the profiles of enzyme concentrations in the process with high accuracy.     

Synthesis and characterization of a water-soluble affinity polymer for trypsin purification

A specific ligand bound polymer has been synthesized for the purpose of purification and stabilization of trypsin, an easily autodigestible enzyme. The affinity polymer was formed by copolymerizing N-acryloyl-m-aminobenzamidine, a strong trypsin inhibitor, and acrylamide in the absence of oxygen. Kinetic studies on the trypsin inhibition revealed that there was a strong binding between this enzyme and the polymer and the mechanism was of a competitive manner with an inhibition constant of 0.6 x 10(-3)M. Such an affinity polymer was also very effective in preventing trypsin from auto-digestion at 4 degrees C.Based on this finding and the principle of cross flow filtration, a new process has been developed for purification of trypsin from a solution containing chymotrypsin. The experimental data indicated that trypsin was bound to the polymer (MW > 10(5)) and remained in the retentate while unbound chymotrypsin was collected in the filtrate. This purification process has a capability of recovering 98% pure trypsin at 90% yield.     

The possibility for improvement of ceramic membrane ultrafiltration of an enzyme solution

Ultrafiltration represents an attractive downstream processing technique for enzymes concentration and their primary purification. However, the process efficiency is often limited by protein fouling and shear-induced enzyme deactivation, resulting in permeate flux decline and loss of enzyme activity. The objective of this work was to investigate the possibility for improvement of ceramic membrane ultrafiltration of endo-pectinase solution. Experimental investigations were performed on a 5 nm ceramic membrane with the Kenics static mixer placed inside the membrane in order to improve the process performance. The use of the static mixer resulted in the flux improvement of about 45% at a volume concentration factor (VCF) of 3 leading to the reduction of operation time of 25% and the energy saving of about 40%. Although the rejection of endo-pectinase was higher than 96%, the extensive loss of the enzyme activity during operation indicated that the modification of the feed solution is essential for improved ultrafiltration performance. Addition of pectin to the original endo-pectinase solution led to a significant reduction of the enzyme deactivation: the enzyme activity yield was 90% at a VCF of 1.6 during operation with the static mixer.     

Ultrafiltration of raw sewage using an immobilized enzyme membrane

Ultrafiltration of raw sewage was performed using multiple enzymes immobilized on non-cellulosic, ultrafiltration membranes. An increase of 12% in the permeate flux rate at quasi-steady state was observed due to the action of the immobilized enzymes. Enzymes were immobilized by physical sorption to minimize the loss of ultrafiltration capability of the membrane, due to the immobilization process. A mathematical model based on diffusive transport and enzymatic action is presented. A standard Marquardt algorithm and a fourth-order Runge-Kutta integration routine were used for estimation of the non-linear parameters in the model. A comparison of data presented here with the data reported earlier on the ultrafiltration of NFDM (non-fat dry milk), showed that the enzyme-membrane has a longer half-life in the case of NFDM than for raw sewage. Furthermore, the first-order enzyme decay rate is much faster in the multiple enzyme system used in raw sewage filtration than in the single enzyme system used in the ultrafiltration of NFDM.     

A shortcut method for evaluation of protein deposition onto the membrane surface in crossflow ultrafiltration

In this study, a procedure for quantifying the surface deposition of proteins in crossflow ultrafiltration has been developed. The procedure consists of determining the protein adsorption behavior onto the membrane surface from a few dynamic measurements performed in a nonfiltration and a filtration mode, and evaluating the concentration polarization (CP) layer thickness based on the adsorption data. To predict the interdependence between the protein adsorption and CP, a simplified mathematical model has been formulated. The model was used to assess the protein adsorption and thus yield reduction in the ultrafiltration process at different protein concentration in the solution. As a case study, ultrafiltration of aqueous solutions of BSA and lysozyme (LYZ) was examined on a polyethersulfone membrane with the molecular weight cutoff of 10 or 100 kDa. The protein concentration in the solutions varied within a relatively low concentration range, i.e. below 10 mg mL^?1, characteristic for solvent exchange between sequential operations of protein purification by chromatography and extraction. Both proteins markedly differed in the mechanism of surface deposition; for BSA hydrophobic interactions were suggested to be dominant, whereas in case of LYZ electrostatic interactions contributed the most to the deposition mechanism. The effect of additives of the protein solutions, i.e. inorganic salts, PEG, and urea depended on the adsorption mechanism and was also specific for each protein. Nevertheless, the proposed procedure performed well in the evaluation of surface deposition and yield reduction, regardless of the protein type and its solvent environment.     

高活力5′-磷酸二酯酶制备及水解RNA的研究

目的:获得高活力5′-磷酸二酯酶液,提高核酸RNA酶解效率。方法:采用超滤和盐析技术对从麦芽根浸提液中纯化5′-磷酸二酯酶工艺进行研究,采用单因子试验法优化酶解工艺条件。结果:浸提液依次经过5万Da超滤膜浓缩、40%饱和度硫酸铵盐析、5万Da超滤膜脱盐后,酶活力可达1 500U/ml;第1次超滤膜透过液可作为浸提液循环使用,酶活力是水浸提的1.15倍;第2次超滤膜透过液浓缩5倍后,可回收56.46%硫酸铵,浓缩母液可按1∶2比例循环使用;在底物浓度5.8%、酶用量8%、反应时间2h条件下,RNA酶解率可达95%。结论:初步建立了适合工业化规模的核苷酸生产新工艺。     

Studies on proteolytic activity in commercial myoglobin preparations

Commercial myoglobin preparations from horse skeletal muscle degraded casein. The maximum activity was at pH8-8.5. A muscle myofibril preparation was also attacked. The protease could be partly separated from the myoglobin by selective ultrafiltration through a membrane with an exclusion limit of mol.wt. 30000. A greater than 1000-fold purification of the proteolytic activity was achieved by affinity chromatography with soya-bean trypsin inhibitor bound to CM-cellulose. The enzyme preparation hydrolysed p-toluenesulphonyl-l-arginine methyl ester and N-benzyloxycarbonyl-l-tyrosine p-nitrophenyl ester. Its activity was inhibited strongly by soya-bean and ovomucoid trypsin inhibitors, serum and the soluble fraction of muscle homogenates. EDTA, p-chloromercuribenzoate and phenylmethylsulphonyl fluoride also caused some inhibition.     

Partial purification and characterization of a novel Mg2+- dependent ATPase present in the cytosol from human erthrocytes

Mg²⁺-ATPase activity was identified in the cytosol of human erythrocytes. A partial purification of this activity was achieved by an initial DEAE-Sephadex column chromatography, followed by gel filtration on Sephadex G-100 and then a second DEAE-Sephadex chromatography procedure. The enzyme appeared in the void volume of the Sephadex G-100 column and was retained on an Amicon XM100A ultrafiltration membrane. The molecular weight of the enzyme was estimated to be 113 000 from SDS gels. The above purification protocol yielded an enzyme with an optimal pH between 7.6 and 8.2. The enzyme activity increased linearly between 30 and 44°C. It was stable for several months at ?20°C. Magnesium was essential for activity, but the rate attainable with Mn²⁺ was at least as great as that due to Mg²⁺. No other divalent cation was able to substitute for Mg²⁺ or Mn²⁺. Neither low nor high Ca²⁺ concentrations significantly affected the enzymatic activity. Substrate specificity studies showed that ATP was the preferred substrate followed by CTP (46% of the rate produced by ATP). Hydrolysis of GTP, UTP, ITP and ADP was less than 10% of the rate seen with ATP. No phosphatase, pyrophosphatase, phosphodiesterase, hexokinase, phosphofructokinase or adenylate cyclase activity could be detected in this enzyme preparation. Calmodulin, which stimulates the (Ca²⁺ + Mg²⁺)-ATPase of the human erythrocyte membrane, failed to enhance the Mg²⁺-ATPase activity. Of considerable interest, the activity of this Mg²⁺-ATPase was enhanced approximately 5-fold by low concentrations of mercuric ion, p-hydroxymercuribenzoate and DTNB, but was much less sensitive to iodoacetamide.     

Proteinase Inhibitors in Germinating Barley Embryos

The activities of trypsin inhibitors and Aspergillus-proteinase inhibitors have been assayed in barley embryos germinating in different conditions. The Aspergillus-proteinase inhibitor activity increased about 20-fold during 6 days at 20°C both in separated embryos germinating on nutrient agar and in the embryos of undissected grains germinating on agar with or without mineral salts. Significant inhibitor activity was also present in root tips at later stages of vegetative growth. Whether any changes occurred in the molecular weight distribution of the inhibitors present in the seedlings was studied by gel filtration on Sephadex G-75; only minor changes were observed. The trypsin inhibitor activity per seedling remained roughly constant in all cultures. In gel filtration experiments all the activity appeared to be due to the inhibitor species present in resting embryos.     

Acidophilic tannase from marine Aspergillus awamori BTMFW032

Aspergillus awamori BTMFW032, isolated from sea water, produced tannase as extracellular enzyme under submerged culture conditions. Enzyme with a specific activity of 2761.89 IU/mg protein, a final yield of 0.51 %, and a purification fold of 6.32 was obtained after purification to homogeneity by ultrafiltration and gel filtration. SDS-PAGE analyses under non- reducing and reducing conditions yielded a single band of 230 kDa and 37.8 kDa, respectively, indicating presence of six identical monomers. pI of 4.4 and 8.02 % carbohydrate content in the enzyme were observed. Optimal temperature was 30oC, although the enzyme was active at 5-80 oC. Two pH optima, pH 2 and pH 8, were recorded and the enzyme was stable only at pH 2.0 for 24 h. Methylgallate recorded maximal affinity and K(m) and V(max) were recorded, respectively, as 1.9 X 10?3 M and 830 micronmol/min. Impact of several metal salts, solvents, surfactants, and typical enzyme inhibitors on tannase activity were determined to establish the novelty of the enzyme. Gene encoding tannase isolated from A. awamori is 1.232 kb and nucleic acid sequence analysis revealed an open reading frame consisting of 1122 bp (374 amino acids) of one stretch in -1 strand. In-silico analyses of gene sequences and comparison with reported sequences of other species of Aspergillus indicated that the acidophilic tannase from marine A. awamori is differs from that of other reported species.     

Separation and purification of useful proteins using hydrogel ultrafiltration

The hydrogel process is a different form of ultrafiltration and has been used to separate biological molecules. In this study, the gel pore size was predicted by pulse NMR technique and neural network using a data base obtained from gel filtration chromatography and diffusion experiment. Recombinant alkaline phosphatase expressed in insect cells was concentrated 1.5 times by hydrogel ultrafiltration by swelling at 20°C and collapsing at 35°C at 53–65% separation efficiency and 78–83% enzyme recovery. Wild and recombinantAutographa californica nuclear polyhedrosis viruses (AcNPV) were also concentrated 1.4 and 1.6 times of the feed solution at 48.5 and 60.0% separation efficiency, respectively. Hydrogel ultrafiltration appears to be an attractive alternative for the concentration of AcNPV and recombinant proteins from insect cells.     

Enhancement and inhibition of enzymes of heme metabolism by diethyl maleate in the rat kidney

The acylation of sn-glycerol 3-phosphate with palmityl-CoA was compared in mitochondria and microsomes isolated from rat liver. Polymyxin B, an antibiotic known to alter bacterial membrane structure, stimulated the mitochondrial glycerophosphate acyltransferase but inhibited the microsomal enzyme. When mitochondrial and microsomal fractions were incubated at 4–6 °C for up to 4 h, the mitochondrial enzyme remained virtually unchanged while the microsomal enzyme lost about one-half of its activity. Incubations at higher temperatures also revealed that the mitochondrial enzyme was comparatively more stable under the conditions employed. The mitochondrial acyltransferase showed no sensitivity to bromelain, papain, Pronase, and trypsin, all of which strongly inhibited the microsomal enzyme. The differential sensitivity to trypsin was observed in mitochondria and microsomes isolated from other rat organs. However, the liver mitochondrial glycerophosphate acyltransferase was inhibited by trypsin in the presence of either 0.05% deoxycholate or 0.1% Triton X-100. The trypsin sensitivity of the mitochondrial glycerophosphate acyltransferase in the presence of detergent was not due to the presence, in the mitochondrial fraction, of a trypsin inhibitor which became inactivated by Triton X-100 or deoxycholate. The results suggest that the catalytic site of mitochondrial glycerophosphate acyltransferase is not exposed to the cytosolic side and it is located in the inner aspect of the outer membrane.     

Modified simplified method for isolation of lysostaphin from the culture filtrate ofStaphylococcus staphylolyticus

The present paper reports a modified method for isolation of lysostaphin—a bacteriolytic agent with specific affinity for staphylococcal cell wall. The proposed purification scheme includes three steps. The first procedure is ultrafiltration through a membrane filter giving a yield of 75.6 %. The result of ultrafiltration is a concentrated, 10-times purified preparation of lysostaphin with specific activity 0.62 U/mg which can be used for digestion ofS. aureus cells. Further step, performed by ion-exchange chromatography on DEAE-cellulose, yields a 60-times purified preparation containing a mixture of enzyme components of lysostaphin. The yield of this step is 47.2 %, the preparation contains 3.54 U/mg protein. Using gel filtration on Sephadex G-50 a component with hexosaminidase activity was separated from the endopeptidase component on the basis of molar mass difference. A 270-times purified preparation of lysostaphin-endopeptidase with minimum of contaminating substances was obtained in this step. The yield of gel filtration was 22.1 %, specific activity increased up to 16.3 U/mg protein.     

Characterisation of cyclodextrin glucanotransferase fromBacillus circulans ATCC 21783 in terms of cyclodextrin production

Cyclodextrin glucanotransferase (CGTase, EC 2.4.1.19) fromBacillus circulans ATCC 21783 was purified by ultrafiltration and a consecutive starch adsorption. Total enzyme yield of 75.5% and purification factor of 13.7 were achieved. CGTase was most active at 65°C, possessed two clearly revealed pH-optima at 6.0 and 8.6 and retained from 75 to 100% of its initial activity in a wide range of pH, between 5.0 and 11.0. The cyclising activity was enhanced by 1 mM CaCl₂ or 4 mM CoCl₂. The enzyme was thermostable up to 70°C, and 64% of the original activity remained at 70°C after 30 min heat treatment. Up to 41% conversion into cyclodextrins was obtained from 40 g l^?1 starch without using any additives. This CGTase produced two types of cyclodextrins, beta and gamma, in a ratio 73:27 after 4 h reaction time at 65°C. This feature of the enzyme could be of interest for industrial cyclodextrin production.     

Indoleacetic Acid Oxidase: A Dual Catalytic Enzyme?

The isolation of a unique enzyme capable of oxidizing indoleacetic acid, but devoid of peroxidase activity, has been reported for preparations from tobacco roots and commercial horseradish peroxidase. Experiments were made to verify these results using enzyme obtained from Betula leaves and commercial horseradish peroxidase. Both indoleacetic acid oxidase and guaiacol peroxidase activity appeared at 2.5 elution volumes from sulfoethyl-Sephadex. These results were obtained with both sources of enzyme. In no case was a separate peak of indoleacetic acid oxidase activity obtained at 5.4 elution volumes as reported for the tobacco enzyme using the same chromatographic system. Both types of activity, from both sources of enzyme, also eluted together during gel filtration. Successful column chromatography of Betula enzyme was dependent upon previous purification by membrane ultrafiltration. These results indicate indoleacetic acid oxidase activity and guaiacol peroxidase activity are dual catalytic functions of a single enzyme.     

Partial purification and characterization of a novel Mg2+-dependent ATPase present in the cytosol from human erythrocytes

Mg2+-ATPase activity was identified in the cytosol of human erythrocytes. A partial purification of this activity was achieved by an initial DEAE-Sephadex column chromatography, followed by gel filtration on Sephadex G-100 and then a second DEAE-Sephadex chromatography procedure. The enzyme appeared in the void volume of the Sephadex G-100 column and was retained on an Amicon XM100A ultrafiltration membrane. The molecular weight of the enzyme was estimated to be 113 000 from SD gels. The above purification protocol yielded an enzyme with an optimal pH between 7.6 and 8.2. The enzyme activity increased linearly between 30 and 44 degrees C. It was stable for several months at -20 degrees C. Magnesium was essential for activity, but the rate attainable with Mn2+ was at least as great as that due to Mg2+. No other divalent cation was able to substitute for Mg2+ or Mn2+. Neither low nor high Ca2+ concentrations significantly affected the enzymatic activity. Substrate specificity studies showed that ATP was the preferred substrate followed by CTP (46% of the rate produced by ATP). Hydrolysis of GTP, UTP, ITP and ADP was less than 10% of the rate seen with ATP. No phosphatase, pyrophosphatase, phosphodiesterase, hexokinase, phosphofructokinase or adenylate cyclase activity could be detected in this enzyme preparation. Calmodulin, which stimulates the (Ca2+ + Mg2+)-ATPase of the human erythrocyte membrane, failed to enhance the Mg2+-ATPase activity. Of considerable interest, the activity of this Mg2+-ATPase was enhanced approximately 5-fold by low concentrations of mercuric ion, p-hydroxymercuribenzoate and DTNB, but was much less sensitive to iodoacetamide.     

Purification, biochemical and molecular characterization of a metalloprotease from Pseudomonas aeruginosa MN7 grown on shrimp wastes

A protease-producing bacterium was isolated and identified as Pseudomonas aeruginosa MN7. The strain was found to produce proteases when it was grown in media containing only shrimp waste powder (SWP), indicating that it can obtain its carbon, nitrogen, and salts requirements directly from shrimp waste. The use of 60 g/l SWP resulted in a high protease production. Elastase, the major protease produced by P. aeruginosa MN7, was purified from the culture supernatant to homogeneity using acetone precipitation, Sephadex G-75 gel filtration, and ultrafiltration using a 10-kDa cut-off membrane, with a 5.2-fold increase in specific activity and 38.4% recovery. The molecular weight of the purified elastase was estimated to be 34 kDa by sodium dodecyl sulfate-polyacrylamide gel electrophoresis and gel filtration. The optimum temperature and pH for protease activity were 60 degrees C and 8.0, respectively. The activity of the enzyme was totally lost in the presence of ethylene glycol tetraacetic acid, suggesting that the purified enzyme is a metalloprotease. The purified enzyme was highly stable in the presence of organic solvents, retaining 100% of its initial activity after 60 days of incubation at 30 degrees C in the presence of dimethyl sulfoxide and methanol. The lasB gene, encoding the MN7 elastase, was isolated and its DNA sequence was determined.     

Recovery of alkaline proteases by membrane filtration

This work describes the recovery of an extracellular alkaline protease from fermentation broths of a Bacillus sp ATCC 21536, at pH=10.0 using ultrafiltration (MWCO 100,000) and microfiltration (0.1 m) membranes in hollow fiber devices. The influence of membrane pore size and polymeric material and membrane filtration performance was studied. High protein recoveries and high average flux rates were obtained with polysulfone membranes. A decrease of concentration polarization was obtained, simultaneously with enhancement of filtration flux rate and enzyme recovery by using submicron sized charged particles. These polymers lead to flocculation and adsorption of whole cells and soluble factors from the fermentation broth. The best results were obtaiend by combination of cationic (0.1%) and anionic (0.04%) polymers.     

Intramodule pressure profiles and protein accumulation during tangential flow filtration

Tangential flow filtration (TFF) through a 30 kDa nominal molecular weight cut-off (MWCO) ultrafiltration membrane is widely employed to concentrate purified monoclonal antibodies (mAbs) to levels required for their formulation into injectable biologics. While TFF has been used to remove casein from milk for cheese production for over 35 years, and in pharmaceutical manufacture of biotherapeutic proteins for 20 years, the rapid decline in filtration rate (i.e., flux) at high protein concentrations is a limitation that still needs to be addressed. This is particularly important for mAbs, many of which are 140–160 kDa immunoglobulin G (IgG) type proteins recovered at concentrations of 200 mg/mL or higher. This work reports the direct measurement of local transmembrane pressure drops and off-line confocal imaging of protein accumulation in stagnant regions on the surface of a 30 kDa regenerated cellulose membrane in a flat-sheet configuration widely used in manufacture of biotherapeutic proteins. These first-of-a-kind measurements using 150 kDa bovine IgG show that while axial pressure decreases by 58 psi across a process membrane cassette, the decrease in transmembrane pressure drop is constant at about 1.2 psi/cm along the 20.7 cm length of the membrane. Confocal laser scanning microscopy of the membrane surface at the completion of runs where retentate protein concentration exceeds 200 mg/mL, shows a 50 μm thick protein layer is uniformly deposited. The localized measurements made possible by the modified membrane system confirm the role of protein deposition on limiting ultrafiltration rate and indicate possible targets for improving membrane performance.     

Trypsin purification by affinity binding to small unilamellar liposomes

A novel protein purification process using affinity-ligand-modified liposomes and membrane ultrafiltration is described. The feasibility of the process was tested using trypsin as the model protein and p-aminobenzamidine (PAB) as the affinity ligand for trypsin. The affinity liposomes were prepared by covalently attaching PAB to the surface of small unilamellar liposomes via the hydrophilic spacer arm diglycolic acid. The liposomes were comprised of dimyristoyl phosphatidyl choline, cholesterol, and dimyristoyl phosphatidyl ethanolamine to which the diglycolic acid was attached. The equilibrium binding constant between trypsin and immobilized PAB was shown to be dependent on the PAB density of the liposome surface. Bound trypsin was eluted from the liposomes by the trypsin inhibitor benzamidine. Trypsin was purified from a trypsin/chymotrypsin mixture and from one of its naturally occurring sources, porcine pancreatic extract. A recovery yield from the crude mixture of 68% was obtained with a trypsin purity of 98%. The affinity-modified liposomes were stable in the complex mixture and retained their trypsin binding capacity after multiple adsorption/elution cycles over a 30-day period.