Pilot plant recovery of catheptic proteases from surimi wash water

Recovery of bioactive compounds, such as proteolytic enzymes, from waste streams is a means to both recuperate value and reduce environmental pollution. Previously optimized lab-scale parameters for the recovery of a stable crude protease fraction from Pacific whiting (Merluccius productus) surimi wash water were tested using pilot plant equipment. Pretreatment of surimi wash water with 60 degrees C heat, acidification to pH 6, and centrifugation doubled ultrafiltration membrane flux and significantly improved protease purity by reducing a majority of the 35-205 kDa proteins. Concentrated crude protease obtained from wash water contained predominantly cathepsin L activity. Enzyme purity was increased about 100-fold, and yield was approximately 80%. Stability (frozen and freeze-dried protease) was maintained for 9 weeks at -80 degrees C. Freeze-dried preparations were also stable for 9 weeks at 4 and -15 degrees C. Successful application of pilot plant conditions allows for sufficient production of protease for further investigations into their applicability.     

A novel membrane based process to isolate photosystem-I membrane complex from spinach

The isolation of photosystem-I (PS-I) from spinach has been conducted using ultrafiltration with 300 kDa molecular weight cut-off polyethersulfone membranes. The effects of ultrafiltration operating conditions on PS-I activity were optimized using parameter scanning ultrafiltration. These conditions included solution pH, ionic strength, stirring speed, and permeate flux. The effects of detergent (Triton X-100 and n-dodecyl-beta-D-maltoside) concentration on time dependent activity of PS-I were also studied using an O₂ electrode. Under optimized conditions, the PS-I purity obtained in the retentate was about 84% and the activity recovery was greater than 94% after ultrafiltration. To our knowledge, this is the first report of the isolation of a membrane protein using ultrafiltration alone.     

Separation of monoclonal antibody alemtuzumab monomer and dimers using ultrafiltration

This article examines the feasibility of using ultrafiltration to separate the monomer of the monoclonal antibody alemtuzumab (Campath or Campath-1H) from a mixture of dimer and higher-order oligomers (collectively called "dimers" here). Using parameter scanning ultrafiltration, we initially assessed the suitability of the following membranes: 100 kDa and 300 kDa polyethersulfone (PES) membranes, and a 100 kDa polyvinylidene fluoride (PVDF) membrane. A detailed study was then carried out to examine the effects of operating conditions (such as solution pH, ionic strength, stirring speed, and permeate flux) on the separation of the monomer from the dimers using 300 kDa PES and 100 kDa PVDF membranes. Results of the experiments carried out in the carrier phase ultrafiltration (CPUF) mode indicate that the size-based protein-protein separation critically depends on the membrane used as well as the system hydrodynamics. The separation of the monoclonal antibody monomer and dimers using 100 kDa PVDF membranes in the diafiltration mode was also examined. Experimental results demonstrate that under suitable conditions, it is feasible to obtain the alemtuzumab monomer with a purity of more than 93% and a yield of more than 85% (from a mixture of 75% monomer and 25% dimers, which is the typical composition obtained after affinity chromatography). Simulation study indicates that this could be further improved to a purity of more than 96% and a monomer yield of more than 96% by increasing the selectivity of separation or by employing a two-stage diafiltration process.     

Fractionation of bovine serum albumin and monoclonal antibody alemtuzumab using carrier phase ultrafiltration

Protein transmission and hence selectivity of separation can be significantly affected by solution pH and ionic strength in protein fractionation using ultrafiltration. Using parameter scanning ultrafiltration, the transmission of bovine serum albumin (BSA) and monoclonal antibody alemtuzumab (Campath-1H) through 300 kDa polyethersulfone (PES) ultrafiltration membranes were studied over a range of pH and salt concentrations, with focus on the likely conditions for achieving "reverse selectivity," i.e., obtaining purified alemtuzumab (approximately 155 kDa) in the permeate. Experimental results demonstrate that the reverse selectivity could be obtained by manipulating the operating conditions such as the solution pH, ionic strength, permeate flux, and system hydrodynamics. With a two-stage batch ultrafiltration process under suitable conditions, the monoclonal antibody alemtuzumab with a purity of > 98% was obtained in the permeate from a feed solution initially containing 0.50 g/l each of BSA and alemtuzumab. Further purity can be expected by selecting more suitable membranes and optimizing operating conditions.     

Enzymes from isolates of Pseudomonas fluorescens involved in food spoilage

AIMS: Psychrotrophic Gram-negative bacteria, such as Pseudomonas species, pose a significant spoilage problem in refrigerated meat and dairy products due to secretion of hydrolytic enzymes, especially lipases and proteases. This study characterized the enzymes produced by strains of Pseudomonas fluorescens isolated from pasteurized milk. METHODS AND RESULTS: Thirty-seven isolates of Ps. fluorescens from skimmed, semiskimmed and whole milk were all shown to be proteolytic and lipolytic on casein and tributyrin agar, respectively. The highest level of protease production by one isolate, SMD 31, from skimmed milk was in minimal salts medium containing 1 mmol x l(-1) calcium chloride at 20 degrees C. The proteases belonged to the class of metallo-proteases, as there was no residual activity with 10 mmol x l(-1) EDTA. They were heat stable and retained activity even after treatment at 121 degrees C for 20 min. One protease of 45-48 kDa was detected in unconcentrated supernatant fluid samples but, in three isolates from different milk sources, five proteases with molecular masses between 28 and 48 kDa were detected on a 12% zymogram casein gel following ultrafiltration. Attempts to purify the lipases proved unsuccessful. CONCLUSIONS: The characteristics of the major protease of 45-48 kDa correspond to those of proteases described for other Pseudomonas species isolated from a range of environments. However, the smaller proteases have not been described previously. SIGNIFICANCE AND IMPACT OF THE STUDY: In the absence of ultrafiltration the presence of the minor protease species may be missed and they may act as contaminants of the major protease in unpurified or semipurified samples.     

Purification of lysozyme using ultrafiltration

This article examines the separation of lysozyme from chicken egg white by ultrafiltration with 25 kDa and 50 kDa MWCO polysulfone membranes. The effects of pH, system hydrodynamics, feed concentration, and transmembrane pressure on permeate flux, lysozyme transmission, purification factor, and productivity have been discussed. With both types of membranes, higher permeate flux and lysozyme transmission were observed at higher pH. Higher lysozyme purity was generally obtained with the 25 kDa MWCO membrane. Purity of lysozyme decreased when the feed concentration was increased. With the 50 kDa MWCO membrane permeate flux, productivity and the purity of lysozyme were found to increase with increase in transmembrane pressure. The possibility of using a two-step ultrafiltration process for achieving high productivity along with high purity of lysozyme was also investigated.     

Improvement of antioxidant activity of peptides with molecular weights ranging from 1 to 10 kDa by PEF technology

Egg white protein powder was hydrolyzed with Alcalase to produce antioxidant peptides. Then, the peptides were fractionated with ultrafiltration membranes. The peptides (1-10 kDa) were further treated by pulsed electric field (PEF) to investigate its effect on the antioxidant activity of the peptides. Antioxidant activity was evaluated using a 2,2-diphenyl-1-picrylhydrazyl (DPPH) radical inhibition assay. The results indicated that optimal electric field intensity and standing times of PEF can enhance the antioxidant activity of the peptides. Therefore, a Box-Behnken design (BBD) with three independent variables including concentration, electric field intensity and pulse frequency was used to establish the regression equation of second-order response surface. The optimal conditions were as follows: concentration 8 mg/ml, electric field intensity 10 kV/cm and pulse frequency 2400 Hz. Under these conditions, the peptides antioxidant activity was 62.64% ± 0.98%. The present study demonstrated that the antioxidant activity of peptides (1-10 kDa) could be improved using PEF.     

Anchorage-dependent growth factor(s) produced by rat sarcoma (XC) cells.

The autocrine growth factor(s) was isolated from serumfree conditioned medium of rat sarcoma (XC) cells. Autocrine activity was enriched by ultrafiltration using Amicon YM 10 membrane, extraction with 1 M acetic acid and partially purified (650-fold) by chromatography on Bio-Gel P-100 and P-60. The final recovery of the autocrine factor(s) was 4 micrograms from 1800 ml of the conditioned medium (a yield of 6%). The factor(s) with molecular weight 6-10 kDa was heat and acid stable but inactivated by trypsin and dithiothreitol. It stimulated anchorage-dependent (but not anchorage-independent) growth of XC cells as well as untransformed, established lines of rat (NRK) and mouse (3T3) cells. The results obtained may suggest that autocrine factor(s) produced by XC cells can be one of EGF-like or/and insulin-like growth factors.     

Inhibition, by a protease inhibitor, of the solubilization of the F1-portion of the Mg2+-stimulated adenosine triphosphatase of Escherichia coli.

The effects of two protease inhibitors on the solubilization of the membrane-bound Mg2+-adenosine triphosphatase (Mg-ATPase) of Escherichia coli were investigated. p-Aminobenzamidine prevented the solubilization of the Mg-ATPase during treatment of membranes with low-ionic-strength buffers containing ethylenediaminetetraacetic acid. p-Aminobenzamidine did not prevent subsequent solubilization of the Mg-ATPase by treatment of the membranes with chloroform. This method of solubilization yielded a preparation of similar apparent molecular weight but with a 10-fold-increased specific activity as compared with the Mg-ATPase solubilized by washing with low-ionic-strength buffer. However, in contrast to the latter preparation, the chloroform-solubilized Mg-ATPase did not reconstitute ATP-dependent energization of stripped membranes, which were prepared by low-ionic-strength washing in the absence of p-aminobenzamidine. Another protease inhibitor, epsilon-amino-n-caproic acid, did not effect the solubilization of the Mg-ATPase, but did inhibit the loss of activity occurring during concentration, by ultrafiltration, of the Mg-ATPase solublized by the low-ionic-strength treatment.     

Parameter scanning ultrafiltration: rapid optimisation of protein separation

High-resolution fractionation of proteins using ultrafiltration is feasible only at highly optimised conditions. Conventional process optimisation methodology demands both time and material. Pulsed sample injection ultrafiltration has been suggested as a rapid process optimisation technique. In the present work the scope of this technique is further extended by "parameter scanning ultrafiltration," which involves continuous change of a process parameter (e.g., pH, salt concentration). The time and material consumption are thus further reduced. The technique was validated using different proteins and membranes. Sieving coefficients at different pH and salt concentration were compared to those obtained in fixed parameter ultrafiltration experiments. As fractionation case studies the separation of monoclonal antibody from bovine serum albumin and separation of human IgG from human serum albumin were examined.     

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.     

Separation of human serum albumin and human immunoglobulins using carrier phase ultrafiltration

The fractionation of the plasma proteins human serum albumin (HSA) and human immunoglobulins (HIgG) using the combination of two newly developed techniques, pulsed sample injection technique and carrier phase ultrafiltration (CPUF), is discussed in this paper. The effects of pH and ionic strength on the transmission of a single protein (i.e., either HSA or HIgG) through 100 and 300 kDa MWCO polyethersulfone (PES) membranes were quantified using the pulsed sample injection technique. The experimental results thus obtained suggested that it would be possible to fractionate these proteins by optimizing the solution pH and ionic strength. With 100 and 300 kDa PES membranes, effective separation of HSA and HIgG was achieved by CPUF using suitable conditions, i.e., pH 4.7 and low salt concentration. The fractionation of HSA and HIgG by "reverse selectivity" using 300 kDa membranes was also examined.     

An acid protease in human erythrocytes and its localization in the inner membrane.

The isolation of erythrocytes of high purity from human blood was achieved by a combination of the two well established methods cells in erythrocyte preparations of different purities was studied. The acid protease activity was recovered to a level comparable with the recovery of erythrocytes, while the neutral protease activity as detected by the release of acid-soluble peptides from hemoglobin or casein disappeared in proportion to the removal of white blood cells. An acid protease was solubilized from the membranes of the purified erythrocytes by the extraction with 1-butanol. The enzyme was active in a pH range from 2 to 4, and sensitive to pepstatin. It was named pH-3 protease after its pH optimum. Sealed ghosts with right-side-out membranes and inside-out vesicles with reverted membranes were prepared from the purified erythrocytes and compared with respect to pH-3 protease activity for its latency as well as its inactivation by tryptic digestion. The results obtained indicate that pH-3 protase is localized on the inner surface of erythrocyte membranes. The self-digestion experiments at pH 4 using the sealed ghosts showed higher availability to pH-3 protease of spectrin and IVa protein than the other membrane proteins, also suggesting the localization of an acid protease in the inner membranes of erythrocytes.     

Massive breakdown of the Photosystem II polypeptides in a mutant of the cyanobacterium Synechocystis sp. PCC 6803

Degradation of the D1 protein of the Photosystem II (PS II) complex was studied in the Fad6/desA::Km^r mutant of a cyanobacterium Synechocystis sp. PCC 6803. The D1 protein of the mutant was degraded during solubilization of thylakoid membranes with SDS at 0°C in darkness, giving rise to the 23 kDa amino-terminal and 10 kDa carboxy-terminal fragments. Moreover, the D2 and CP43 proteins were also degraded under such conditions of solubilization. Degradation of the D2 protein generated 24, 17 and 15.5 kDa fragments, and degradation of the CP43 protein gave rise to 28, 27.5, 26 and 16 kDa fragments. The presence of Ca²⁺ and urea protected the D1, D2 and CP43 proteins against degradation. Degradation of the D1 protein was also inhibited by the presence of a serine protease inhibitor suggesting that the putative protease involved belonged to the serine class of proteases. The protease had the optimum activity at pH 7.5; it was active at low temperature (0°C) but a brief heating (65°C) during solubilization destroyed the activity. Interestingly, the protease was active in isolated thylakoid membranes in complete darkness, suggesting that proteolysis may be a non-ATP-dependent process. Proteolytic activity present in thylakoid membranes seemed to reside outside of the PS II complex, as demonstrated by the 2-dimensional gel electrophoresis. These results represent the first (in vitro) demonstration of strong activity of a putative ATP-independent serine-type protease that causes degradation of the D1 protein in cyanobacterial thylakoid membranes without any induction by visible or UV light, by active oxygen species or by any chemical treatments.     

Separation of proteases from yellowfin tuna spleen by ultrafiltration

Separation of protease, trypsin and chymotrypsin from yellowfin tuna spleen extract by ultrafiltration (UF) using regenerated cellulose membranes with molecular weight cut off (MWCO) 30 and 100 kDa was studied. The 100 kDa membrane had a higher transmission of enzymes than that of the 30 kDa membrane. The enzyme transmission varied from 0.01 to 0.18 and from 0.6 to 0.8 for the 30 kDa membrane and 100 kDa membrane, respectively. The protein transmission was about 0.8 for both membranes. Increasing cross-flow rate and transmembrane pressure (TMP) increased permeate flux. The limiting fluxes at cross-flow rate 120, 240 and 360 L/h for the 30 kDa membrane were 17.3, 43.9 and 54.7 L/m2h, respectively and the limiting fluxes at the same flow rate for 100 kDa membrane were 34.1, 51.1 and 68.4 L/m2h, respectively. The separation of these proteases was achieved using the 30 kDa membrane. The purities of proteases were increased more than ten times at TMP 1.5 bar and cross-flow rate 360 L/h by diafiltration using 30 kDa membrane.     

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.     

Clinical dextran purified by fractional ultrafiltration coupled with water washing

Dextran with extremely narrow molecular weight distribution (MWD) is demanded for clinical use. To elucidate the effect of fractional ultrafiltration on the purification of clinical dextran, a range of ultrafiltration membranes with 100, 30, 5 and 1 kDa molecular weight cut-off (MWCO) were applied. High Performance Gel Permeation Chromatography (HPGPC) analysis indicated that the MWD of ultrafiltrated dextran fractions are wide, with polydispersity index (D) between 2.2 and 5.4, suggesting that the MWD of dextran is hard to be strictly controlled by fractional ultrafitration. However, when coupled with water washing during ultrafiltration process, the homogeneity of dextran was greatly improved. An ultrafiltration fraction of 5-30 kDa (Mw ≈ 35 kDa) with narrow MWD (D = 1.2) was obtained after 5 times of water washing. The results show that fractional ultrafiltration coupled with water washing can be used as a simple and effective method to improve the quality of clinical dextran.     

Coupling of the Penicillium duponti acid protease to ethylene-maleic acid (1 : 1) linear copolymer. Preparation and properties of the water-soluble derivative.

The coupling of the thermostable acid protease (EC 3.4.23.-) of Penicillium duponti K 1014 to ethylene-maleic acid (1 : 1) linear copolymer in the presence of 1-cyclohexyl-3-(2-morpholinoethyl)-carbodiimide at pH 3.0, afforded a soluble enzyme derivative with a protein incorporation yield of 67% under optimal conditions. The protein content of the enzyme-polymer complex, the molecular weights of the reactants, and the mean value of 2.2 lysine residues per mol of enzyme found in amide linkage to the matrix, support a structure consisting of two polymer chains per mol of protease, each chain acylating a single lysine residue of the enzyme. The isoelectric point of the coupled enzyme was found to be 3,47, a value lower than that measured on the free protease (3.81). The specific activity of the bound protease against casein, at pH 3.7 and 30 degrees C, was 34% of that of the free enzyme, and at 75 degrees C increased to 70%. The increased size of the coupled enzyme resulted in an improved retention of activity by ultrafiltration membranes over that observed with free protease, alone or in admixture with ethylene-maleic acid copolymer. A water-soluble, coupled pepsin was prepared in 43% yield on protein basis by using the aminoethylmonoamide of ethylene-maleic acid copolymer and the same water-soluble carbodiimide.     

OmpT expression and activity increase in response to recombinant chloramphenicol acetyltransferase overexpression and heat shock in E. coli

The activity of a 35 kDa protease increased in response to induced expression of chloramphenicol acetyltransferase (CAT) in E. coli. This protease was partially purified, extensively characterized, and identified via the use of zymogram gels as the outer membrane protease, OmpT. In experiments targeting the overlap of well-characterized stress responses, OmpT activity was found to increase in response to heat shock but was only minimally affected by amino acid limitation. The largest increase in activity was found after induction of CAT. OmpT expression levels also increased in response to induction of recombinant CAT overexpression and heat shock. This is the first report of increased activity and expression of an outer membrane protease during cytoplasmic overexpression of a recombinant protein.     

超滤膜分离纯化珊瑚藻溴过氧化物酶

利用超滤膜对珊瑚藻中溴过氧化物酶(EC 1.11.1.18,分子质量740kDa)进行分离纯化,对膜的截留分子质量、操作压力、起始蛋白质浓度、搅拌速率、pH、离子强度等条件进行了优化。超滤分离纯化最优条件为:截留分子质量为100kDa的聚偏氟乙烯(PVDF)膜,操作压力为0.02MPa,搅拌速率为600r/min,起始蛋白质浓度为0.1g/L,pH=6.0。对粗酶液先进行热沉淀纯化,再进行超滤纯化,溴过氧化物酶被纯化了21倍,比活为212U/mg,酶活回收率为96%。