Protein fouling of virus filtration membranes: effects of membrane orientation and operating conditions

The capacity of virus filters used in the purification of therapeutic proteins is determined by the rate and extent of membrane fouling. Current virus filtration membranes have a complex multilayer structure that can be used with either the skin-side up or with the skin-side facing away from the feed, but there is currently no quantitative understanding of the effects of membrane orientation or operating conditions on the filtration performance. Experiments were performed using Millipore's Viresolve 180 membrane under both constant pressure and constant flux operation with sulfhydryl-modified BSA used as a model protein. The capacity with the skin-side up was greater during operation with constant flux and at low transmembrane pressures, with the flux decline or pressure rise due primarily to osmotic pressure effects. In contrast, data obtained with the skin-side down showed a slower, steady increase in total resistance with the cumulative filtrate volume, with minimal contribution from osmotic pressure. The capacity with the skin-side down was significantly greater than that with the skin-side up, reflecting the different fouling mechanisms in the different membrane orientations. These results provide important insights for the design and operation of virus filtration membranes.     

Purification and properties of human serum cholinesterase

Cholinesterase was purified from human serum by a three-stage procedure involving chromatography on DEAE-cellulose at pH4.0, an electrofocusing technique and gel filtration on Sephadex G-200. The final product was purified 13000-fold with a yield of 54%, and only one protein and one cholinesterase band could be demonstrated by polyacrylamide-disc electrophoresis. The catalytic properties appeared to be unchanged by the purification procedure. The molecular weight was determined by both ultracentrifugation in a density gradient and gel filtration, and values close to 366000 were obtained. The isoelectric point of cholinesterase was estimated to be pH3.99. The method appears suitable for the preliminary purification of the rare genetic variants of human cholinesterase.     

Large scale preparation of pure hog kidney renin

The complete purification of renin raises difficult problems due to its extremely low concentration in kidney (less than 1/50,000 of total proteins). The complete purification of hog kidney renin has been realized on a large scale, starting from 300 kg of fresh hog kidneys. 14.6 mg of pure renin were obtained with an overall yield of 4%. The purification procedure involved 14 steps. The enzyme was extracted at pH 3.5. Subsequent purification steps were performed in the presence of protease inhibitors to decrease renin proteolysis. These steps included an ammonium sulfate precipitation and a batch-chromatography on DEAE-cellulose. The major purification step was an affinity chromatography on Sepharose-hexamethylene-diaminopepstatin. The enzyme obtained was further purified by molecular sieving gel filtration and isoelectric focusing.     

Separation of alpha-lactalbumin and beta-lactoglobulin using membrane ultrafiltration

There is considerable commercial interest in the preparation of individual whey proteins as high-value food additives, nutraceuticals, and therapeutics. This study examined the use of membrane filtration for the separation of alpha-lactalbumin and beta-lactoglobulin. Stirred cell filtration experiments were performed using both cellulosic and polyethersulfone membranes to determine the optimal pH, ionic strength, and filtration conditions. Selectivities of greater than 55 could be achieved at pH 5.5 and 50 mM ionic strength using a 30-kD cellulose membrane. A diafiltration process was then designed for the protein separation. A 16-diavolume filtration yielded beta-lactoglobulin as the retentate product with a purification factor of 100 and recovery of 90%. The alpha-lactalbumin was recovered in the filtrate with a purification factor of more than 10 and nearly 99% yield. Model calculations were in good agreement with the experimental data.     

Effect of divalent ions on protein precipitation with polyethylene glycol: mechanism of action and applications.

Polyethylene glycol (PEG) is extensively employed for protein purification by fractional precipitation. Efficiency of precipitation is highest when the solution pH is near the isoelectric point of the target protein. At pH values far from the isoelectric point of the target protein, proteins develop a net positive or negative charge and are not more resistant to precipitation. We have found that divalent cations (Ba2+, Sr2+, and Ca2+) or divalent anions (SO4(2-)) significantly change the pattern of PEG precipitation when the ion is chosen so as to counteract the expected net charge on the target protein. At moderate (5-50 mM) concentrations of Ba2+, negatively charged proteins can be precipitated from solution at pH values as high as 10 with efficiency unchanged from precipitation at pH values near their isoelectric point values. The mechanism of PEG precipitation of protein at these high pH values appears to be unchanged from the mechanism operative at the protein isoelectric point. Precipitation is rapid and the capacity for protein precipitation is high. There is no detectable coprecipitation of small molecules (AMP, ATP, and NADH) or soluble proteins (carbonic anhydrase) induced when large quantities of protein are precipitated by this method. The purification of bovine carbonic anhydrase from erythrocyte lysate is more efficient at pH 10 in the presence of Ba2+ than is conventional PEG precipitation carried out at the isoelectric point of carbonic anhydrase. Application of these observations should broaden the utility of protein purification by fractional precipitation with PEG.     

Modified method for production and purification of Staphylococcus aureus enterotoxin B.

A medium containing 4% bio-trypcase and 1% yeast extract was used for the production of Staphylococcus aureus enterotoxin B. The yield obtained was estimated at 200 micrograms of enterotoxin per ml of S. aureus S-6 culture supernatant. The purification method involves chromatography on Biorex 70 resin, isoelectric focusing, and gel filtration on Sephadex G-100. The purified enterotoxin (isoionic point, pH 8.55) was shown to be homogenous protein with a molecular weight of 29,000 when tested by gel electrophoresis.     

Effect of solution pH on protein transport through ultrafiltration membranes

Although a number of previous studies have demonstrated that solution pH can have a dramatic effect on protein transport through ultrafiltration membranes, the exact origin of this behavior has been unclear. Experimental data were obtained for the transport of a broad range of proteins with different surface charge and molecular weight. The effective hydrodynamic size of the proteins was evaluated using size‐exclusion chromatography. The membrane charge, both before and after exposure to a given protein, was evaluated using streaming potential measurements. In most cases, the electrostatic interactions were dominated by the distortion of the electrical double layer surrounding the protein, leading to a distinct maximum in protein transmission at the protein isoelectric point. Attractive electrostatic interactions did occur when the protein and membrane had a large opposite charge, causing a second maximum in transmission at a pH between the isoelectric points of the protein and membrane. The sieving data were in good agreement with theoretical calculations based on available models for the partitioning of charged solutes in cylindrical pores. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 64: 27–37, 1999.     

Purification and partial characterization of a cellular retinol-binding protein from human liver

A protein with binding specificity for retinol was purified from human liver. [³H]Retinol was added to liver extracts and the [³H]retinol-binding protein isolated by conventional chromatographic techniques including ion-exchange chromatography on DEAE-Sepharose, gel filtration on Sephadex G-75 and G-50 and preparative isoelectric focusing. The yield was 10–15% in different preparations and the degree of purification was about 3000-fold. The purified protein had a molecular weight of about 15 000 as estimated from both gel filtration and polyacrylamide gel electrophoresis in sodium dodecyl sulphate and was homogeneous in several electrophoretic systems. Isoelectric focusing of the purified protein gave a doublet band. Only one fluorescent band at pH 4.70 was seen if the protein solution was incubated with excess retinol prior to isoelectric focusing. The isolated protein did not react with antiserum to the retinol-binding protein of plasma. The amino acid composition and the amino terminal amino acid sequence for the first sixteen amino acids of the purified protein differed significantly from that of the plasma retinol-binding protein.     

Marke''s disease herpesviruses. III. Purification and characterization of Marek''s disease herpesvirus B antigen.

Sera from chickens naturally infected with Marek's disease herpesvirus (MDHV) form preciptin lines with at least two immunologically distinct soluble antigens designated MDHV-A and MDHV-B. Partial purification and characterization of the glycoprotein MDHV-A antigen was previously reported. MDHV-B was found predominantly in the sonically treated extracts of infected cells, in contrast to the predominantly extracellular MDHV-A. Analysis of these extracts from [14C]glucosamine-labeled cells by immunodiffusion with chicken anti MDHV-B serum negative for MDHV-A followed by autoradiography confirmed that MDHV-B was a common antigen between MDHV and herpesvirus of turkeys and revealed that it was also a glycoprotein. Because of their glycoprotein nature, both MDHV-A and MDHV-B bound to concanavalin A affinity chromatography columns and could then be eluted by alpha-methyl-D-mannoside and recovered for further analysis. Concanavalin A affinity chromatography was an excellent technique for initial purification of MDHV-A and MDHV-B, since approximately 5- and 15- fold purification, respectively, was achieved in a single simple step. MDHV-B was resistant to trypsin under conditions where MDHV-A was sensitive, but was similar to MDHV-A in resistance to pH 2.0 and to 1.0 or 2.0 M urea and 0.05% Brij 35. Partially purified MDHV-B was analyzed by sucrose gradient sedimentation, isoelectric focusing, and gel filtration on Sephadex G-200 in the presence of 1.0 or 2.0 M urea and 0.05% Brij 35 to purify the antigen and to determine its physical and chemical properties in comparison with those already reported for MDHV-A. MDHV-B had a much lower isoelectric point in pH 4,54, a higher sedimentation coefficient of 4.4S, and a greater molecular weight of 58,250. These data indicate that MDHV-B is physically distinct from MDHV-A antigen, although the size difference is not sufficient to allow for effective separation. In contrast, the isoelectric point difference of greater than 2 pH units makes isoelectric focusing an effective means of purifying the antigens free of one another. The four-step purification procedure achieved greater than 200-fold purification of MDHV-B. Immunization of rabbits with this highly purified antigen results in the preparation of antisera that appeared monospecific for MDHV-B in immunodiffusion.     

正辛酸沉淀在单克隆抗体纯化中的工艺优化与应用

为应对治疗性抗体快速增长的市场需求,抗体上游细胞培养规模和表达量水平已显著提高,而下游纯化工艺的生产效率则相对落后,下游处理能力已成为限制抗体产能的瓶颈。本研究以单克隆抗体mab-X为实验材料,优化了细胞培养液、低pH病毒灭活收集液2种模式的正辛酸(caprylic acid,CA)沉淀工艺条件,并研究了CA处理去除聚体、CA处理灭活病毒等2种应用,在小试的基础上,采用低pH病毒灭活收集液CA沉淀的模式进行了500 L细胞培养规模生产放大研究,对沉淀前后的产品质量和收率进行了检测和对比。结果显示,两种模式的CA沉淀均可显著降低宿主细胞蛋白(host cell protein,HCP)残留和聚体含量,在聚体去除实验中CA沉淀可去除约15%的聚体,病毒灭活研究显示CA对逆转录模型病毒具有完全的病毒灭活能力。在放大生产规模中,下游依次进行了深层过滤收获、亲和层析、低pH病毒灭活、CA沉淀及深层过滤、阳离子交换层析,CA沉淀过程中混合时间和搅拌速度显著影响CA沉淀效果,CA沉淀处理后低pH病毒灭活液中的HCP残留量降低了895倍,沉淀后产品纯度和HCP残留均已控制在单克隆抗体质量要求范围内,CA沉淀可以减少传统纯化工艺中的一个精纯步骤。总之,下游工艺中采用CA沉淀,能够精简传统纯化工艺,并完全满足mab-X的纯化质量要求,而且能提高生产效率、降低生产成本。本研究结果将推动CA沉淀在单克隆抗体下游纯化生产中的应用,为解决目前传统纯化工艺的问题提供参考。     

Effect of protein fouling on filtrate flux and virus breakthrough behaviors during virus filtration process

Virus filtration process is used to ensure viral safety in the biopharmaceutical downstream processes with high virus removal capacity (i.e., >4 log₁₀). However, it is still constrained by protein fouling, which results in reduced filtration capacity and possible virus breakthrough. This study investigated the effects of protein fouling on filtrate flux and virus breakthrough using commercial membranes that had different symmetricity, nominal pore size, and pore size gradients. Flux decay tendency due to protein fouling was influenced by hydrodynamic drag force and protein concentration. As the results of prediction with the classical fouling model, standard blocking was suitable for most virus filters. Undesired virus breakthrough was observed in the membranes having relatively a large pore diameter of the retentive region. The study found that elevated levels of protein solution reduced virus removal performance. However, the impact of prefouled membranes was minimal. These findings shed light on the factors that influence protein fouling during the virus filtration process of biopharmaceutical production.     

Purification of singly PEGylated α-lactalbumin using charged ultrafiltration membranes

One of the challenges in producing a PEGylated therapeutic protein is that the PEGylation reaction typically generates a mixture of both singly and multiply PEGylated species. The objective of this study was to examine the feasibility of using ultrafiltration for the purification of a singly PEGylated protein from the multiply PEGylated conjugates. Data were obtained with α‐lactalbumin that was PEGylated with a 20 kDa activated PEG, with the ultrafiltration performed over a range of pH and ionic strength using both unmodified and negatively charged composite regenerated cellulose membranes. Purification of the singly PEGylated α‐lactalbumin from the multiply PEGylated species was accomplished using a diafiltration process with a negatively charged membrane at pH 5 and an ionic strength of 0.4 mM, conditions that maximized the electrostatic exclusion of the multiply PEGylated species from the charged membrane. The diafiltration process provided more than 97% yield with greater than 20‐fold purification between the singly and doubly PEGylated proteins and nearly complete removal of the more heavily PEGylated species. The singly PEGylated α‐lactalbumin was recovered as a dilute filtrate solution, although this dilution could be eliminated using a cascade filtration or the final product could be re‐concentrated in a second ultrafiltration as part of the final formulation. These results demonstrate the feasibility of using ultrafiltration for the purification of singly PEGylated protein therapeutics. Biotechnol. Bioeng. 2011; 108:822–829. © 2010 Wiley Periodicals, Inc.     

Purification and Some Physical Properties of Acid-cellulase from Aspergillus niger

A cellulase preparation which exhibits the highest activity at a lower pH range, 2.3 to 2.5, was purified from a commercial cellulase preparation from a culture filtrate of Asp. niger and referred to as acid-cellulase.

The purification involves ammonium sulfate fractionation, gel filtration and ion-exchange and adsorption chromatographies. The purified enzyme was revealed to be homogenous in ultracentrifugation and disc as well as ampholine electrophoreses and to be an acidic protein of which isoelectric point lied at pH 3.3. The sedimentation coefficient and molecular weight were determined to be 3.27 S and 46,000, respectively. The optical properties were also studied.     

Purification and detection of multiple forms of histidine decarboxylase in rat gastric mucosa (author's transl)]

A specific histidine decarboxylase from rat gastric mucosa has been obtained at high purity and good yield (purification about 600-fold). The purification procedure included double (NH4)2SO4 fractionation, ion-exchange chromatography, preparative isoelectric focusing in a granulated gel and gel filtration. Only the specific histidine enzyme was obtained by that procedure; DOPA decarboxylase, a non-specific enzyme, was absent in our final preparation. Each step of the purification was visualized by polyacrylamide gel electrophoresis and analytical isoelectric focusing. The purified enzyme was apparently homogenous by criteria of electrophoresis and gel filtration and has a molecular weight of 94 000. Several protein bands appeared after isoelectric focusing and the enzyme activity was localized in 3 distinct peaks. The gastric enzyme consists of 3 active forms which could be distinguished by their isoelectric points: 5.4, 5.75 and 6. Moleculare weights estimated by SDS polyacrylamide gel electrophoresis were 97 000, 93 000 and 90 000, and no subunits were observed. Pyridoxal phosphate was required as a coenzyme and resolution of the holoenzyme agreed with a portion of the coenzyme tightly bound to the apoenzyme. The purified enzyme was stable at low ionic strength, near neutral pH; concentrated reducing agents inhibit the enzyme.     

A method for the purification of bovine somatomedin C

The large scale purification of bovine somatomedin C has been achieved using a protocol that includes cross-flow ultrafiltration of fresh bovine plasma, treatment of the concentrated plasma with formic acid and ethanol, removal of the insoluble material by high speed centrifugation, cross-flow ultrafiltration of the formic acid and ethanol-soluble proteins, ion exchange chromatography, gel filtration and preparative isoelectric focusing. Thirty L of bovine plasma containing 2.16 kg protein were processed to yield approximately 170 micrograms of highly purified bovine somatomedin C. This represents an 840,000-fold purification of this peptide. The purified peptide has a molecular weight of 10,200 daltons, an isoelectric point of 8.5 and a specific activity of 11,750 Units/mg protein.     

Purification and partial characterization of a cohaemolysin (CAMP-factor) produced by Streptococcus canis

Abstract A cohaemolysin from the culture supernate of a canine pathogenic group G streptococcus ( S. canis ) was purified to electrophoretic homogeneity. The purification procedure involved ammonium sulphate precipitation, ultrafiltration, gel filtration and preparative isoelectric focusing. The cohaemolysin consisted of a single polypeptide chain, 18.6 kDa, with an isoelectric point at pH 5.1. The protein reacted with an homologous anti-serum, appeared to be trypsin-sensitive and relatively heat-stable. The cohaemolysin did not show any non-specific IgG binding activities.     

Affinity purification and properties of cathepsin-E-like acid proteinase from rat spleen.

A unique acid proteinase different from cathepsin D was purified from rat spleen by a method involving precipitation at pH 3.5, affinity chromatography on pepstatin-Sepharose 4B and concanavalin A-Sepharose 4B, chromatography on Sephadex G-100 and DEAE-Sephacel, and isoelectric focusing. A purification of 4200-fold over the homogenate was achieved and the yield was 11%. The purified enzyme appeared to be homogeneous on electrophoresis in polyacrylamide gels. The isoelectric point of the enzyme was determined to be 4.1-4.4. The enzyme hydrolyzed hemoglobin with a pH optimum of about 3.1. The molecular weight of the enzyme was estimated to be about 90000 by gel filtration on Sephadex G-100. In sodium dodecylsulfate polyacrylamide gel electrophoresis, the purified enzyme showed a single protein band corresponding to a molecular weight of about 45000. The hydrolysis of bovine hemoglobin by the enzyme was much higher than that of serum albumin. Various synthetic and natural inhibitors of the enzyme were tested. The enzyme was inhbited by Zn2+, Fe3+, Pb2+, cyanide, p-chloromercuribenzoate, iodoacetic acid and pepstatin, whereas 2-mercaptoethanol, phenylmethyl-sulfonyl fluoride and leupeptin showed no effect.     

Evaluation of the effects of the parameters involved in the purification of clavulanic acid from fermentation broth by aqueous two-phase systems

The purification of clavulanic acid (CA), which is an important β-lactam antibiotic produced by submerged cultivation of Streptomyces clavuligerus, was studied through the use of phosphate and polyethylene glycol-based aqueous two-phase systems. The parameters’ effect on the yield and purification was evaluated through an experimental design and the preliminary results showed that the polyethylene molecular mass and tie-line length and phase volume ratio exerted the strongest effect on the yield and distribution coefficient in the range tested. In addition, the response surface methodology was used to optimize the distribution coefficient, yield, and purification factor. The optimal conditions of yield and purification factor are in the regions where polyethylene has a low molecular mass, pH close to the isoelectric point, and lower top phase volume. A 100% yield and a 1.5-fold purification factor are obtained when extracting CA by maximizing the conditions of an aqueous two-phase system.     

An improved purification procedure for rat liver lysosomal phospholipase A1

A purification procedure is presented for the isolation of lysosomal acid phospholipase A1 (PLA1) from livers of non-pretreated rats, in a high yield and purity. The purification starts from a crude mitochondrial-lysosomal fraction. PLA1 is solubilised and subsequently purified by chromatography on concanavalin A-Sepharose, by chromatofocusing, and by gel filtration. After chromatofocusing, the enzyme is already purified 50200-fold with a yield of 50%, and after gel filtration 56600-fold with a yield of 7%. Purified PLA1 exhibits a specific activity of approx. 8.2 mumol phosphatidylethanolamine (preferred substrate) hydrolysed per min per mg protein, and upon chromatofocusing an apparent isoelectric point of 5.3 Gel filtration of purified PLA1 suggests a molecular mass of about 29 kDa, whereas in SDS-PAGE two proteins of 27 kDa and 55 kDa (mass ratio about 1/2) were visualised.     

Extraction and partial purification of mouse uterine alkaline phosphatase.

Alkaline phosphatase in uterine homogenates from day 7 pregnant mice was solubilized using 0.2% (v/v) Triton X-100 and extracted wtih 20% (v/v) n-butanol. The procedure, which resulted in 182-fold purification, included ammonium sulfate precipitation, DEAE-cellulose anion exchange chromatography and Sephadex G200 gel filtration. Solubilization with Triton X-100 was an important step in the procedure since extraction with n-butanol alone only partially solubilized the enzyme and gave low extraction yields, much of the enzyme activity remaining in association with negatively charged residues. However, butanol extraction of Triton X-100-treated homogenates gave high yields of enzyme and eliminated p-nitrophenyl phosphatases which displayed activity in the pH range 3.0--7.5, together with a large proportion of inactive protein. The activity of the purified enzyme preparations was electrophoretically homogeneous on cellulose acetate membranes, suggesting that the alkaline phosphatase in the mouse uterus exists in a single isozymic form. Polyacrylamide-gel electrophoresis revealed that the purified preparations contained at least one protein as an impurity. Attempts to further purify the alkaline phosphatase by isoelectric focusing were unsuccessful since the enzyme was found to have an isoelectric point of about 5.0 and at this pH it was rapidly inactivated.