Anion-exchange Membrane Chromatography Research Articles

Membrane chromatography for AAV full capsid enrichment: Process development to scale up

The recent FDA approval of several adeno-associated virus (AAV)-based gene therapies is driving demand for AAV production. One of the biggest AAV manufacturing challenges is removing “empty” capsids, which do not contain the gene of interest. Anion exchange chromatography has emerged as the leading solution for scalable full capsid enrichment. Here we develop a process for the baseline separation of empty and full AAV capsids using anion exchange membrane chromatography. This process development approach utilized AAV serotypes 8 and 9 and traverses initial screening of separation conditions up to manufacturing-scale processes. Process development of a two-step elution was performed via response surface DoE, exploring conductivity and the length of the first elution step. The results from response surfaces were used to construct statistical models of the process operating space. These models provide optimal conditions for recovery and purity, both of which can exceed 70 %. Model predictions were then validated at small scale prior to scale-up. We present the results from our scale-up purification and show that purity and yield are consistent with the results obtained from the response surface model.

Purification of phage for therapeutic applications using high throughput anion exchange membrane chromatography

As cases of multidrug resistant bacterial infections increase, scientists and clinicians around the world are increasingly turning to bacteriophages as alternatives to antibiotics. Even though our understanding of phage has increased significantly since the early days of its discovery, over a century ago, the currently used tools and technologies for phage purification for therapeutic applications are severely limited. Bacteriophages are produced by bacterial cultures, and impurities such as endotoxins must therefore be removed before clinical use. We present an anion exchange bind-and-elute membrane chromatographic method for purifying T7 bacteriophage from Escherichia coli culture supernatant that removes undesirable impurities, while ensuring a high viable phage count in the purified product. Our method does not involve the use of chemicals such as organic solvents and caesium chloride that could typically leave residual toxicity in the final product. It also does not require expensive equipment, such as an ultracentrifuge. Using our method, that is based on an in-house designed membrane module, 65% of viable T7 phage was recovered, and up to 94% endotoxins could be removed. The method, which took approximately 15 min, is rapid and scalable, and produces quite pure bacteriophage samples in a single step. It therefore potentially represents a major improvement over the status quo, and shows the way ahead for streamlining phage manufacturing for therapeutic use.

Factors affecting robustness of anion exchange chromatography: Selective retention of minute virus of mice using membrane media

Mobile and stationary phase factors were investigated in order to identify conditions for effective capture of minute virus of mice (MVM), a potential adventitious contaminant in biomanufacturing, using anion exchange membrane chromatography (AEX). The initial study was conducted for Membrane A for a range of feed conditions using bovine serum albumin (BSA) as a model protein mimicking acidic host-cell proteins (HCPs) competitive for virus binding. The effects of pH (6–8), salt concentration (0–150 mM NaCl) and level of BSA (0–10 g/L) were systematically investigated. It was found that higher BSA concentration has the most negative impact on MVM binding followed by the increased conductivity of the feed solution. The effect of pH on MVM binding is also detected but has a less impact compared to other two factors in the range of feed conditions investigated. In addition to Membrane A, three other AEX membranes (Membrane B, C and D) were investigated for MVM binding at a selected feed condition. Based on properties of the membranes investigated, it was found that ligand charge density has the most significant impact on MVM binding performance of AEX membranes from stationary phase perspective.

Design and optimization of membrane chromatography for monoclonal antibody charge variant separation.

The manufacturing scale implementation of membrane chromatography to purify monoclonal antibodies has gradually increased with the shift in industry focus toward flexible manufacturing and disposable technologies. Membrane chromatography are used to remove process-related impurities such as host cell proteins (HCPs) and DNA, leachates, and endotoxins, with improved productivity and process flexibility. However, application of membrane chromatography to separate product-related variants such as charge variants has not gained major traction due to low-binding capacity. The work reported here demonstrates that a holistic process development strategy to optimize static binding (pH and salt concentration) and dynamic process (membrane loading, flowrate, and gradient length) parameters can alleviate the capacity limitations. The study employed high throughput screening tools and scale-down membranes for intermediate and polishing purification of the model monoclonal antibody. An optimized process consisting of anion exchange and cation exchange membrane chromatography reduced the acidic variants present in Protein A eluate from 89.5% to 19.2% with 71% recovery of the target protein. The membrane chromatography process also cleared HCP to below limit of detection with 6- to 30-fold higher membrane loading, compared to earlier reported values. The results confirm that membrane chromatography is effective in separating closely related product variants when supported by a well-defined process development strategy.

Novel anion exchange membrane chromatography method for the separation of empty and full adeno-associated virus.

A challenge in the production of recombinant Adeno-Associated Virus (AAV) for gene therapies is the presence of capsids that lack the required gene of interest. The impact of these empty vectors in therapies is not fully understood, however the ability to control the ratio of empty to full particles, which contain the genetic payload, is a necessary step in the purification of these viruses. In this study, a novel anion exchange chromatography elution method for enrichment of full AAV particles is demonstrated. A step gradient with small conductivity increases of around 1 mS cm-1 provides more efficient separation of empty and full AAV serotype 5 across membrane media as compared to conventional linear gradient method. The use of this approach in optimizing a simpler method for manufacturing processes and scalability to a larger chromatographic volume is explored. With this approach, the authors achieved greater than 4-fold enrichment of full capsids, to give a total of ≈50%-60% full capsids, using a 25mM Bis-Tris Propane pH 9.0 buffer system with NaCl as the eluting salt. Results suggest that this elution method can be implemented into a scalable process and can provide insight into development of elution methods for other AAV serotypes.

Proceedings of the 2019 Viral Clearance Symposium, Session 1: Viral Clearance Strategies and Case Studies.

Session 1 of the 2019 Viral Clearance Symposium proposed strategies to use prior knowledge for demonstrating robust viral clearance for biotechnologically produced recombinant proteins, such as monoclonal antibodies, and introduced methods for virus reduction applicable to recombinant adeno-associated virus (rAAV) vectors. Proposals for generic virus clearance claims were made for detergent inactivation with Triton CG-110, low pH inactivation, anion-exchange membrane chromatography, and virus filtration, and acceptance of these proposals were discussed. Furthermore, the development of an ASTM standard for retrovirus removal by small virus filters was presented, and it was found that updating and refining of conditions is still warranted. The current approach for log reduction value calculation by using the lower value from duplicate runs as worst case was questioned, and a modified concept was proposed. Finally, for rAAV vectors, several options for reduction of adventitious viruses were demonstrated such as 35 nm virus filtration, detergent inactivation, heat inactivation, and anion-exchange or affinity chromatography and were found to be feasible in order to satisfy the principles of ICH Q5A.

Empty and full separation of adeno-associated virus vectors by anion exchange membrane chromatography

Empty and full separation of adeno-associated virus vectors by anion exchange membrane chromatography

Evaluation of two-species binding model with anion-exchange membrane chromatography to predict pressure buildup during recovery of virus

Membrane chromatography is an emerging bioprocessing technology. This work aimed to determine the cause of pressure rise during the loading phase of a large-scale viral recovery process, through small-scale experimentation. Comparable pressure rise was observed at both small and large scales, using Sartobind® Q anion exchange membranes. By varying low rate and feed concentrations of virus and host cell DNA, a linear relation between Viral Dynamic Dynamic Binding Capacity (DBC) and pressure rise was observed when DNA levels exceeded 1 × 10−8 g/ml. A mathematical model, assuming an uncompetitive interaction between the two species in a representative pore, was developed to predict breakthrough from which DBC and then pressure rise was determined. The results matched experimental data quite well at low to moderate DBC values (ie <8 mg/ml membrane), and can be utilized to anticipate pressure rise when higher DNA levels give rise to problematic levels of pressure rise.

Selection of chromatographic methods for the purification of cell culture-derived Orf virus for its application as a vaccine or viral vector

In recent years, the Orf virus has become a promising tool for protective recombinant vaccines and oncolytic therapy. However, suitable methods for an Orf virus production, including up- and downstream, are very limited. The presented study focuses on downstream processing, describing the evaluation of different chromatographic unit operations. In this context, ion exchange-, pseudo-affinity- and steric exclusion chromatography were employed for the purification of the cell culture-derived Orf virus, aiming at a maximum in virus recovery and contaminant depletion. The most promising chromatographic methods for capturing the virus particles were the steric exclusion- or salt-tolerant anion exchange membrane chromatography, recovering 84 % and 86 % of the infectious virus. Combining the steric exclusion chromatography with a subsequent Capto™ Core 700 resin or hydrophobic interaction membrane chromatography as a secondary chromatographic step, overall virus recoveries of up to 76 % were achieved. Furthermore, a complete cellular protein removal and a host cell DNA depletion of up to 82 % was possible for the steric exclusion membranes and the Capto™ Core 700 combination.The study reveals a range of possible unit operations suited for the chromatographic purification of the cell culture-derived Orf virus, depending on the intended application, i.e. a human or veterinary use, and the required purity.

Adsorption of beta-lactoglobulin in anion exchange membrane chromatography versus the contacting mode and temperature

Adsorption of beta-lactoglobulin to strong anion exchange membranes was investigated using three different contacting modes (batch adsorption, radial and tangential flow), and by equilibrium adsorption isotherm, as a function of temperature. The maximum binding capacity (qmax) was: (1) higher at lower temperature for the isotherm where qmax = 1.08 mg/cm2 at 10 °C versus qmax = 0.82 mg/cm2 at 50 °C, (2) independent of temperature for batch adsorption where the average qmax = 0.82 mg/cm2, (3) higher at lower temperature for radial flow where qmax = 0.87 mg/cm2 at 15 °C versus qmax = 0.38 mg/cm2 at 50 °C. For tangential flow at 10 °C, qmax = 0.65 mg/cm2. Differences in qmax between the three contacting modes were minor compared to the differences in the mass transfer coefficients that were tenfold higher for tangential flow than for batch adsorption. This was attributed to convective flow in the membrane pores closest to the flow channel, and diffusive mass transfer in the membrane pores farthest from the flow channel. The present work is the first report of mass transfer coefficients in tangential flow adsorbers, and the first report on the effect of temperature on the binding capacity of beta-lactoglobulin to adsorptive membranes.

Removal process of prion and parvovirus from human platelet lysates used as clinical-grade supplement for ex vivo cell expansion

Background aimsPooled human platelet lysate (HPL) is becoming the new gold standard as supplement for ex vivo cell culture for clinical protocols. However, the risk of pathogen contamination of HPL increases with the platelet pool size. We hypothesized that hollow fiber anion exchange membrane chromatography using QyuSpeed D (QSD) could remove resistant and untested bloodborne pathogens, such as parvoviruses and prions, from HPL-supplemented growth media without substantially affecting their capacity to support ex vivo cell expansion. MethodsFrozen or thawed platelet concentrates were serum-converted and centrifuged for obtaining HPL that was added to various growth media (ca. 100 mL), filtered through a 0.6-mL QSD membrane and characterized for proteins, growth factors and chemical composition. Capacity to expand Chinese hamster ovary, periodontal ligament, gingival fibroblast cells and Wharton's jelly mesenchymal stromal cells was studied. Removal of porcine parvovirus (PPV) and of the 263K prion strain of hamster-adapted scrapie was studied by spiking experiments following international guidelines. ResultsQSD had minimal impact on HPL-supplemented medium composition in proteins, growth factors and chemical content, nor capacity to expand and differentiate cells. In addition, QSD could remove ≥5.58 log10 [TCID50/mL] and ≥3.72 log10 of PPV and the 263K prion, respectively. ConclusionsQSD hollow fiber chromatography can be used to improve the virus and prion safety of HPL-supplemented media to safely expand cells for clinical protocols. These data bring new perspectives for increasingly safer use of pooled HPL in cell therapy and regenerative medicine applications.

Modeling and simulation of anion-exchange membrane chromatography for purification of Sf9 insect cell-derived virus-like particles

Recombinant protein-based virus-like particles (VLPs) are steadily gaining in importance as innovative vaccines against cancer and infectious diseases. Multiple VLPs are currently evaluated in clinical phases requiring a straightforward and rational process design. To date, there is no generic platform process available for the purification of VLPs. In order to accelerate and simplify VLP downstream processing, there is a demand for novel development approaches, technologies, and purification tools. Membrane adsorbers have been identified as promising stationary phases for the processing of bionanoparticles due to their large pore sizes. In this work, we present the potential of two strategies for designing VLP processes following the basic tenet of ‘quality by design’: High-throughput experimentation and process modeling of an anion-exchange membrane capture step. Automated membrane screenings allowed the identification of optimal VLP binding conditions yielding a dynamic binding capacity of 5.7mg/mL for human B19 parvovirus-like particles derived from Spodoptera frugiperda Sf9 insect cells. A mechanistic approach was implemented for radial ion-exchange membrane chromatography using the lumped-rate model and stoichiometric displacement model for the in silico optimization of a VLP capture step. For the first time, process modeling enabled the in silico design of a selective, robust and scalable process with minimal experimental effort for a complex VLP feedstock. The optimized anion-exchange membrane chromatography process resulted in a protein purity of 81.5%, a DNA clearance of 99.2%, and a VLP recovery of 59%.

Directing membrane chromatography to manufacture α1-antitrypsin from human plasma fraction IV

The surging demand for plasma proteins, mainly driven by the growing market and the development of new therapeutic indications, is promoting manufacturers to improve the throughput of plasma proteins. Due to the inherent convective mass transfer, membrane chromatography has been proved to be an efficient approach for extracting a small amount of target proteins from large-volume feed. In this study, α1-antitrypsin (AAT) was extracted from human plasma fraction IV by a two-step membrane chromatography. An anion-exchange membrane chromatography (AEMC) was used to capture the plasma proteins in bind/elute mode, and the obtained effluent was further polished by a hydrophobic interaction membrane chromatography (HIMC) in flow-through mode. Under optimal conditions, the recovery and purity of AAT achieved 87.0% and 0.58 AAT/protein (g/g) by AEMC, respectively. After the precise polishing by HIMC, the purity of AAT was 1.22 AAT/protein (g/g). The comparison results showed that membrane chromatography outperformed column chromatography in both steps because of its high throughput. This two-step membrane chromatography could obtain an AAT recovery of 83.3% and an activity recovery of 91.4%. The outcome of this work not only offers an alternative process for protein purification from plasma, but also provides guidelines for manufacturing product from a large-volume feed with multi-components by membrane chromatography.

Enhanced sensitivity of an antibody competitive blocking enzyme-linked immunosorbent assay using Equine arteritis virus purified by anion-exchange membrane chromatography.

In an effort to improve a competitive blocking enzyme-linked immunosorbent assay (cELISA) for antibody detection to Equine arteritis virus (EAV), antigen purified by anion-exchange membrane chromatography capsule (AEC) was evaluated. Virus purification by the AEC method was rapid and easily scalable. A comparison was made between virus purified by the AEC method with that obtained by differential centrifugation based on the following: 1) the relative purity and quality of EAV glycoprotein 5 (GP5) containing the epitope defined by monoclonal antibody 17B7, and 2) the relative sensitivity of a commercial antibody cELISA with the only change being the 2 purified antigens. On evaluation by Western blot using GP5-specific monoclonal antibody 17B7, the AEC-purified EAV contained 86% GP5 monomer whereas the differentially centrifuged EAV contained <29% of the monomer. Improvement of analytical sensitivity without sacrifice of analytical specificity was clearly evident when cELISAs prepared with EAV antigen by each purification method were evaluated using 7 sensitivity and specificity check sets. Furthermore, the AEC-purified EAV-based cELISA had 30-40% higher agreement with the virus neutralization (VN) test than the cELISA prepared with differentially centrifuged EAV based on testing 40 borderline EAV-seropositive samples as defined by the VN test. In addition, the AEC-purified cELISA had highly significant (P = 0.001) robustness indicated by intra-laboratory repeatability and interlaboratory reproducibility when evaluated with the sensitivity check sets. Thus, use of AEC-purified EAV in the cELISA should lead to closer harmonization of the cELISA with the World Organization for Animal Health-prescribed VN test.

Optimization of lactoferrin and bovine serum albumin separation using ion-exchange membrane chromatography

Lactoferrin (LF), which is a high value minor whey protein, has recently received extensive attention from research scientists and industry due to its multifunction and potential therapeutic applications. In this study, the separation of two similar-sized proteins: bovine serum albumin (BSA) and LF was investigated using strong cation and anion exchange membrane chromatography (MC). Single protein and BSA–LF mixture adsorption were performed on Sartobind Q75 and S75 at pH between the LF and BSA isoelectric points. Identical breakthrough curves were obtained for both single protein and binary protein mixture, which suggests that there is no protein adsorption competition at the binding sites. The process optimization was further studied to yield optimum buffer and operating conditions. The highest BSA flux per membrane area (728.00gm−2h−1) was obtained using 100mM phosphate buffer solution at pH 6.0 on the cation exchange membrane, whereas LF was bound to the membrane with the dynamic binding capacity at 10% breakthrough (DBC10%) of about 60mg. On the anion exchange membrane, LF was collected in the effluent at the flux of 287.46gm−2h−1 using 5mM phosphate buffer at pH 6.0, while BSA was retained on the membrane with DBC10% equal to 60.96mg. The combination effect between pH change and hydrophobic interaction improved the eluted protein mass for both anion and cation exchangers. Furthermore, the completed separation cycle was operated with the Sartobind S75 device with a short process time of 34.19min and optimal LF productivity over 2628.84mgmL−1h−1. This study confirms the advantage of MC for the separation of biomolecules with similar molecular weight and different isoelectric points, such as BSA–LF mixture separation. This fast and effective protein separation method could be applied at an industry scale.

Removal of transmissible spongiform encephalopathy prion from large volumes of cell culture media supplemented with fetal bovine serum by using hollow fiber anion-exchange membrane chromatography.

Cases of variant Creutzfeldt-Jakob disease in people who had consumed contaminated meat products from cattle with bovine spongiform encephalopathy emphasize the need for measures aimed at preventing the transmission of the pathogenic prion protein (PrPSc) from materials derived from cattle. Highly stringent scrutiny is required for fetal bovine serum (FBS), a growth-medium supplement used in the production of parenteral vaccines and therapeutic recombinant proteins and in the ex vivo expansion of stem cells for transplantation. One such approach is the implementation of manufacturing steps dedicated to removing PrPSc from materials containing FBS. We evaluated the use of the QyuSpeed D (QSD) adsorbent hollow-fiber anion-exchange chromatographic column (Asahi Kasei Medical, Tokyo, Japan) for the removal of PrPSc from cell culture media supplemented with FBS. We first established that QSD filtration had no adverse effect on the chemical composition of various types of culture media supplemented with 10% FBS or the growth and viability characteristics of human embryonic kidney (HEK293) cells, baby hamster kidney (BHK-21) cells, African green monkey kidney (Vero) cells, and Chinese hamster ovary (CHO-k1) cells propagated in the various culture-medium filtrates. We used a 0.6-mL QSD column for removing PrPSc from up to 1000 mL of Dulbecco’s modified Eagle’s medium containing 10% FBS previously spiked with the 263K strain of hamster-adapted scrapie. The Western blot analysis, validated alongside an infectivity assay, revealed that the level of PrPSc in the initial 200mL flow-through was reduced by 2.5 to > 3 log10, compared with that of the starting material. These results indicate that QSD filtration removes PrPSc from cell culture media containing 10% FBS, and demonstrate the ease with which QSD filtration can be implemented in at industrial-scale to improve the safety of vaccines, therapeutic recombinant proteins, and ex vivo expanded stem cells produced using growth media supplemented with FBS.

A scalable method to concentrate lentiviral vectors pseudotyped with measles virus glycoproteins.

Lentiviral (LV) vectors have emerged as powerful tools for basic research and clinical applications because of their ability to stably transduce both dividing and nondividing cells. A wide range of viral envelope (Env) glycoproteins have the ability to associate with the membrane of LV vectors, a process that is referred to as pseudotyping. Pseudotyped vectors have the capacity to transduce specific cell types for specific applications. For example, LV vectors pseudotyped with the measles virus (MV)-derived hemagglutinin (H) and fusion (F) proteins have the ability to transduce quiescent lymphocytes. In addition, the MV H glycoprotein can be engineered allowing cell-specific targeting of LV vectors. One problem with MV glycoprotein-pseudotyped LV vectors is low titer during vector production. This results in the need to manufacture large volumes of the vectors and to concentrate them to appropriate titers. The commonly used centrifugation-based concentration techniques for LV vectors are not practical for large-scale vector manufacturing. Thus, there is a need for improved methods to concentrate LV vectors. In this study, we adapted an anion-exchange membrane chromatography method that we previously used in the context of LV vectors pseudotyped with the vesicular stomatitis virus glycoprotein to concentate MV glycoprotein-pseudotyped LV vectors. Up to 60% of the input vectors with an up to 5300-fold reduction in volume was achieved using this anion-exchange chromatography method in conjunction with a desalting/concentration step involving centrifugal filter units. This technique provides a rapid and scalable approach for concentrating MV-pseudotyped LV vectors that does not require an elaborate setup.

Human plasma-derived immunoglobulin G fractionated by an aqueous two-phase system, caprylic acid precipitation, and membrane chromatography has a high purity level and is free of detectable in vitro thrombogenic activity.

Instituto Clodomiro Picado has developed an immunoglobulin G (IgG) plasma fractionation process combining a polyethylene glycol/phosphate aqueous two-phase system (ATPS), caprylic acid precipitation and anion-exchange membrane chromatography. We evaluated the purity and in vitro thrombogenicity of such IgG, in line with current international requirements. Contributions of the different production steps to reduce thrombogenicity were assessed at 0·2l-scale, and then the methodology was scaled-up to a 10l-scale and final products (n=3) were analysed. Purity, immunoglobulin composition, and subclass distribution were determined by electrophoretic and immunochemical methods. The in vitro thrombogenic potential was determined by a thrombin generation assay (TGA) using a Technothrombin fluorogenic substrate. Prekallikrein activator (PKA), plasmin, factor Xa, thrombin and thrombin-like activities were assessed using S-2302, S-2251, S-2222, S-2238 and S-2288 chromogenic substrates, respectively, and FXI by an ELISA. The thrombogenicity markers were reduced mostly during the ATPS step and were found to segregate mostly into the discarded liquid upper phase. The caprylic acid precipitation eliminated the residual procoagulant activity. The IgG preparations made from the 10l-batches contained 100% gamma proteins, low residual IgA and undetectable IgM. The IgG subclass distribution was not substantially affected by the process. TGA and amidolytic activities revealed an undetectable in vitro thrombogenic risk and the absence of proteolytic enzymes in the final product. Fractionating human plasma by an ATPS combined with caprylic acid and membrane chromatography resulted in an IgG preparation of high purity and free of a detectable in vitro thrombogenic risk.

Separation and purification of linear covalently closed deoxyribonucleic acid by Q-anion exchange membrane chromatography

We have constructed an in vivo system for rapid, scalable production of linear covalently closed (LCC) DNA from precursor circular covalently closed (CCC) plasmid DNA (pDNA) that offers a stronger safety profile compared to conventional CCC pDNA vectors. In the processing of LCC DNA products from the precursor CCC pDNA, LCC minivector DNA is produced in addition to other precursor DNA species and isoforms. DNA purification by anion exchange chromatography (AEC) attains high vector purity, making it an efficient and valuable approach to purification processes for the production of clinical grade DNA. Membrane chromatography offers significant advantages over traditional column chromatography including large convective pores, higher binding capacities, high throughput, scalable purification processes, and disposability. A hydrogel-based strong Q-anion exchange membrane for anion exchange chromatography can bind DNA with high capacity and recovery upon purification. We exploited these membrane properties in the separation of DNA sizes and isoforms to purify LCC DNA. We employed a NaCl concentration gradient at varying flow rates to successfully achieve effective separation of parental supercoiled CCC pDNA from processed isogenic LCC derivatives generated by the LCC DNA vector production system. We propose that anion exchange membrane chromatography is well positioned to play an integral role in large scale LCC DNA vector purification, successfully separating vectors by DNA isoforms.

Simultaneous clarification of Escherichia coli culture and purification of extracellularly produced penicillin G acylase using tangential flow filtration and anion-exchange membrane chromatography (TFF-AEMC)

Downstream purification often represents the most cost-intensive step in the manufacturing of recombinant proteins since conventional purification processes are lengthy, technically complicated, and time-consuming. To address this issue, herein we demonstrated the simultaneous clarification and purification of the extracellularly produced recombinant protein by Escherichia coli using an integrated system of tangential flow filtration and anion exchange membrane chromatography (TFF-AEMC). After cultivation in a bench-top bioreactor with 1L working volume using the developed host/vector system for high-level expression and effective secretion of recombinant penicillin G acylase (PAC), the whole culture broth was applied directly to the established system. One-step purification of recombinant PAC was achieved based on the dual nature of membrane chromatography (i.e. microfiltration-sized pores and anion-exchange chemistry) and cross-flow operations. Most contaminant proteins in the extracellular medium were captured by the anion-exchange membrane and cells remained in the retentate, whereas extracellular PAC was purified and collected in the filtrate. The batch time for both cultivation and purification was less than 24h and recombinant PAC with high purity (19U/mg), yield (72% recovery), and productivity (41mg of purified PAC per liter of culture) was obtained. Due to the nature of the non-selective protein secretion system and the versatility of ion-exchange membrane chromatography, the developed system can be widely applied for effective production and purification of recombinant proteins.