Structural and performance characteristics of representative anion exchange resins used for weak partitioning chromatography

Weak partitioning chromatography (WPC) has been proposed for the purification of monoclonal antibodies using an anion exchange (AEX) resin to simultaneously remove both acidic and basic protein impurities. Despite potential advantages, the relationship between resin structure and WPC performance has not been evaluated systematically. In this work, we determine the structure of representative AEX resins (Fractogel® EMD TMAE HiCap, Q Sepharose FF, and POROS 50 HQ) using transmission electron microscopy and inverse size exclusion chromatography and characterize protein interactions while operating these resins under WPC conditions using two mAb monomers, a mAb dimer, mAb multimers, and BSA as model products and impurities. We determine the isocratic elution behavior of the weakly bound monomer and dimer species and the adsorptive and mass transfer properties of the strongly bound multimers and BSA by confocal laser scanning microscopy. The results show that for each resin, using the product K_p value as guidance, salt, and pH conditions can be found where mAb multimers and BSA are simultaneously removed. Isocratic elution and adsorption mechanisms are, however, different for each resin and for the different components. Under WPC conditions, the Fractogel resin exhibited very slow diffusion of both mAb monomer and dimer species but fast adsorption for both mAb multimers and BSA with high capacity for BSA, while the Sepharose resin, because of its small pore size, was unable to effectively remove mAb multimers. The POROS resin was instead able to bind both multimers and BSA effectively, while exhibiting a greater resolution of mAb monomer and dimer species. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:425–434, 2017     

Enhancing Protein A performance in mAb processing: A method to reduce and rapidly evaluate host cell DNA levels during primary clarification

The use and impact of 3M™ Emphaze™ AEX Hybrid Purifier, a single-use, fully synthetic chromatographic product, was explored to reduce host cell DNA (HC-DNA) concentration during the primary clarification of a monoclonal antibody (mAb). An approximately 5-log reduction in HC-DNA was achieved at an Emphaze AEX Hybrid Purifier throughput of 200 L/m². The appreciable reduction in HC-DNA achieved during primary clarification enhanced Protein A chromatography performance, resulting in a sharper and narrower elution profile. In addition, a 24× improvement in host cell protein (HCP) removal and fewer impurities nonspecifically bound to the Protein A column were observed compared to those resulting from the use of depth filtration for clarification. The use of a rapid, qualitative acidification assay to facilitate HC-DNA monitoring was also investigated. This assay involves the acidification-induced precipitation of HC-DNA, enabling the easy and rapid detection of DNA breakthrough across purification media such as Emphaze AEX Hybrid Purifier by means of turbidimetric and particle size measurements.     

Anion exchange chromatography provides a robust, predictable process to ensure viral safety of biotechnology products

The mammalian cell-lines used to produce biopharmaceutical products are known to produce endogenous retrovirus-like particles and have the potential to foster adventitious viruses as well. To ensure product safety and regulatory compliance, recovery processes must be capable of removing or inactivating any viral impurities or contaminants which may be present. Anion exchange chromatography (AEX) is a common process in the recovery of monoclonal antibody products and has been shown to be effective for viral removal. To further characterize the robustness of viral clearance by AEX with respect to process variations, we have investigated the ability of an AEX process to remove three model viruses using various combinations of mAb products, feedstock conductivities and compositions, equilibration buffers, and pooling criteria. Our data indicate that AEX provides complete or near-complete removal of all three model viruses over a wide range of process conditions, including those typically used in manufacturing processes. Furthermore, this process provides effective viral clearance for different mAb products, using a variety of feedstocks, equilibration buffers, and different pooling criteria. Viral clearance is observed to decrease when feedstocks with sufficiently high conductivities are used, and the limit at which the decrease occurs is dependent on the salt composition of the feedstock. These data illustrate the robust nature of the AEX recovery process for removal of viruses, and they indicate that proper design of AEX processes can ensure viral safety of mAb products.     

The effect of protein a cycle number on the performance and lifetime of an anion exchange polishing step

Most mAb platform purification processes consist of an affinity capture step followed by one or two polishing steps. An understanding of the performance linkages between the unit operations can lead to robust manufacturing processes. In this study, a weak‐partitioning anion‐exchange chromatography polishing step used in a mAb purification process was characterized through high‐throughput screening (HTS) experiments, small‐scale experiments including a cycling study performed on qualified scale‐down models, and large‐scale manufacturing runs. When material from a Protein A column that had been cycled <10× was loaded on the AEX resin, early breakthrough of impurities and premature loss of capacity was observed. As the cycle number on the Protein A resin increased, the capacity of the subsequent AEX step increased. Different control strategies were considered for preventing impurity breakthrough and improving AEX resin lifetimes. Depth filtration of the Protein A peak pool significantly improved the AEX resin capacity, robustness, and lifetime. Further, the turbidity of the Protein A pool has the potential for use as an in‐process control parameter for monitoring the performance of the AEX step. Biotechnol. Bioeng. 2013; 110: 1142–1152. © 2012 Wiley Periodicals, Inc.     

Development of a modular virus clearance package for anion exchange chromatography operated in weak partitioning mode

Anion exchange chromatography (AEX) operated under weak partitioning mode has been proven to be a powerful polishing step as well as a robust viral clearance step in Pfizer's monoclonal antibody (mAb) platform purification process. A multivariate design of experiment (DoE) study was conducted to understand the impact of operating parameters and feedstream impurity levels on viral clearance by weak partitioning mode AEX. Bacteriophage was used initially as a surrogate for neutral and acidic isoelectric point mammalian viruses (e.g., retrovirus and parvovirus). Five different mAbs were used in the evaluation of process parameters such as load challenge (both product and impurities), load pH, load conductivity, and contact time (bed height and flow‐rate). The operating ranges obtained from phage clearance studies and Pfizer's historical data were used to define an appropriate operating range for a subsequent clearance study with model retrovirus and parvovirus. Both phage and virus clearance evaluations included feedstreams containing different levels of impurities such as high molecular mass species (HMMS), host cell proteins (HCPs), and host cell DNA. For all the conditions tested, over 5 log₁₀ of clearance for both retrovirus and parvovirus was achieved. The results demonstrated that weak partitioning mode AEX chromatography is a robust step for viral clearance and has the potential to be included as part of the modular viral clearance approach. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:750–757, 2015     

药用级微生物谷氨酰胺转胺酶的纯化工艺研究

为了提高谷氨酰胺转胺酶的纯度和扩展在医药领域的应用,探索了一种适合工业化生产的、安全高效的微生物谷氨酰胺转胺酶纯化方法。轮枝链霉菌发酵后,经离心10 000 r/min 4℃除去菌体,调节发酵液电导率至4.1mS/cm和pH6.0后,以直线流速60cm/h通过SP Sepharose FF阳离子交换层析柱对目的蛋白高 选择性和高载量地捕获,再通过phenyl sepharose 6 FF（high sub）疏水层析柱进行精细纯化。纯化后经SDS-PAGE鉴定纯度达到95%以上,HPLC分析纯度> 99%。鲎试剂测定内毒素含量为0.013EU/ml,达到中国药典中血制品要求的低于0.15EU/ml标准。     

Investigating the combination of single-pass tangential flow filtration and anion exchange chromatography for intensified mAb polishing

There is growing interest within the biopharmaceutical industry to improve manufacturing efficiency through process intensification, with the goal of generating more product in less time with smaller equipment. In monoclonal antibody (mAb) purification, a unit operation that can benefit from intensification is anion exchange (AEX) polishing chromatography. Single-pass tangential flow filtration (SPTFF) technology offers an opportunity for process intensification by reducing intermediate pool volumes and increasing product concentration without recirculation. This study evaluated the performance of an AEX resin, both in terms of host cell protein (HCP) purification and viral clearance, following concentration of a mAb feed using SPTFF. Results show that preconcentration of AEX feed material improved isotherm conditions for HCP binding, resulting in a fourfold increase in resin mAb loading at the target HCP clearance level. Excellent clearance of minute virus of mouse and xenotropic murine virus was maintained at this higher load level. The increased mAb loading enabled by SPTFF preconcentration effectively reduced AEX column volume and buffer requirements, shrinking the overall size of the polishing step. In addition, the suitability of SPTFF for extended processing time operation was demonstrated, indicating that this approach can be implemented for continuous biomanufacturing. The combination of SPTFF concentration and AEX chromatography for an intensified mAb polishing step which improves both manufacturing flexibility and process productivity is supported.     

Multiblock Copolymers with Highly Sulfonated Blocks Containing Di‐ and Tetrasulfonated Arylene Sulfone Segments for Proton Exchange Membrane Fuel Cell Applications

Multiblock copoly(arylene ether sulfone)s with different block lengths and ionic contents are tailored for durable and proton‐conducting electrolyte membranes. Two series of fully aromatic copolymers are prepared by coupling reactions between non‐sulfonated hydrophobic precursor blocks and highly sulfonated hydrophilic precursor blocks containing either fully disulfonated diarylsulfone or fully tetrasulfonated tetraaryldisulfone segments. The sulfonic acid groups are exclusively introduced in ortho positions to the sulfone bridges to impede desulfonation reactions and give the blocks ion exchange capacities (IECs) of 4.1 and 4.6 meq. g^?1, respectively. Solvent cast block copolymer membranes show well‐connected hydrophilic nanophase domains for proton transport and high decomposition temperatures above 310 °C under air. Despite higher IEC values, membranes containing tetrasulfonated tetraaryldisulfone segments display a markedly lower water uptake than the corresponding ones with disulfonated diarylsulfone segments when immersed in water at 100 °C, presumably because of the much higher chain stiffness and glass transition temperature of the former segments. The former membranes have proton conductivities in level of a perfluorosulfonic acid membrane (NRE212) under fully humidified conditions. A membrane with an IEC of 1.83 meq. g^?1 reaches above 6 mS cm^?1 under 30% relative humidity at 80 °C, to be compared with 10 mS cm^?1 for NRE212 under the same conditions.     

Hypothermic storage of sheep embryos with antifreeze proteins: development in vitro and in vivo

Antifreeze proteins (AFPs) non-colligatively lower the freezing point of aqueous solutions, block membrane ion channels and thereby confer a degree of protection during cooling. Ovine embryos following prolonged hypothermic storage were used to determine 1) the type and concentration of a group of AFPs that can confer hypothermic tolerance, 2) the storage temperature, 3) the cooling rate, and 4) the in vitro and in vivo viability. In Experiment 1, Grade 1 and 2 embryos produced following superovulation were either cultured fresh (control) or stored at 4 degrees C for 4 d in media containing protein from 1 of 3 sources: Winter Flounder (WF; AFP Type 1); Ocean Pout (OP; AFP Type 3) at a concentration of 1 or 10 mg/ml; or bovine serum albumen (BSA) at 4 mg/ml in phosphate buffered saline (PBS). Following 72 h of culture, the viability rates were not different between controls (18 21 ); BSA (9 15 ); WF at 1 mg/ml (14 15 ); WF at 10 mg/ml (13 15 ) or OP at I mg/n-d (15 21 ), but were decreased (P < 0.05) in embryos stored in OP at 1 0 mg/ml (I 1 20 ). Pooled data showed higher (P < 0.05) viability rates for WF (27 30 ) than for OP (26 41 ) or BSA (9 15 ). There was no effect of protein source on hatching rates, but mean hatched diameters of embryos were lower (P < 0.05) following storage in BSA. In Experiment 2, Grade I to 3 embryos were either cultured fresh or stored for 4 d at 0 degrees or 4 degrees C in 4 mg/n-d BSA or 1 mg/ml WF. Embryos stored in WF at 4 degrees C (WF/4 degrees C) had comparable hatching rates (8 12 ) to that of controls (10 10 ), but embryos in the other treatments (WF 0 degrees C, 5 11 , BSA 4 degrees C, 6 11 and BSA 0 degrees C, 3 10 ) had significantly lower hatching rates (P < 0.01) compared with controls. Hatched diameters were comparable between controls and embryos stored in WF 4 degrees C, but embryos stored in WF 0 degrees C and BSA at both temperatures had smaller diameters (P < 0.05). In Experiment 3, Grade 1 to 3 embryos were either transferred fresh or were stored for 4 d at 4 degrees C in 4 mg/ml BSA or 1 mg/ml WF at different cooling rates (T1, BSA > 2 degrees C/min; T2, WF > 2 degrees C/min and T3, WF < 1 degrees C/min) prior to transfer. There were no differences in the number of ewes pregnant (T1, 10 1 1; T2, 6 10 and T3, 8 10 ) or in the number of viable fetuses recovered per treatment (T1, 14 25 ; T2, 10 1 4 and T3, 15 2 1) to indicate a negative effect of cooling rate or protein on embryo survival. In conclusion, ovine embryos can be stored in WF or BSA at 4 degrees C for 4 d, yielding similar pregnancy and embryo survival rates as fresh embryos following transfer to recipient ewes.     

Advective hydrogel membrane chromatography for monoclonal antibody purification in bioprocessing

Protein A chromatography is widely employed for the capture and purification of monoclonal antibodies (mAbs). Because of the high cost of protein A resins, there is a significant economic driving force to seek new downstream processing strategies. Membrane chromatography has emerged as a promising alternative to conventional resin based column chromatography. However, to date, the application has been limited to mostly ion exchange flow through (FT) mode. Recently, significant advances in Natrix hydrogel membrane has resulted in increased dynamic binding capacities for proteins, which makes membrane chromatography much more attractive for bind/elute operations. The dominantly advective mass transport property of the hydrogel membrane has also enabled Natrix membrane to be run at faster volumetric flow rates with high dynamic binding capacities. In this work, the potential of using Natrix weak cation exchange membrane as a mAb capture step is assessed. A series of cycle studies was also performed in the pilot scale device (> 30 cycles) with good reproducibility in terms of yield and product purities, suggesting potential for improved manufacturing flexibility and productivity. In addition, anion exchange (AEX) hydrogel membranes were also evaluated with multiple mAb programs in FT mode. Significantly higher binding capacity for impurities (support mAb loads up to 10Kg/L) and 40X faster processing speed were observed compared with traditional AEX column chromatography. A proposed protein A free mAb purification process platform could meet the demand of a downstream purification process with high purity, yield, and throughput. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:974–982, 2015     

Effect of Electrical Conductivity and Silicate on Infection of Basil with Colletotrichum gloeosporioides in Soilless Culture

The aim of this study was to evaluate the effect of potassium silicate administration and of electrical conductivity of nutrient solution in three experiments against Colletotrichum gloeosporioides infection on basil (Ocimum basilicum L. cv Genovese Gigante) grown in a closed soilless system. Potassium silicate was added at 100 mg/l of nutrient solution at three different levels of electrical conductivity: 1.5–1.6 mS/cm (E.C.1), 3–3.2 mS/cm (E.C.2, 0.70 g/l NaCl) and 4–4.2 mS/cm (E.C.3, 0.95 g/l NaCl). Basil plants were inoculated with C. gloeosporioides spores 21–31 days after sowing or placing the pots on the channels, applying 5 ml of conidial suspension to each treatment. The increased electrical conductivity of the nutrient solution generally reduced the incidence and severity of the disease, with the highest electrical conductivity (E.C.3) providing the best results. The addition of potassium silicate to the different nutrient solutions showed a significant reduction in both incidence and severity of the disease compared to a solution without silicate and the best results were given by the addition of silicate with the highest electrical conductivity (E.C.3) in all the trials carried out. The combination of high electrical conductivity and potassium silicate supplied gave good results. The possibility and benefits of applying Si amendments in practice are examined.     

Evaluation of a new assay for HBV DNA quantitation in patients with chronic hepatitis B

Background: The Amplicor™ HBV Monitor Test for quantitative determination of serum hepatitis B virus (HBV) DNA has recently been introduced. This assay is based on PCR and a non-radioactive hybridization and detection system on microwell plates.Objective: The performance of the Amplicor™ HBV Monitor Test was evaluated in a routine diagnostic laboratory. The Amplicor™ HBV Monoitor assay was compared to the Digene Hybrid Capture™ System HBV DNA assay for the quantitation of HBV in patient sera.Study design: Sensitivity and reproducibility were determined with 10-fold dilution series of two Eurohep HBV reference plasma specimens. Furthermore, 196 sera from 14 children with chronic HBV infection and interferon therapy were tested with both assays.Results: The detection limit was found to be 10³ copies/ml with the Amplicor™ PCR assay compared to 10⁶ to 10⁷ copies/ml with the Digene™ hybridization assay. Both assays were quasi-linear over the measurable ranges. The new PCR assay proved to be very reliable. With the Amplicor™ PCR assay, 26.2% of the HBV DNA-positive clinical samples were found between 10³ and 10⁷ copies/ml and all of them tested below the detection limit with the hybridization assay.Conclusion: The Amplicor™ HBV Monitor Test shows excellent sensitivity and provides a valuable tool for the detection of HBV DNA in serum. It can be used for recognizing those patients who might benefit from antiviral therapy, for evaluation of the efficacy of anti-HBV therapy, and for validation of blood products.     

Peptide ligands for the affinity purification of adeno-associated viruses from HEK 293 cell lysates

Adeno-associated viruses (AAVs) are the vector of choice for delivering gene therapies that can cure inherited and acquired diseases. Clinical research on various AAV serotypes significantly increased in recent years alongside regulatory approvals of AAV-based therapies. The current AAV purification platform hinges on the capture step, for which several affinity resins are commercially available. These adsorbents rely on protein ligands—typically camelid antibodies—that provide high binding capacity and selectivity, but suffer from low biochemical stability and high cost, and impose harsh elution conditions (pH < 3) that can harm the transduction activity of recovered AAVs. Addressing these challenges, this study introduces peptide ligands that selectively capture AAVs and release them under mild conditions (pH = 6.0). The peptide sequences were identified by screening a focused library and modeled in silico against AAV serotypes 2 and 9 (AAV2 and AAV9) to select candidate ligands that target homologous sites at the interface of the VP1-VP2 and VP2-VP3 virion proteins with mild binding strength (K_D ~ 10⁻⁵–10⁻⁶ M). Selected peptides were conjugated to Toyopearl resin and evaluated via binding studies against AAV2 and AAV9, demonstrating the ability to target both serotypes with values of dynamic binding capacity (DBC_10% > 10¹³ vp/mL of resin) and product yields (~50%–80%) on par with commercial adsorbents. The peptide-based adsorbents were finally utilized to purify AAV2 from a HEK 293 cell lysate, affording high recovery (50%–80%), 80- to 400-fold reduction of host cell proteins (HCPs), and high transduction activity (up to 80%) of the purified viruses.     

Germanium toxicity in selected bacterial and yeast strains

Summary The toxicity of germanium dioxide (GeO₂) to 21 bacterial and 13 yeast strains was investigated in liquid broth medium to obtain information on strains tolerant to high (1 to 2 mg/ml) GeO₂ concentrations.Arthrobacter sp. NRC 32005,enterobacter aerogenes NRC 2926,Klebsiella aerogenes NCTC 418 andPseudomonas putida NRC 5019 were tolerant to 1 mg/ml GeO₂.Bacillus sp. RC607 was able to grow in the presence of 2 mg/ml GeO₂ at pH 10 in broth culture. The yeastsCandida guilliermondii, Candida shehatae andPachysolen tannophilus were the most sensitive to GeO₂ as evidenced by their diminished growth rates at a GeO₂ concentration as low as 0.1 mg/ml. None of the yeast strains tested exhibited growth in the presence of 1 mg/ml GeO₂. The high pH of the medium containing germanium may be partially responsible for the growth inhibition of the yeast cultures. Select bacterial cultures previously exposed to 1 mg/ml GeO₂ could tolerate and grow better at 2 mg/ml GeO₂, suggesting the existence of very efficient adaptive mechanisms. The pH of the medium could modulate GeO₂ tolerance and this effect was found to be strain-dependent.     

Development of a submerged-liquid sporulation medium for the johnsongrass bioherbicide<Emphasis Type="Italic"> Gloeocercospora sorghi</Emphasis>

Submerged culture experiments were conducted in three phases to determine the optimal medium for rapidly producing conidia of the fungal bioherbicide Gloeocercospora sorghi. In phase I, 18 crude carbon sources were evaluated to determine which would support sporulation. Under the conditions tested, butter bean and lima bean brines (1.5–4.6 mS/cm) provided best conidiation. In phase II, a fractional-factorial design was utilized to screen 76 different medium adjuncts in combination with butter bean brine for improved sporulation. d-Mannitol and carboxymethylcellulose (CMC) were the only acceptable factors that resulted in a significant improvement. In phase III, a central composite design with response surface methodology was used to optimize concentrations of these critical factors. The model predicted optimal sporulation in a medium composed of 2.69 mS/cm butter bean brine +0.043 M d-mannitol +0.37% w/v CMC with an expected titer of 1.51×10⁷ conidia/ml. Actual mean titer attained with the model-derived medium was 1.91×10⁷ conidia/ml. Optimal sporulation occurred at 25.5°C in this medium and conidia remained viable up to 2.71 days when stored at 12°C. No significant difference was observed in virulence of conidia produced on agar vs washed conidia produced in the model-derived (liquid) medium.     

A new serum-free method of measuring growth factor activities for human breast cancer cells in culture

Summary Growth of the MCF-7, T47D, and ZR-75-1 human breast cancer cells was established in a serum-free defined medium (MOM-1) composed of a 1∶1 (vol/vol) mixture of Ham's F12 medium and Dulbecco's modified Eagle's medium containing 15 mM HEPES (pH 7.2), 2 mM 1-glutamine, 20 μg/ml glutathione, 10 μg/ml insulin, 10 μg/ml transferrin (Tf), 10 ng/ml selenous acid, 0.3 nM triiodothyronine, 50 μg/ml ethanolamine, 20 ng/ml epidermal, growth factor, 2.0 nM 17β-estradiol, and 1.0 mg/ml bovine serum albumin (BSA). Proliferation in MOM-1 was 50 to 70% of the serum stimulated rate. Deletion of components from MOM-1 gave a medium (Tf-BSA) containing only HEPES, 10 μg/ml Tf, and 200 μg/ml BSA, which sustained MCF-7 and T47D cells in a slowly dividing and mitogen responsive state; ZR-75-1 cells required Tf plus 1.0 mg/ml BSA. In Tf-BSA, insulin and insulin-like growth factor I(IGF-I) were mitogenic with ED₅₀ values of 2 to 3 ng/ml and 30 to 150 pg/ml, respectively, with MCF-7 cells. The T47D cells were responsive to these factors in Tf-BSA but required 10-fold higher concentrations for ED₅₀. At saturating concentrations, insulin and IGF-I promoted 1.5 to 3.5 cell population doublings over controls in 8 d. At≤ng/ml concentrations, epidermal growth factor, insulin-like growth factor II, and basic fibroblast growth factor were mitogenic for human breast cancer cells in Tf-BSA. Mitogen activities in uterus and pituitary extracts were assayed readily in Tf-BSA. This new method offers a convenient means of comparing the potencies of growth-promoting factors on human breast cancer cells without interfering activities known to be present in serum. This work was supported by grants CA-38024 and CA-26617, from the National Cancer Institute, Bethesda, MD, and by American Cancer Society grant BC-255 and grant 2225 from the Council for Tobacco Research, USA, Inc.     

Enzyme inactivation and stabilization studies in an ultrafiltration reactor

Summary An ultrafiltration membrane enzymatic reactor is used in connection with different reacting systems.The experimental conditions are such that the enzyme, which operates at fairly high concentration levels because of the concentration polarization phenomena taking place in the reactor, is still in soluble form.The analysis of the system unsteady-state response enables the identification of the mechanism of enzyme deactivation and the extraction of the kinetic parameters of both the deactivation and the main reaction.The stabilizing effect observed in connection with enzyme entrapment within an inert gel deposited onto the U.F. membrane active surface is also discussed.List of Symbols A U.F. membrane cross sectional area cm² - C_E Enzyme concentration mg/ml - C_EI Enzyme concentration at the active membrane surface mg/ml - C_E Mean enzyme concentration mg/ml - c _s ^o Substrate concentration in the feed m moles/ml - c _s ^u Substrate concentration in the outlet m moles/ml - D_E Enzyme diffusivity cm²/s - Km michaelis constant mM - k₂ Kinetic constant of the enzymatic reaction m moles/mg s - k_d Kinetic constant of the enzyme deactivation reaction s^–1 - N^o Initial amount of active enzyme mg - N(t) Active enzyme amount at reaction time t mg - Q Flow rate ml/s - r Rate of the main reaction m moles/ml s - t Reaction time s - t^* Reaction time at which product concentration in the outlet is within ± 2% of the steady-state value s - v Fluid velocity cm/s - V Cell volume ml - V_B Volume within which 99% of the enzyme fed is contained at the steady-state ml - V_S Volume within which 99% of the total substrate concentration drop occurs at the steady-state ml - x Distance upstream the membrane measured from the membrane surface cm     

Capacitation of hamster spermatozoa with the divalent cation chelators D-penicillamine,L-histidine,and L-cysteine in a protein-free culture medium

By using a chemically defined (protein-free) culture medium that supports sperm viability but not capacitation or the acrosome reaction, we have determined that hamster spermatozoa can be chemically capacitated in vitro by the divalent cation chelators D-penicilla-mine, L-histidine, and L-cysteine in the absence of bovine serum albumin (BSA). Washed cauda epididymal spermatozoa were preincubated (1–2 × 10⁶ sperm/ml) for 3, 4, or 6 hr at 37°C in 5% CO₂ in air. The basic culture medium used for sperm preincubation and for sperm:egg coincubation was a modified Tyrode's solution (protein-free) containing 10 mM sodium lactate, 100 μM sodium pyruvate, and 1.0 mg/ml polyvinylalcohol (TLP-PVA). Sperm viability was maintained in all preincubation and coincubation media with PHE (20 μM D-penicillamine, 100 μM hypotaurine, and 1.0 μM epinephrine). The low control sperm preincubation medium consisted of TLP-PVA. In some cases the high control preincubation medium also contained 3 mg/ml BSA (TALP-PVA). The experimental preincubation medium was TLP-PVA with additional D-penicillamine (125 or 500 μM), or L-histidine (10, 100, or 1,000 μM) or L-cysteine (25, 75, or 125 μM). After preincubation, sperm were coincubated (2 × 10⁴ sperm/ml) with cumulus-free hamster eggs in TALP-PVA ± additional D-penicillamine, L-histidine, or L-cysteine for 1.5 hr, fixed, and evaluated for percent egg penetration as an index of sperm capacitation. The results demonstrate that hamster spermatozoa can be chemically capacitated in vitro with D-penicillamine (500 μM: range of mean penetration values, 53.6%–84.3%), L-histidine (100 μM: range of mean values, 24.8%–56.3%) or L-cysteine (75 μM: 51.3%) in the absence of exogenous protein.     

Impact of the isoelectric point of model parvoviruses on viral retention in anion‐exchange chromatography

Anion‐exchange chromatography (AEX) is used in the downstream purification of monoclonal antibodies to remove impurities and potential viral contamination based on electrostatic interactions. Although the isoelectric point (pI) of viruses is considered a key factor predicting the virus adsorption to the resin, the precise molecular mechanisms involved remain unclear. To address this question, we compared structurally homologous parvoviruses that only differ in their surface charge distribution. A single charged amino acid substitution on the capsid surface of minute virus of mice (MVM) provoked an increased apparent pI (pI_app) 6.2 compared to wild‐type MVM (pI_app = 4.5), as determined by chromatofocusing. Despite their radically different pI_app, both viruses displayed the same interaction profile in Mono Q AEX at different pH conditions. In contrast, the closely related canine parvovirus (pI_app = 5.3) displayed a significantly different interaction at pH 5. The detailed structural analysis of the intricate three‐dimensional structure of the capsids suggests that the charge distribution is critical, and more relevant than the pI, in controlling the interaction of a virus with the chromatographic resin. This study contributes to a better understanding of the molecular mechanisms governing virus clearance by AEX, which is crucial to enable robust process design and maximize safety.     

Ion exchange chromatography of antibody fragments

Effects of pH and conductivity on the ion exchange chromatographic purification of an antigen-binding antibody fragment (Fab) of pI 8.0 were investigated. Normal sulfopropyl (SP) group modified agarose particles (SP Sepharosetrade mark Fast Flow) and dextran modified particles (SP Sepharose XL) were studied. Chromatographic measurements including adsorption isotherms and dynamic breakthrough binding capacities, were complemented with laser scanning confocal microscopy. As expected static equilibrium and dynamic binding capacities were generally reduced by increasing mobile phase conductivity (1-25 mS/cm). However at pH 4 on SP Sepharose XL, Fab dynamic binding capacity increased from 130 to 160 (mg/mL media) as mobile phase conductivity changed from 1 to 5 mS/cm. Decreasing protein net charge by increasing pH from 4 to 5 at 1.3 mS/cm caused dynamic binding capacity to increase from 130 to 180 mg/mL. Confocal scanning laser microscopy studies indicate such increases were due to faster intra-particle mass transport and hence greater utilization of the media's available binding capacity. Such results are in agreement with recent studies related to ion exchange of whole antibody molecules under similar conditions.