Salt tolerant membrane adsorbers for robust impurity clearance

Clearance of impurities such as viruses, host cell protein (HCP), and DNA is a critical purification design consideration for manufacture of monoclonal antibody therapeutics. Anion exchange chromatography has frequently been utilized to accomplish this goal; however, anion exchange adsorbents based on the traditional quaternary amine (Q) ligand are sensitive to salt concentration, leading to reduced clearance levels of impurities at moderate salt concentrations (50–150 mM). In this report, membrane adsorbers incorporating four alternative salt tolerant anion exchange ligands were examined for impurity clearance: agmatine, tris‐2‐aminoethyl amine, polyhexamethylene biguanide (PHMB), and polyethyleneimine. Each of these ligands provided greater than 5 log reduction value (LRV) for viral clearance of phage ?X174 (pI ～ 6.7) at pH 7.5 and phage PR772 (pI ～ 4) at pH 4.2 in the presence of salt. Under these same conditions, the commercial Q membrane adsorber provided no clearance (zero LRV). Clearance of host‐cell protein at pH 7.5 was the most challenging test case; only PHMB maintained 1.5 LRV in 150 mM salt. The salt tolerance of PHMB was attributed to its large positive net charge through the presence of multiple biguanide groups that participated in electrostatic and hydrogen bonding interactions with the impurity molecules. On the basis of the results of this study, membrane adsorbers that incorporate salt tolerant anion exchange ligands provide a robust approach to impurity clearance during the purification of monoclonal antibodies. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Viral clearance by flow‐through mode ion exchange columns and membrane adsorbers

Anion exchange (AEX) is a common downstream purification operation for biotechnology products manufactured in cell culture such as therapeutic monoclonal antibodies (mAbs) and Fc‐fusion proteins. We present a head‐to‐head comparison of the viral clearance efficiency of AEX adsorbers and column chromatography using the same process fluids and comparable run conditions. We also present overall trends from the CDER viral clearance database. In our comparison of multiple brands of resins and adsorbers, clearance of three model viruses (PPV, X‐MuLV, and PR772) was largely comparable, with some exceptions which may reflect run conditions that had not been optimized on a resin/membrane specific basis. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:124–131, 2014     

Monoclonal antibody capture and viral clearance by cation exchange chromatography

Traditionally, post-production culture harvest capture of therapeutic monoclonal antibodies (mAbs) is performed using Protein A chromatography. We investigated the efficiency and robustness of cation exchange chromatography (CEX) in an effort to evaluate alternative capture methodologies. Up to five commercially available CEX resins were systematically evaluated using an experimentally optimized buffer platform and a design-of-experiment (DoE) approach for their ability to (a) capture a model mAb with a neutral isoelectric point, (b) clear three model viruses (porcine parvovirus, CHO type-C particles, and a bacteriophage). This approach identified a narrow operating space where yield, purity, and viral clearance were optimal under a CEX capture platform, and revealed trends between viral clearance of PPV and product purity (but not yield). Our results suggest that after unit operation optimization, CEX can serve as a suitable capture step.     

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     

Anion exchange membrane adsorbers for flow‐through polishing steps: Part I. clearance of minute virus of mice

Membrane adsorbers may be a viable alternative to the packed‐bed chromatography for clearance of virus, host cell proteins, DNA, and other trace impurities. However, incorporation of membrane adsorbers into manufacturing processes has been slow due to the significant cost associated with obtaining regulatory approval for changes to a manufacturing process. This study has investigated clearance of minute virus of mice (MVM), an 18–22 nm parvovirus recognized by the FDA as a model viral impurity. Virus clearance was obtained using three commercially available anion exchange membrane adsorbers: Sartobind Q®, Mustang Q®, and ChromaSorb®. Unlike earlier studies that have focused on a single or few operating conditions, the aim here was to determine the level of virus clearance under a range of operating conditions that could be encountered in industry. The effects of varying pH, NaCl concentration, flow rate, and other competing anionic species present in the feed were determined. The removal capacity of the Sartobind Q and Mustang Q products, which contain quaternary ammonium based ligands, is sensitive to feed conductivity and pH. At conductivities above about 20 mS/cm, a significant decrease in capacity is observed. The capacity of the ChromaSorb product, which contains primary amine based ligands, is much less affected by ionic strength. However the capacity for binding MVM is significantly reduced in the presence of phosphate ions. These differences may be explained in terms of secondary hydrogen bonding interactions that could occur with primary amine based ligands. Biotechnol. Bioeng. 2013; 110: 491–499. © 2012 Wiley Periodicals, Inc.     

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.     

Generic/matrix evaluation of SV40 clearance by anion exchange chromatography in flow-through mode

The potential of viral contamination is a regulatory concern for continuous cell line-derived pharmaceutical proteins. Complementary and redundant safety steps, including an evaluation of the viral clearance capacity of unit operations in the purification process, are performed prior to registration and marketing of biotechnology pharmaceuticals. Because process refinement is frequently beneficial, CBER/FDA has published guidance facilitating process improvement by delineating specific instances where the bracketing and generic approaches are appropriate for virus removal validation. In this study, a generic/matrix study was performed using Q-Sepharose Fast Flow (QSFF) chromatography to determine if bracketing and generic validation can be applied to anion exchange chromatography. Key operational parameters were varied to upper and lower extreme values and the impact on viral clearance was assessed using simian virus 40 (SV40) as the model virus. Operational ranges for key chromatography parameters were identified where an SV40 log(10) reduction value (LRV) of >or=4.7 log(10) is consistently achieved. On the basis of the apparent robustness of SV40 removal by Q-anion exchange chromatography, we propose that the concept of "bracketed generic" validation can be applied to this and potentially other chromatography unit operations.     

Impact of ligand density on the optimization of ion-exchange membrane chromatography for viral vector purification

The effect of ligand density on anion-exchange membrane chromatography (AEXmc) for the purification of recombinant baculoviruses (rBVs), potential viral vectors in clinical applications, is studied by surface plasmon resonance on customized AEX surfaces and gradient elution experiments on Sartobind D membrane prototypes with different diethylamine ligand densities, complemented by dynamic light scattering analysis for estimation of the hydrodynamic particle size of the various biologics. A chromatographic-column model based on the steric mass action model of ion exchange is employed to analyze the gradient-elution AEXmc experiments, extrapolate the results to other operating conditions, and provide directions for process improvement. Although counterintuitively, the experimental evidence provided in this study shows that the lowering of ligand density is beneficial for rBV purification by AEXmc in bind-and-elute-mode, because it decreases the residual concentrations of host cell protein, dsDNA, and non-infective rBVs in the eluted product cut, and increases the overall yield by roughly 20% over current standard values. Overall, we present a case study on how rational design can streamline downstream process development.     

Development of a 3‐step straight‐through purification strategy combining membrane adsorbers and resins

The pressures to efficiently produce complex biopharmaceuticals at reduced costs are driving the development of novel techniques, such as in downstream processing with straight‐through processing (STP). This method involves directly and sequentially purifying a particular target with minimal holding steps. This work developed and compared six different 3‐step STP strategies, combining membrane adsorbers, monoliths, and resins, to purify a large, complex, and labile glycoprotein from Chinese hamster ovary cell culture supernatant. The best performing pathway was cation exchange chromatography to hydrophobic interaction chromatography to affinity chromatography with an overall product recovery of up to 88% across the process and significant clearance of DNA and protein impurities. This work establishes a platform and considerations for the development of STP of biopharmaceutical products and highlights its suitability for integration with single‐use technologies and continuous production methods. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:931–940, 2017     

Anion exchange membrane adsorbers for flow‐through polishing steps: Part II. Virus,host cell protein,DNA clearance,and antibody recovery

Anion exchange membrane adsorbers are used for contaminant removal in flow‐through polishing steps in the manufacture of biopharmaceuticals. This contribution describes the clearance of minute virus of mice, DNA, and host cell proteins by three commercially available anion‐exchange membranes: Sartobind Q, Mustang Q, and ChromaSorb. The Sartobind Q and Mustang Q products contain quaternary amine ligands; whereas, ChromaSorb contains primary amine based ligands. Performance was evaluated over a range of solution conditions: 0–200 mM NaCl, pH 6.0–9.0, and flow rates of 4–20 membrane volumes/min in the presence and absence of up to 50 mM phosphate and acetate. In addition contaminant clearance was determined in the presence and absence of 5 g/L monoclonal antibody. The quaternary amine based ligands depend mainly on Coulombic interactions for removal of negatively charged contaminants. Consequently, performance of Sartobind Q and Mustang Q was compromised at high ionic strength. Primary amine based ligands in ChromaSorb enable high capacities at high ionic strength due to the presence of secondary, hydrogen bonding interactions. However, the presence of hydrogen phosphate ions leads to reduced capacity. Monoclonal antibody recovery using primary amine based anion‐exchange ligands may be lower if significant binding occurs due to secondary interactions. The removal of a specific contaminant is affected by the level of removal of the other contaminants. The results of this study may be used to help guide selection of commercially available membrane absorbers for flow‐through polishing steps. Biotechnol. Bioeng. 2013; 110: 500–510. © 2012 Wiley Periodicals, Inc.     

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.     

The prevention of an anomalous chromatographic behavior and the resulting successful removal of viruses from monoclonal antibody with an asymmetric charge distribution by using a membrane adsorber in highly efficient,anion-exchange chromatography in flow-through mode

Anion exchange (AEX) chromatography in the flow-through mode is a widely employed purification process for removal of process/product-related impurities and exogenous/endogenous viruses from monoclonal antibodies (mAbs). The pH of the mobile phase for AEX chromatography is typically set at half a unit below the isoelectric point (pI) of each mAb (i.e., pI − 0.5) or lower and, in combination with a low ionic strength, these conditions are usually satisfactory for both the recovery of the mAb and removal of impurities. However, we have recently encountered a tight binding of mAb1 to AEX resins under these standard chromatographic conditions. This anomalous adsorption behavior appears to be an effect of the asymmetric charge distribution on the surface of the mAb1. We found that mAb1 did not bind to the AEX resins if the mobile phase has a much lower pH and higher ionic strength, but those conditions would not allow adequate virus removal. We predicted that the use of membrane adsorbers might provide effective mAb1 purification, since the supporting matrix has a network structure that would be less susceptible to interactions with the asymmetric charge distribution on the protein surface. We tested the Natriflo HD-Q AEX membrane adsorber under standard chromatographic conditions and found that mAb1 flowed through the membrane adsorber, resulting in successful separation from murine leukemia virus. This AEX membrane adsorber is expected to be useful for process development because mAbs can be purified under similar standard chromatographic conditions regardless of their charge distributions.     

Strategies for developing design spaces for viral clearance by anion exchange chromatography during monoclonal antibody production

The quality‐by‐design (QbD) regulatory initiative promotes the development of process design spaces describing the multidimensional effects and interactions of process variables on critical quality attributes of therapeutic products. However, because of the complex nature of production processes, strategies must be devised to provide for design space development with reasonable allocation of resources while maintaining highly dependable results. Here, we discuss strategies for the determination of design spaces for viral clearance by anion exchange chromatography (AEX) during purification of monoclonal antibodies. We developed a risk assessment for AEX using a formalized method and applying previous knowledge of the effects of certain variables and the mechanism of action for virus removal by this process. We then use design‐of‐experiments (DOE) concepts to perform a highly fractionated factorial experiment and show that varying many process parameters simultaneously over wide ranges does not affect the ability of the AEX process to remove endogenous retrovirus‐like particles from CHO‐cell derived feedstocks. Finally, we performed a full factorial design and observed that a high degree of viral clearance was obtained for three different model viruses when the most significant process parameters were varied over ranges relevant to typical manufacturing processes. These experiments indicate the robust nature of viral clearance by the AEX process as well as the design space where removal of viral impurities and contaminants can be assured. In addition, the concepts and methodology presented here provides a general approach for the development of design spaces to assure that quality of biotherapeutic products is maintained. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Impact of antibody aggregation on a flowthrough anion‐exchange membrane process

The impact of typical anion‐exchange flowthrough conditions on the IgG mass loading of an anion‐exchange membrane scale‐down unit (Mustang® Q coin) was investigated. High performance size‐exclusion chromatography and multiangle laser light scattering results suggested the presence of a small fraction of IgG aggregates with average radius >100 nm under anion‐exchange flowthrough conditions. The small filtration area presented by the 0.35 mL membrane volume Mustang® Q coin limited the membrane throughput due to fouling from the aggregates at higher antibody loading. Data in this report indicated that a 0.2 μm hybrid polyethersulfone and polyvinylidene fluoride membrane in‐line prefilter with a minimum filtration area of 20 sq cm alleviated the Mustang® Q coin fouling. The combined cake filtration and intermediate blocking model was proposed as the most likely membrane pore blocking mechanism. Increasing the filtration area in the in‐line prefilter resulted in higher IgG mass throughput. Thus, using an appropriately sized in‐line prefilter could provide more robust antibody throughput performance on scale‐down membrane anion‐exchange units. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Fractionation of β‐Lactoglobulin from whey by mixed matrix membrane ion exchange chromatography

Mixed matrix membranes (MMMs), which incorporate adsorptive particles during membrane casting, can be prepared simply and have performances that are competitive with other membrane chromatography materials. The application of MMM chromatography for fractionation of β‐Lactoglobulin from bovine whey is described in this article. MMM chromatography was prepared using ethylene vinyl alcohol polymer and lewatit anion exchange resin to form a flat sheet membrane. The membrane was characterized in terms of structure and its static and dynamic binding capacities were measured. The optimum binding for β‐Lactoglobulin was found to be at pH 6.0 using 20 mM sodium phosphate buffer. The MMM had a static binding capacity of 120 mg/g membrane (36 mg/mL membrane) and 90 mg/g membrane (27 mg/mL membrane) for β‐Lactoglobulin and α‐Lactalbumin, respectively. In batch fractionation of whey, the MMM showed selective binding towards β‐Lactoglobulin compared to other proteins. The dynamic binding capacity of β‐Lactoglobulin in whey solution was about 80 mg/g membrane (24 mg β‐Lac/mL of MMM), which is promising for whey fractionation using this technology. This is the first reported application of MMM chromatography to a dairy feed stream. Biotechnol. Bioeng. 2009;103: 138–147. © 2008 Wiley Periodicals, Inc.     

Sulfated membrane adsorbers for economic pseudo‐affinity capture of influenza virus particles

Strategies to control outbreaks of influenza, a contagious respiratory tract disease, are focused mainly on prophylactic vaccinations in conjunction with antiviral medications. Currently, several mammalian cell culture‐based influenza vaccine production processes are being established, such as the technologies introduced by Novartis Behring (Optaflu®) or Baxter International Inc. (Celvapan). Downstream processing of influenza virus vaccines from cell culture supernatant can be performed by adsorbing virions onto sulfated column chromatography beads, such as Cellufine® sulfate. This study focused on the development of a sulfated cellulose membrane (SCM) chromatography unit operation to capture cell culture‐derived influenza viruses. The advantages of the novel method were demonstrated for the Madin Darby canine kidney (MDCK) cell‐derived influenza virus A/Puerto Rico/8/34 (H1N1). Furthermore, the SCM‐adsorbers were compared directly to column‐based Cellufine® sulfate and commercially available cation‐exchange membrane adsorbers. Sulfated cellulose membrane adsorbers showed high viral product recoveries. In addition, the SCM‐capture step resulted in a higher reduction of dsDNA compared to the tested cation‐exchange membrane adsorbers. The productivity of the SCM‐based unit operation could be significantly improved by a 30‐fold increase in volumetric flow rate during adsorption compared to the bead‐based capture method. The higher flow rate even further reduced the level of contaminating dsDNA by about twofold. The reproducibility and general applicability of the developed unit operation were demonstrated for two further MDCK cell‐derived influenza virus strains: A/Wisconsin/67/2005 (H3N2) and B/Malaysia/2506/2004. Overall, SCM‐adsorbers represent a powerful and economically favorable alternative for influenza virus capture over conventional methods using Cellufine® sulfate. Biotechnol. Bioeng. 2009;103: 1144–1154. © 2009 Wiley Periodicals, Inc.     

Understanding the mechanism of virus removal by Q sepharose fast flow chromatography during the purification of CHO‐cell derived biotherapeutics

During production of therapeutic monoclonal antibodies (mAbs) in mammalian cell culture, it is important to ensure that viral impurities and potential viral contaminants will be removed during downstream purification. Anion exchange chromatography provides a high degree of virus removal from mAb feedstocks, but the mechanism by which this is achieved has not been characterized. In this work, we have investigated the binding of three viruses to Q sepharose fast flow (QSFF) resin to determine the degree to which electrostatic interactions are responsible for viral clearance by this process. We first used a chromatofocusing technique to determine the isoelectric points of the viruses and established that they are negatively charged under standard QSFF conditions. We then determined that virus removal by this chromatography resin is strongly disrupted by the presence of high salt concentrations or by the absence of the positively charged Q ligand, indicating that binding of the virus to the resin is primarily due to electrostatic forces, and that any non‐electrostatic interactions which may be present are not sufficient to provide virus removal. Finally, we determined the binding profile of a virus in a QSFF column after a viral clearance process. These data indicate that virus particles generally behave similarly to proteins, but they also illustrate the high degree of performance necessary to achieve several logs of virus reduction. Overall, this mechanistic understanding of an important viral clearance process provides the foundation for the development of science‐based process validation strategies to ensure viral safety of biotechnology products. Biotechnol. Bioeng. 2009; 104: 371–380 © 2009 Wiley Periodicals, Inc.     

Systematic purification of salt‐intolerant proteins by ion‐exchange chromatography: The example of human α‐galactosidase A

Chromatography is an essential tool for purifying biopharmaceutical products. Many processes are still developed based on traditional routines and empirical procedures. Product losses are mostly due to insufficient optimization of purification setups and product sensitivity to process conditions. In order to eliminate these shortcomings, a systematic strategy for the setup of ion‐exchange chromatography is presented, which considers both product stability as well as operational conditions. The stages—a hybrid approach combining high‐throughput screening and analytical small‐scale chromatography—are as follows: (1) pH stability (short‐term); (2) pH stability (long‐term), followed by a screening of additives to enhance protein stability, if required; (3) analytical pH gradient chromatography for evaluation of the operational pH window; and (4) salt stability (long‐term) in the operational pH window determined. The efficiency and straightforwardness of the strategy were shown in a case study on capturing the human α‐galactosidase A enzyme. Following the above procedure, the enzyme was found to be salt‐unstable; a purification factor of 13.2, a concentration factor of 4, and an overall yield of 84.3% were achieved. The applied strategy allowed for a quick establishment of a dedicated capture step at low salt concentrations under stable conditions by well‐chosen prior screening experiments.     

Characterization of an ethanol‐tolerant 1,4‐β‐xylosidase produced by Pichia membranifaciens

Aims: The purification and biochemical properties of the 1,4‐β‐xylosidase of an oenological yeast were investigated. Methods and Results: An ethanol‐tolerant 1,4‐β‐xylosidase was purified from cultures of a strain of Pichia membranifaciens grown on xylan at 28°C. The enzyme was purified by sequential chromatography on DEAE cellulose and Sephadex G‐100. The relative molecular mass of the enzyme was determined to be 50 kDa by SDS‐PAGE. The activity of 1,4‐β‐xylosidase was optimum at pH 6·0 and at 35°C. The activity had a K_m of 0·48 ± 0·06 mmol l^?1 and a V_max of 7·4 ± 0·1 μmol min^?1 mg^?1 protein for p‐nitrophenyl‐β‐d ‐xylopyranoside. Conclusions: The enzyme characteristics (pH and thermal stability, low inhibition rate by glucose and ethanol tolerance) make this enzyme a good candidate to be used in enzymatic production of xylose and improvement of hemicellulose saccharification for production of bioethanol. Significance and Impact of the Study: This study may be useful for assessing the ability of the 1,4‐β‐xylosidase from P. membranifaciens to be used in the bioethanol production process.     

PPAR‐β facilitating maturation of hepatic‐like tissue derived from mouse embryonic stem cells accompanied by mitochondriogenesis and membrane potential retention

Relatively little is known about mitochondria metabolism in differentiating embryonic stem (ES) cells. Present research focused on several elements of cellular energy metabolism in hepatic‐like tissue derived from mouse ES cells. We demonstrated that mitochondrial location patterns and mitochondrial membrane potential (ΔΨ_m) existed in subsequent differentiation of the tissue. Mitochondriogenesis appeared at the early stage and kept a normal ΔΨ_m in differentiated mature hepatocytes. Peroxisome proliferator‐activated receptor‐α (PPAR‐α) expression was transitorily increased at the beginning, and kept a relatively low level later, which accompanied by expression of PPAR‐γ coactivator (PGC)‐1α, a master regulator of mitochondrial biogenesis. PPAR‐β expression showed robust up‐regulation in the late differentiation course. Enhanced co‐expressions of PPAR‐β and albumin with catalysis of UDP‐glucuronosyltransferases (UGTs) were observed at mature stage. While PPAR‐γ expression changed little before and after differentiation. Mitochondriogenesis could be accelerated by PPAR‐α specific agonist WY14643 and abolished by its antagonist GW6471 at the early stage. Neither of them affected mitochondrial ΔΨ_m and albumin generation in the differentiated hepatocytes. Furthermore, maturation of hepatic‐like tissue and mitochondriogenesis in hepatocyte could be efficiently stimulated by PPAR‐β specific agonist L165041 and abolished by PPAR‐β specific antagonist GSK0660, but not affected by PPAR‐γ specific agonist GW1929. In conclusion, the derived hepatic tissue morphologically possessed cellular energy metabolism features. PPAR‐α seemed only necessary for early mitochondriogenesis, while less important for ΔΨ_m retention in the mature tissue derived. The stimulation of PPAR‐β but not ‐γ enhanced hepatogenesis, hepatocytes maturation, and mitochondriogenesis. PPAR‐β took an important role in cellular energy metabolism of hepatogenesis. J. Cell. Biochem. 109: 498–508, 2010. © 2009 Wiley‐Liss, Inc.