Evaluation of options for harvest of a recombinant E. Coli fermentation producing a domain antibody using ultra scale‐down techniques and pilot‐scale verification

Ultra scale‐down (USD) methods operating at the millilitre scale were used to characterise full‐scale processing of E. coli fermentation broths autolysed to different extents for release of a domain antibody. The focus was on the primary clarification stages involving continuous centrifugation followed by depth filtration. The performance of this sequence was predicted by USD studies to decrease significantly with increased extents of cell lysis. The use of polyethyleneimine reagent was studied to treat the lysed cell broth by precipitation of soluble contaminants such as DNA and flocculation of cell debris material. The USD studies were used to predict the impact of this treatment on the performance and here it was found that the fermentation could be run to maximum productivity using an acceptable clarification process (e.g., a centrifugation stage operating at 0.11 L/m² equivalent gravity settling area per hour followed by a resultant required depth filter area of 0.07 m²/L supernatant). A range of USD predictions was verified at the pilot scale for centrifugation followed by depth filtration. © 2016 The Authors Biotechnology Progress published by Wiley Periodicals, Inc. on behalf of American Institute of Chemical Engineers Biotechnol. Prog., 32:382–392, 2016     

Adapted ultra scale-down approach for predicting the centrifugal separation behavior of high cell density cultures

The work presented here describes an ultra scale-down (USD) methodology for predicting centrifugal clarification performance in the case of high cell density fermentation broths. Existing USD approaches generated for dilute systems led to a 5- to 10-fold overprediction of clarification performance when applied to such high cell density feeds. This is due to increased interparticle forces, leading to effects such as aggregation, flocculation, or even blanket sedimentation, occurring in the low shear environment of a laboratory centrifuge, which will not be apparent in the settling region of a continuous-flow industrial centrifuge. A USD methodology was created based upon the dilution of high solids feed material to approximately 2% wet wt/vol prior to the application of the clarification test. At this level of dilution cell-cell interactions are minimal. The dilution alters the level of hindered settling in the feed suspensions, and so mathematical corrections are applied to the resultant clarification curves to mimic the original feed accurately. The methodology was successfully verified: corrected USD curves accurately predicted pilot-scale clarification performance of high cell density broths of Saccharomyces cerevisiae and Escherichia coli cells. The USD method allows for the rapid prediction of large-scale clarification of high solids density material using millilitre quantities of feed. The advantages of this method to the biochemical engineer, such as the enabling of rapid process design and scale-up, are discussed.     

Mcl‐1 overexpression leads to higher viabilities and increased production of humanized monoclonal antibody in Chinese hamster ovary cells

Bioreactor stresses, including nutrient deprivation, shear stress, and byproduct accumulation can cause apoptosis, leading to lower recombinant protein yields and increased costs in downstream processing. Although cell engineering strategies utilizing the overexpression of antiapoptotic Bcl‐2 family proteins such as Bcl‐2 and Bcl‐x_L potently inhibit apoptosis, no studies have examined the use of the Bcl‐2 family protein, Mcl‐1, in commercial mammalian cell culture processes. Here, we overexpress both the wild type Mcl‐1 protein and a Mcl‐1 mutant protein that is not degraded by the proteasome in a serum‐free Chinese hamster ovary (CHO) cell line producing a therapeutic antibody. The expression of Mcl‐1 led to increased viabilities in fed‐batch culture, with cell lines expressing the Mcl‐1 mutant maintaining ～90% viability after 14 days when compared with 65% for control cells. In addition to enhanced culture viability, Mcl‐1‐expressing cell lines were isolated that consistently showed increases in antibody production of 20–35% when compared with control cultures. The quality of the antibody product was not affected in the Mcl‐1‐expressing cell lines, and Mcl‐1‐expressing cells exhibited 3‐fold lower caspase‐3 activation when compared with the control cell lines. Altogether, the expression of Mcl‐1 represents a promising alternative cell engineering strategy to delay apoptosis and increase recombinant protein production in CHO cells. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Shear stress analysis of mammalian cell suspensions for prediction of industrial centrifugation and its verification

This article describes the use of ultra scale-down studies requiring milliliter quantities of process material to study the clarification of mammalian cell culture broths using industrial-scale continuous centrifuges during the manufacture of a monoclonal antibody for therapeutic use. Samples were pretreated in a small high-speed rotating-disc device in order to mimic the effect on the cells of shear stresses in the feed zone of the industrial scale centrifuges. The use of this feed mimic was shown to predict a reduction of the clarification efficiency by significantly reducing the particle size distribution of the mammalian cells. The combined use of the rotating-disc device and a laboratory-scale test tube centrifuge successfully predicted the separation characteristics of industrial-scale, disc stack centrifuges operating with different feed zones. A 70% reduction in flow rate in the industrial-scale centrifuge was shown to arise from shear effects. A predicted 2.5-fold increase in throughput for the same clarification performance, achieved by the change to a centrifuge using a feed zone designed to give gentler acceleration of the bioprocess fluid, was also verified at large-scale.     

Mimic of a large‐scale diafiltration process by using ultra scale‐down rotating disc filter

Ultra scale‐down (USD) approach is a powerful tool to predict large‐scale process performance by using very small amounts of material. In this article, we present a method to mimic flux and transmission performance in a labscale crossflow operation by an USD rotating disc filter (RDF). The Pellicon 2 labscale system used for evaluation of the mimic can readily be related to small pilot and industrial scale. Adopted from the pulsed sample injection technique by Ghosh and Cui (J Membr Sci. 2000;175:5‐84), the RDF has been modified by building in inserts to allow the flexibility of the chamber volume, so that only 1.5 mL of processing material is required for each diafiltration experiment. The reported method enjoys the simplicity of dead‐end mode operation with accurate control of operation conditions that can mimic well the crossflow operation in large scale. Wall shear rate correlations have been established for both the labscale cassette and the USD device, and a mimic has been developed by operating both scales under conditions with equivalent averaged shear rates. The studies using E. coli lysate show that the flux vs. transmembrane pressure profile follows a first‐order model, and the transmission of antibody fragment (Fab′) is independent of transmembrane pressure. Predicted flux and transmission data agreed well with the experimental results of a labscale diafiltration where the cassette resistance was considered. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Ultra scale‐down prediction using microwell technology of the industrial scale clarification characteristics by centrifugation of mammalian cell broths

This article describes how a combination of an ultra scale‐down (USD) shear device feeding a microwell centrifugation plate may be used to provide a prediction of how mammalian cell broth will clarify at scale. In particular a method is described that is inherently adaptable to a robotic platform and may be used to predict how the flow rate and capacity (equivalent settling area) of a centrifuge and the choice of feed zone configuration may affect the solids carry over in the supernatant. This is an important consideration as the extent of solids carry over will determine the required size and lifetime of a subsequent filtration stage or the passage of fine particulates and colloidal material affecting the performance and lifetime of chromatography stages. The extent of solids removal observed in individual wells of a microwell plate during centrifugation is shown to correlate with the vertical and horizontal location of the well on the plate. Geometric adjustments to the evaluation of the equivalent settling area of individual wells (Σ_M) results in an improved prediction of solids removal as a function of centrifuge capacity. The USD centrifuge settling characteristics need to be as for a range of equivalent flow rates as may be experienced at an industrial scale for a machine of different shear characteristics in the entry feed zone. This was shown to be achievable with two microwell‐plate based measurements and the use of varying fill volumes in the microwells to allow the rapid study of a fivefold range of equivalent flow rates (i.e., at full scale for a particular industrial centrifuge) and the effect of a range of feed configurations. The microwell based USD method was used to examine the recovery of CHO‐S cells, prepared in a 5 L reactor, at different points of growth and for different levels of exposure to shear post reactor. The combination of particle size distribution measurements of the cells before and after shear and the effect of shear on the solids remaining after centrifugation rate provide insight into the state of the cells throughout the fermentation and the ease with which they and accumulated debris may be removed by continuous centrifugation. Hence bioprocess data are more readily available to help better integrate cell culture and cell removal stages and resolve key bioprocess design issues such as choice of time of harvesting and the impact on product yield and contaminant carry over. Operation at microwell scale allows data acquisition and bioprocess understanding over a wide range of operating conditions that might not normally be achieved during bioprocess development. Biotechnol. Bioeng. 2009; 104: 321–331 © 2009 Wiley Periodicals, Inc.     

IL7‐hCD25 and IL7‐Cre BAC transgenic mouse lines: New tools for analysis of IL‐7 expressing cells

IL‐7 is a cytokine that is required for T‐cell development and homeostasis as well as for lymph node organogenesis. Despite the importance of IL‐7 in the immune system and its potential therapeutic relevance, questions remain regarding the sites of IL‐7 synthesis, specific cell types involved and molecular mechanisms regulating IL‐7 expression. To address these issues, we generated two bacterial artificial chromosome (BAC) transgenic mouse lines in which IL‐7 regulatory elements drive expression of either Cre recombinase or a human CD25 (hCD25) cell surface reporter molecule. Expression of the IL‐7.hCD25 BAC transgene, detected by reactivity with anti‐hCD25 antibody, mimicked endogenous IL‐7 expression. Fetal and adult tissues from crosses between IL‐7.Cre transgenic mice and Rosa26R or R26‐EYFP reporters demonstrated X‐gal or YFP staining in tissues known to express endogenous IL‐7 at some stage during development. These transgenic lines provide novel genetic tools to identify IL‐7 producing cells in various tissues and to manipulate gene expression selectively in IL‐7 expressing cells. genesis 47:281–287, 2009. © 2009 Wiley‐Liss, Inc.     

Screening and assessment of performance and molecule quality attributes of industrial cell lines across different fed‐batch systems

The major challenge in the selection process of recombinant cell lines for the production of biologics is the choice, early in development, of a clonal cell line presenting a high productivity and optimal cell growth. Most importantly, the selected candidate needs to generate a product quality profile which is adequate with respect to safety and efficacy and which is preserved across cell culture scales. We developed a high‐throughput screening and selection strategy of recombinant cell lines, based on their productivity in shaking 96‐deepwell plates operated in fed‐batch mode, which enables the identification of cell lines maintaining their high productivity at larger scales. Twelve recombinant cell lines expressing the same antibody with different productivities were selected out of 470 clonal cell lines in 96‐deepwell plate fed‐batch culture. They were tested under the same conditions in 50 mL vented shake tubes, microscale and lab‐scale bioreactors in order to confirm the maintenance of their performance at larger scales. The use of a feeding protocol and culture conditions which are essentially the same across the different scales was essential to maintain productivity and product quality profiles across scales. Compared to currently used approaches, this strategy has the advantage of speeding up the selection process and increases the number of screened clones for getting high‐producing recombinant cell lines at manufacturing scale with the desired performance and quality. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:160–170, 2016     

A methodology for centrifuge selection for the separation of high solids density cell broths by visualisation of performance using windows of operation

Expression systems capable of growing to high cell densities are now readily available and are popular due to the benefits of increased product concentration. However, such high solids density cultures pose a major challenge for bioprocess engineers as choosing the right separation equipment and operating it at optimal conditions is crucial for efficient recovery. This study proposes a methodology for the rapid determination of suitable operating conditions for the centrifugal recovery of high cell density fermentation broths. An ultra scale-down (USD) approach for the prediction of clarification and dewatering levels achieved in a range of typical high-speed centrifuges is presented. Together with a visualisation tool, a Window of Operation, this provides for the rapid analysis of separation performance and evaluation of the available operating conditions, as an aid in the selection of the centrifuge equipment most appropriate for a given process duty. A case study examining centrifuge selection for the processing of a high cell density Pichia pastoris culture demonstrates the method. The study examines semi-continuous disc-stack centrifuges and batch-operated machines such as multi-chamber bowls and Carr Powerfuges. Performance is assessed based on the variables of clarification, dewatering and product yield. Inclusion of limits imposed by the centrifuge type and design, and operation itself, serve to constrain the process and to define the Windows of Operation. The insight gained from the case study provides a useful indication of the utility of the methodology presented and illustrates the challenges of centrifuge selection for the demanding case of high solids concentration feed streams.     

N‐linked glycosylation is an important parameter for optimal selection of cell lines producing biopharmaceutical human IgG

We studied the variations in N‐linked glycosylation of human IgG molecules derived from 105 different stable cell lines each expressing one of the six different antibodies. Antibody expression was based on glutamine synthetase selection technology in suspension growing CHO‐K1SV cells. The glycans detected on the Fc fragment were mainly of the core‐fucosylated complex type containing zero or one galactose and little to no sialic acid. The glycosylation was highly consistent for the same cell line when grown multiple times, indicating the robustness of the production and glycan analysis procedure. However, a twofold to threefold difference was observed in the level of galactosylation and/or non‐core‐fucosylation between the 105 different cell lines, suggesting clone‐to‐clone variation. These differences may change the Fc‐mediated effector functions by such antibodies. Large variation was also observed in the oligomannose‐5 glycan content, which, when present, may lead to undesired rapid clearance of the antibody in vivo. Statistically significant differences were noticed between the various glycan parameters for the six different antibodies, indicating that the variable domains and/or light chain isotype influence Fc glycosylation. The glycosylation altered when batch production in shaker was changed to fed‐batch production in bioreactor, but was consistent again when the process was scaled from 400 to 5,000 L. Taken together, the observed clone‐to‐clone glycosylation variation but batch‐to‐batch consistency provides a rationale for selection of optimal production cell lines for large‐scale manufacturing of biopharmaceutical human IgG. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

The immunoglobulin‐like cell adhesion molecule hepaCAM induces differentiation of human glioblastoma U373‐MG cells

Subsequent to our identification of a novel immunoglobulin‐like cell adhesion molecule hepaCAM, we showed that hepaCAM is frequently lost in diverse human cancers and is capable of modulating cell motility and growth when re‐expressed. Very recently, a molecule identical to hepaCAM (designated as GlialCAM) was found highly expressed in glial cells of the brain. Here, we demonstrate that hepaCAM is capable of inducing differentiation of the human glioblastoma U373‐MG cells. Expression of hepaCAM resulted in a significant increase in the astrocyte differentiation marker glial fibrillary acid protein (GFAP), indicating that hepaCAM promotes glioblastoma cells to undergo differentiation. To determine the relationship between hepaCAM expression level and cell differentiation, we established two U373‐MG cell lines expressing hepaCAM at different levels. The results revealed that high‐level hepaCAM triggered a clear increase in GFAP expression as well as morphological changes characteristic of glioblastoma cell differentiation. Furthermore, high expression of hepaCAM significantly accelerated cell adhesion but inhibited cell proliferation and migration. Concomitantly, deregulation of cell cycle regulatory proteins was detected. Expectedly, the differentiation was noticeably less apparent in cells expressing low‐level hepaCAM. Taken together, our findings suggest that hepaCAM induces differentiation of the glioblastoma U373‐MG cells. The degree of cell differentiation is dependent on the expression level of hepaCAM. J. Cell. Biochem. 107: 1129–1138, 2009. © 2009 Wiley‐Liss, Inc.     

An ultra scale‐down characterization of low shear stress primary recovery stages to enhance selectivity of fusion protein recovery from its molecular variants

Fusion proteins offer the prospect of new therapeutic products with multiple functions. The primary recovery is investigated of a fusion protein consisting of modified E2 protein from hepatitis C virus fused to human IgG1 Fc and expressed in a Chinese hamster ovary (CHO) cell line. Fusion protein products inevitably pose increased challenge in preparation and purification. Of particular concerns are: (i) the impact of shear stress on product integrity and (ii) the presence of product‐related contaminants which could prove challenging to remove during the high resolution purification steps. This paper addresses the use of microwell‐based ultra scale‐down (USD) methods to develop a bioprocess strategy focused on the integration of cell culture and cell removal operations and where the focus is on the use of operations which impart low shear stress levels even when applied at eventual manufacturing scale. An USD shear device was used to demonstrate that cells exposed to high process stresses such as those that occur in the feed zone of a continuous non‐hermetic centrifuge resulted in the reduction of the fusion protein and also the release of glycosylated intracellular variants. In addition, extended cell culture resulted in release of such variants. USD mimics of low shear stress, hydrohermetic feed zone centrifugation and of depth filtration were used to demonstrate little to no release during recovery of these variants with both results verified at pilot scale. Furthermore, the USD studies were used to predict removal of contaminants such as lipids, nucleic acids, and cell debris with, for example, depth filtration delivering greater removal than for centrifugation but a small (～10%) decrease in yield of the fusion protein. These USD observations of product recovery and carryover of contaminants were also confirmed at pilot scale as was also the capacity or throughput achievable for continuous centrifugation or for depth filtration. The advantages are discussed of operating a lower yield cell culture and a low shear stress recovery process in return for a considerably less challenging purification demand. Biotechnol. Bioeng. 2013; 110: 1973–1983. © 2013 Wiley Periodicals, Inc.     

miRNA engineering of CHO cells facilitates production of difficult‐to‐express proteins and increases success in cell line development

In recent years, coherent with growing biologics portfolios also the number of complex and thus difficult‐to‐express (DTE) therapeutic proteins has increased considerably. DTE proteins challenge bioprocess development and can include various therapeutic protein formats such as monoclonal antibodies (mAbs), multi‐specific affinity scaffolds (e.g., bispecific antibodies), cytokines, or fusion proteins. Hence, the availability of robust and versatile Chinese hamster ovary (CHO) host cell factories is fundamental for high‐yielding bioprocesses. MicroRNAs (miRNAs) have emerged as potent cell engineering tools to improve process performance of CHO manufacturing cell lines. However, there has not been any report demonstrating the impact of beneficial miRNAs on industrial cell line development (CLD) yet. To address this question, we established novel CHO host cells constitutively expressing a pro‐productive miRNA: miR‐557. Novel host cells were tested in two independent CLD campaigns using two different mAb candidates including a normal as well as a DTE antibody. Presence of miR‐557 significantly enhanced each process step during CLD in a product independent manner. Stable expression of miR‐557 increased the probability to identify high‐producing cell clones. Furthermore, production cell lines derived from miR‐557 expressing host cells exhibited significantly increased final product yields in fed‐batch cultivation processes without compromising product quality. Strikingly, cells co‐expressing miR‐557 and a DTE antibody achieved a twofold increase in product titer compared to clones co‐expressing a negative control miRNA. Thus, host cell engineering using miRNAs represents a promising tool to overcome limitations in industrial CLD especially with regard to DTE proteins. Biotechnol. Bioeng. 2017;114: 1495–1510. © 2017 The Authors. Biotechnology and Bioengineering Published by Wiley Periodicals, Inc.     

An automated laboratory‐scale methodology for the generation of sheared mammalian cell culture samples

Continuous disk‐stack centrifugation is typically used for the removal of cells and cellular debris from mammalian cell culture broths at manufacturing‐scale. The use of scale‐down methods to characterise disk‐stack centrifugation performance enables substantial reductions in material requirements and allows a much wider design space to be tested than is currently possible at pilot‐scale. The process of scaling down centrifugation has historically been challenging due to the difficulties in mimicking the Energy Dissipation Rates (EDRs) in typical machines. This paper describes an alternative and easy‐to‐assemble automated capillary‐based methodology to generate levels of EDRs consistent with those found in a continuous disk‐stack centrifuge. Variations in EDR were achieved through changes in capillary internal diameter and the flow rate of operation through the capillary. The EDRs found to match the levels of shear in the feed zone of a pilot‐scale centrifuge using the experimental method developed in this paper (2.4×10⁵ W/Kg) are consistent with those obtained through previously published computational fluid dynamic (CFD) studies (2.0×10⁵ W/Kg). Furthermore, this methodology can be incorporated into existing scale‐down methods to model the process performance of continuous disk‐stack centrifuges. This was demonstrated through the characterisation of culture hold time, culture temperature and EDRs on centrate quality.     

Prediction and verification of centrifugal dewatering of P. pastoris fermentation cultures using an ultra scale-down approach

Recent years have seen a dramatic rise in fermentation broth cell densities and a shift to extracellular product expression in microbial cells. As a result, dewatering characteristics during cell separation is of importance, as any liquor trapped in the sediment results in loss of product, and thus a decrease in product recovery. In this study, an ultra scale-down (USD) approach was developed to enable the rapid assessment of dewatering performance of pilot-scale centrifuges with intermittent solids discharge. The results were then verified at scale for two types of pilot-scale centrifuges: a tubular bowl equipment and a disk-stack centrifuge. Initial experiments showed that employing a laboratory-scale centrifugal mimic based on using a comparable feed concentration to that of the pilot-scale centrifuge, does not successfully predict the dewatering performance at scale (P-value <0.05). However, successful prediction of dewatering levels was achieved using the USD method (P-value ≥0.05), based on using a feed concentration at small-scale that mimicked the same height of solids as that in the pilot-scale centrifuge. Initial experiments used Baker's yeast feed suspensions followed by fresh Pichia pastoris fermentation cultures. This work presents a simple and novel USD approach to predict dewatering levels in two types of pilot-scale centrifuges using small quantities of feedstock (<50 mL). It is a useful tool to determine optimal conditions under which the pilot-scale centrifuge needs to be operated, reducing the need for repeated pilot-scale runs during early stages of process development.     

A Probasin‐MerCreMer BAC allows inducible recombination in the mouse prostate

Tissue‐specific transgene expression in the prostate epithelium has previously been achieved using short prostate‐specific promoters, rendering transgenic mouse lines susceptible to integration site‐dependent effects. Here we demonstrate the applicability of bacterial artificial chromosome (BAC) technology to transgene expression in the prostate epithelium. We present mouse lines expressing an inducible Cre protein (MerCreMer) under the control of regulatory elements of the probasin gene on a BAC. These mouse lines show high organ specificity, high transgene expression in anterior, dorsal and lateral prostate lobes, no background Cre recombination using a reporter strain and adjustable amounts of Cre‐induced recombination upon tamoxifen induction. Together with two recently reported transgenic lines expressing the Cre‐ERT2 protein from small prostate‐specific promoters, these mouse lines will be useful in research focused on prostate‐specific disorders such as benign hyperplasia or cancer. genesis 47:757–764, 2009. © 2009 Wiley‐Liss, Inc.     

Bone sialoprotein stimulates focal adhesion‐related signaling pathways: Role in migration and survival of breast and prostate cancer cells

Bone sialoprotein (BSP) is a secreted glycoprotein found in mineralized tissues however, BSP is aberrantly expressed in a variety of osteotropic tumors. Elevated BSP expression in breast and prostate primary carcinomas is directly correlated with increased bone metastases and tumor progression. In this study, the intracellular signaling pathways responsible for BSP‐induced migration and tumor survival were examined in breast and prostate cancer cells (MDA‐MB‐231, Hs578T and PC3). Additionally, the effects of exogenous TGF‐β1 and EGF, cytokines associated with tumor metastasis and present in high‐levels in the bone microenvironment, were examined in BSP‐expressing cancer cells. Expression of BSP but not an integrin‐binding mutant (BSP‐KAE) in tumor cell lines resulted in increased levels of α_v‐containing integrins and number of mature focal adhesions. Adhesion of cells to recombinant BSP or the expression of BSP stimulated focal adhesion kinase and ERK phosphorylation, as well as activated AP‐1‐family proteins. Activation of these pathways by BSP expression increased the expression of the matrix metalloproteinases MMP‐2, MMP‐9, and MMP‐14. The BSP‐mediated activation of the FAK‐associated pathway resulted in increased cancer cell invasion in a Matrigel‐coated Boyden‐chamber assay and increased cell survival upon withdrawal of serum. Addition of EGF or TGF‐β1 to the BSP‐expressing cell lines significantly increased ERK phosphorylation, AP‐1 activation, MMP‐2 expression, cell migration and survival compared to untreated cells expressing BSP. This study thus defines the cooperative mechanisms by which BSP can enhance specific factors associated with a metastatic phenotype in tumor cell lines, an effect that is increased by circulating TGF‐β1 and EGF. J. Cell. Biochem. 107: 1118–1128, 2009. © 2009 Wiley‐Liss, Inc.     

A transgenic red fluorescent protein‐expressing nude mouse for color‐coded imaging of the tumor microenvironment

The tumor microenvironment (TME) is critical for tumor growth and progression. We have previously developed color‐coded imaging of the TME using a green fluorescent protein (GFP) transgenic nude mouse as a host. However, most donor sources of cell types appropriate for study in the TME are from mice expressing GFP. Therefore, a nude mouse expressing red fluorescent protein (RFP) would be an appropriate host for transplantation of GFP‐expressing stromal cells as well as double‐labeled cancer cells expressing GFP in the nucleus and RFP in the cytoplasm, thereby creating a three‐color imaging model of the TME. The RFP nude mouse was obtained by crossing non‐transgenic nude mice with the transgenic C57/B6 mouse in which the β‐actin promoter drives RFP (DsRed2) expression in essentially all tissues. In crosses between nu/nu RFP male mice and nu/+ RFP female mice, the embryos fluoresced red. Approximately 50% of the offspring of these mice were RFP nude mice. In the RFP nude mouse, the organs all brightly expressed RFP, including the heart, lungs, spleen, pancreas, esophagus, stomach, duodenum, the male and female reproductive systems; brain and spinal cord; and the circulatory system, including the heart, and major arteries and veins. The skinned skeleton highly expressed RFP. The bone marrow and spleen cells were also RFP positive. GFP‐expressing human cancer cell lines, including HCT‐116‐GFP colon cancer and MDA‐MB‐435‐GFP breast cancer were orthotopically transplanted to the transgenic RFP nude mice. These human tumors grew extensively in the transgenic RFP nude mouse. Dual‐color fluorescence imaging enabled visualization of human tumor–host interaction. The RFP nude mouse model should greatly expand our knowledge of the TME. J. Cell. Biochem. 106: 279–284, 2009. © 2008 Wiley‐Liss, Inc.     

Generic Raman‐based calibration models enabling real‐time monitoring of cell culture bioreactors

Raman‐based multivariate calibration models have been developed for real‐time in situ monitoring of multiple process parameters within cell culture bioreactors. Developed models are generic, in the sense that they are applicable to various products, media, and cell lines based on Chinese Hamster Ovarian (CHO) host cells, and are scalable to large pilot and manufacturing scales. Several batches using different CHO‐based cell lines and corresponding proprietary media and process conditions have been used to generate calibration datasets, and models have been validated using independent datasets from separate batch runs. All models have been validated to be generic and capable of predicting process parameters with acceptable accuracy. The developed models allow monitoring multiple key bioprocess metabolic variables, and hence can be utilized as an important enabling tool for Quality by Design approaches which are strongly supported by the U.S. Food and Drug Administration. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1004–1013, 2015     

Sustaining an efficient and effective CHO cell line development platform by incorporation of 24‐deep well plate screening and multivariate analysis

Efficient and effective cell line screening is paramount toward a successful biomanufacturing program. Here we describe the implementation of 24‐deep well plate (24‐DWP) screening of CHO lines as part of the cell line development platform at AbbVie. Incorporation of this approach accelerated the identification of the best candidate lines for process development. In an effort to quantify and predict process performance comparability, we compared cell culture performance in and in shake flasks, for a panel of Chinese Hamster Ovary cell lines expressing a monoclonal antibody. The results in 24‐DWP screening showed reduced growth profiles, but comparable viability profiles. Slow growers in 24‐DWP achieved the highest productivity improvement upon scaling‐up to shake flasks. Product quality of the protein purified from shake flasks and 24‐DWP were also compared. The 24‐DWP culture conditions were found to influence the levels of acidic species, reduce the G0 N‐glycan species, and increase the high‐mannose N‐glycan species. Nevertheless, the identification of undesirable profiles is executed consistently with the scaled‐up culture. We further employed multivariate data analysis to capture differences depending on the two scales and we could demonstrate that cell line profiles were adequately clustered, regardless of the vessel used for the development. In conclusion, the 24‐DWP platform was reasonably predictive of the parameters crucial for upstream process development activities, and has been adapted as part of the AbbVie cell line development platform. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 34:175–186, 2018