Although historically used for the treatment of anemia, erythropoietin (EPO) has emerged as a neurotrophic and neuroprotective agent in different conditions of neuronal damage (traumatic brain injury, ischemia, spinal cord compression, peripheral neuropathy, retinal damage, epilepsy, Parkinson's Disease, among others). Nonetheless, EPO's therapeutic application is limited due to its hematological side-effects. With the aim of obtaining EPO derivatives resembling the hormone isolated from cells and tissues of neural origin, a novel combination of less acidic EPO glycoforms -designated as neuroepoetin (rhNEPO)- was purified to homogeneity from the supernatant of a CHO-producing cell line by a four-step chromatographic procedure. This simple and single process allowed us to prepare two EPO derivatives with distinct therapeutic expectations: the hematopoietic version and a minimally hematopoietic, but mainly in vitro cytoprotective, alternative. Further biological characterization showed that the in vivo erythropoietic activity of rhNEPO was 25-times lower than that of rhEPO. Interestingly, using different in vitro cytoprotective assays we found that this molecule exerts cytoprotection equivalent to, or better than, that of rhEPO in cells of neural phenotype. Furthermore, despite its shorter plasma half-life, rhNEPO was rapidly absorbed and promptly detected in the cerebrospinal fluid after intravenous administration in rats (5 min postinjection, in comparison with 30 min for rhEPO). Therefore, our results support the study of neuroepoetin as a potential drug for the treatment of neurological diseases, combining high cytoprotective activity with reduced hematological side-effects.

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This article reports the results obtained from comparison of internal spin filter (ISF) and alternating flow filtration (ATF) as cell retention systems, regarding cell growth, volumetric perfusion rate, cell specific perfusion rate and cell productivity in the fermentation process. As expected we were able to reach higher cell densities and to achieve longer runs since ATF systems are known to be less affected by fouling. Volumetric production of the reactor using the ATF system was 50-70% higher than the production achieved using the ISF due to higher cell density and a two-fold increase in the perfusion rate. On the other hand, downstream processing performances were evaluated regarding chromatographic steps yields and productivity and quality attributes of the purified materials. Similar results were obtained for all evaluated systems. The fact that we were able to achieve a 2 working volumes (WV)/day perfusion rate using an ATF system as cell retention device allowed us to virtually double the WV of a 25 L reactor. These results constitute valuable data for the optimization of recombinant protein production in perfusion processes since a two-fold increase in the average production of a manufacturing facility could be easily achieved as long as downstream scale up is possible. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1010-1014, 2017.

Recent trends in the pharmaceutical sector are changing the way protein purification processes are designed and executed, moving from operating the process in a fixed point to allowing a permissible region in the operating space known as design space. This trend is driving product development to design quality into the manufacturing process (Quality by Design) and not to rely exclusively on testing quality in the product. A typical purification step has numerous operating parameters that can impact its performance. Therefore, optimization and robustness analysis in purification processes can be time-consuming since they are mainly grounded on experimental work. A valuable approach consists in the combination of an adequate risk analysis technique for selecting the relevant factors influencing process performance and the design of experiment methodology. The latter allows for many process variables which can be studied at the same time; thus, the number of tests will be reduced in comparison with the conventional approach based on trial and error. These multivariate studies permit a detailed exploration in the experimental range and lay the foundation of Quality by Design principles application. This article outlines a recommended sequence of activities toward the establishment of an expanded design space for a purification process.

A typical chromatographic purification step has numerous operating parameters that can impact its performance. As it is not feasible to evaluate the influence of each one, the current practice in biopharmaceutical industry is to apply risk analysis approach to identify process parameters that should be examined during process characterization. Once these parameters are identified, a response surface study can be run to help understand the relationship between critical inputs and outputs. We performed a study comprising optimization and robustness determination for a Blue-Sepharose purification step of rhEPO, a well-known therapeutic glycoprotein. Initially, risk analysis was fulfilled to identify key parameters. A small-scale model was created and qualified before its use in experimental studies, given by a Box-Behnken design with three factors. This method proved to be a very useful tool in bioprocess validation studies in which many input variables can affect product quality and safety.

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