Analysis of Recombinant Human Serum Albumin Extraction and Degradation in Transgenic Rice Extracts.

Transgenic plant systems have successfully been used to express recombinant proteins, including rice seed-expressed recombinant human serum albumin (rHSA), without the risk of contamination of human pathogens. Developing an efficient extraction process is critical as the step determines recombinant protein concentration and purity, quantity of impurities, and process volume. This article evaluates the effect of pH and time on the extraction and stability of rHSA. The amount of rHSA in clarified extract after 60 min of solubilization increased with pH from 0.9 mg/g (pH 3.5) to 9.6 mg/g (pH 6.0), but not over time as 10 min was sufficient for solubilization. Total soluble protein in extracts also increased with pH from 3.9 mg/g (pH 3.5) to 19.7 mg/g (pH 6.0) in clarified extract. Extraction conditions that maximized rHSA purity were not optimal for rHSA stability and yield. Extraction at pH 3.5 resulted in high purity (78%), however, rHSA degraded over time. Similar purities (78%) were observed in pH 4.0 extracts yet rHSA remained stable. rHSA degradation was not observed in pH 4.5 and 6.0 extracts but higher native protein concentrations decreased purity. Strategies such as pH and temperature adjustment were effective for reducing rHSA degradation in pH 3.5 rice extracts. Low temperature pH 3.5 extraction retained high purity (97%) and rHSA stability. While seed-expressed recombinant proteins are known to be stable for up to 3 years, the degradation of rHSA was notably extensive (56% within 60 min) when extracted at low pH. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:681-691, 2018.

Recovery and purification of plant-made recombinant proteins.

Plants are becoming commercially acceptable for recombinant protein production for human therapeutics, vaccine antigens, industrial enzymes, and nutraceuticals. Recently, significant advances in expression, protein glycosylation, and gene-to-product development time have been achieved. Safety and regulatory concerns for open-field production systems have also been addressed by using contained systems to grow transgenic plants. However, using contained systems eliminates several advantages of open-field production, such as inexpensive upstream production and scale-up costs. Upstream technological achievements have not been matched by downstream processing advancements. In the past 10 years, the most research progress was achieved in the areas of extraction and pretreatment. Extraction conditions have been optimized for numerous proteins on a case-by-case basis leading to the development of platform-dependent approaches. Pretreatment advances were made after realizing that plant extracts and homogenates have unique compositions that require distinct conditioning prior to purification. However, scientists have relied on purification methods developed for other protein production hosts with modest investments in developing novel plant purification tools. Recently, non-chromatographic purification methods, such as aqueous two-phase partitioning and membrane filtration, have been evaluated as low-cost purification alternatives to packed-bed adsorption. This paper reviews seed, leafy, and bioreactor-based platforms, highlights strategies for the primary recovery and purification of recombinant proteins, and compares process economics between systems. Lastly, the future direction and research needs for developing economically competitive recombinant proteins with commercial potential are discussed.

Evaluation of monoclonal antibody and phenolic extraction from transgenic Lemna for purification process development.

Several pharmaceutical protein products made in transgenic plant hosts are advancing through clinical trials. Plant hosts present a different set of impurities from which the proteins must be purified compared to other expression hosts such as mammalian cells. In this work, phenolic compounds present in extracts of monoclonal antibody (mAb)-expressing Lemna minor were examined. Two different extraction pHs were evaluated to assess the effect of extraction condition on the concentration of mAb and phenolics in the extracts. The extract prepared at pH 4.5 had an enriched level of mAb relative to native protein when compared to a pH 7.5 extract although similar overall mAb was extracted at either pH. Slightly more mAb was recovered from the pH 3 elution of the pH 4.5 extract run on a MabSelect column than was recovered from the pH 7.5 extract. Phenolic levels in extracts were assessed by spectrophotometry, Folin-Ciocalteu assay and by profiling on RP-HPLC. The Folin-Ciocalteu assay results did not agree with those obtained by the other two methods. Therefore phenolic levels were quantified by RP-HPLC comparing the total area of phenolic peaks to those of reference phenolic compounds. The pH 7.5 extract had 22% less phenolics than the pH 4.5 extract. Acidic precipitation of the pH 7.5 extract resulted in further reduction of phenolics originally present in the pH 7.5 extract. The total phenolics present in the extracts were effectively removed by incubation of extracts with a commercially available anion exchange resin, Amberlite IRA-402. We anticipate that early removal of phenolic compounds will prolong the life of more expensive affinity columns used for the purification of potential pharmaceutical proteins and should therefore be considered in process development involving proteins extracted from transgenic plant hosts.