Engineering robust protein production and purification of correctly folded biotherapeutic proteins in cell-based systems is often challenging due to the requirements for maintaining complex cellular networks for cell viability and the need to develop associated downstream processes that reproducibly yield biopharmaceutical products with high product quality. Here, we present an alternative Escherichia coli-based open cell-free synthesis (OCFS) system that is optimized for predictable high-yield protein synthesis and folding at any scale with straightforward downstream purification processes. We describe how the linear scalability of OCFS allows rapid process optimization of parameters affecting extract activation, gene sequence optimization, and redox folding conditions for disulfide bond formation at microliter scales. Efficient and predictable high-level protein production can then be achieved using batch processes in standard bioreactors. We show how a fully bioactive protein produced by OCFS from optimized frozen extract can be purified directly using a streamlined purification process that yields a biologically active cytokine, human granulocyte-macrophage colony-stimulating factor, produced at titers of 700 mg/L in 10 h. These results represent a milestone for in vitro protein synthesis, with potential for the cGMP production of disulfide-bonded biotherapeutic proteins. Biotechnol. Bioeng. 2011; 108:1570–1578. © 2011 Wiley Periodicals, Inc.

(2012) Aglycosylated antibodies and antibody fragments produced in a scalable in vitro transcription-translation system, mAbs, 4:2, 217-225,

Escherichia coli extracts activate cell-free protein synthesis systems by providing the catalysts for translation and other supporting reactions. Recent results suggest that high-density fermentations can be used to provide the source cells, but the subsequent cell extract preparation procedure requires multiple centrifugation and dialysis steps as well as an expensive runoff reaction. In the work reported here, the extract preparation protocol duration was reduced by nearly 50% by significantly shortening several steps. In addition, by optimizing the runoff incubation, overall reagent costs were reduced by 70%. Nonetheless, extracts produced from the shorter, less expensive procedure were equally active. Crucial steps were further examined to indicate minimal ribosome loss during the standard 30,000g centrifugations. Furthermore, sucrose density centrifugation analysis indicated that although an incubation step significantly activates the extract, ribosome/polysome dissociation is not required. These insights suggest that consistent cell extract can be produced more quickly and with considerably less expense for large-scale cell-free protein production, especially when combined with high-density fermentation protocols.

Cell‐free protein synthesis (CFPS) systems allow for robust protein expression with easy manipulation of conditions to improve protein yield and folding. Recent technological developments have significantly increased the productivity and reduced the operating costs of CFPS systems, such that they can compete with conventional in vivo protein production platforms, while also offering new routes for the discovery and production of biotherapeutics. As cell‐free systems have evolved, productivity increases have commonly been obtained by addition of components to previously designed reaction mixtures without careful re‐examination of the essentiality of reagents from previous generations. Here we present a systematic sensitivity analysis of the components in a conventional Escherichia coli CFPS reaction mixture to evaluate their optimal concentrations for production of the immunoglobulin G trastuzumab. We identify eight changes to the system, which result in optimal expression of trastuzumab. We find that doubling the potassium glutamate concentration, while entirely eliminating pyruvate, coenzyme A, NAD, total tRNA, folinic acid, putrescine and ammonium glutamate, results in a highly productive cell‐free system with a 95% reduction in reagent costs (excluding cell‐extract, plasmid, and T7 RNA polymerase made in‐house). A larger panel of other proteins was also tested and all show equivalent or improved yields with our simplified system. Furthermore, we demonstrate that all of the reagents for CFPS can be combined in a single freeze‐thaw stable master mix to improve reliability and ease of use. These improvements are important for the application of the CFPS system in fields such as protein engineering, high‐throughput screening, and biotherapeutics. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:823–831, 2015

A novel feeding strategy that prolongs rapid growth rates for Escherichia coli fermentations to moderately high cell density is presented. High-density fermentations are a common and successful means of producing biological products. However, acetate accumulation can be a substantial problem in these procedures. To avoid this problem, many feeding strategies and host modifications have been developed, but all result in relatively low growth rates. If a faster growth rate could be maintained, the growth phase of the process would be shortened, leading to increased productivity. It is also possible that the subsequent specific production rate could be enhanced by growing the early culture at a faster rate. We have developed a procedure to enable rapid growth to a cell density of 20 g/L and have used cell-free protein synthesis to evaluate the relative potential of the resulting cells for producing recombinant proteins. The method uses glucose pulses and the duration of the dissolved oxygen response to calculate the appropriate glucose feed rate based on the glucose demand of the culture. Amino acids and vitamins were supplied in the medium to increase the growth rate. We were able to sustain a growth rate of 0.8/h up to 20 g/L dry cell weight without significant acetate accumulation. Analysis of amino acid consumption indicates that cell composition is an accurate predictor of amino acid demand for most amino acids. Cell-free protein synthesis was used to compare the protein production potential of the high-density cultures with that of cells grown in complex medium and harvested at low cell density and maximum growth rate. Protein production for the extract from the controlled, high-density fermentations was 950 mg/L compared with 860 mg/L for the low-density control. Therefore, the new control procedure has promising potential for developing rapid and productive industrial fermentations.

Cell-free protein synthesis is a useful research tool and now stands poised to compete with in vivo expression for commercial production of proteins. However, both the extract preparation and protein synthesis procedures must be scaled up. A key challenge is producing the required amount of biomass that also results in highly active cell-free extracts. In this work, we show that the growth rate of the culture dramatically affects extract performance. Extracts prepared from cultures with a specific growth rate of 0.7/h or higher produced approximately 0.9 mg/mL of chloramphenicol acetyl transferase (CAT) in a batch reaction. In contrast, when the source culture growth rate was 0.3/h, the resulting extract produced only 0.5 mg/mL CAT. Examination of the ribosome content in the extracts revealed that the growth rate of the source cells strongly influenced the final ribosome concentration. Polysome analysis of cell-free protein synthesis reactions indicated that about 22% of the total 70S ribosomes are in polysomes for all extracts regardless of growth rate. Furthermore, the overall specific production from the 70S ribosomes is about 22 CAT proteins per ribosome over the course of the reaction in all cases. It appears that rapid culture growth rates are essential for producing a productive extract. However, growth rate does not seem to influence specific ribosome activity. Rather, the increase in extract productivity is a result of a higher ribosome concentration. These results are important for cell-free technology and also suggest an assay for intrinsic in vivo protein synthesis activity.

Cell-free protein synthesis systems use a crude cell extract to produce proteins. While these systems have many advantages over in vivo expression systems, the current procedures for preparation of the cell extract are very labor-intensive. In addition, since they start with low cell density cultures, the methods yield small amounts of final extract. Fed-batch fermentations were performed with a defined medium and a glucose feeding strategy designed to meet metabolic demand but avoid acetate production. We have investigated cultures with cell densities from 3 to 50 OD595 for extract preparation. Furthermore, the effect of growth rate (0.2 to 1.1 /hr) on extract performance was studied in glucose-limited cultures. The glucose feeding strategy was able to control acetate production in some fermentations but not in others. The feeding of amino acids may have caused the variability. Neither cell density nor growth rate had a significant impact on protein synthesis by the cell-free extract. Finally, a relA and spoT null mutant grew more slowly, but still produced extract with the same activity as the parent relAl spoTl strain.

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