Production enhancement and refolding of caprine growth hormone expressed in Escherichia coli

This study describes comparison between IPTG and lactose induction on expression of caprine growth hormone (cGH), enhancing cell densities of Escherichia coli cultures and refolding the recombinant cGH, produced as inclusion bodies, to biologically active state. 2–3 times higher cell densities were obtained in shake flask cultures when induction was done with lactose showing almost same level of expression as in case of IPTG induction. With lactose induction highest cell densities were achieved in TB (OD₆₀₀ 16.3) and M9NG (OD₆₀₀ 16.1) media, producing 885 and 892 mg cGH per liter of the culture, respectively. Lactose induction done at mid-exponential stage resulted in a higher cell density and thus higher product yield. cGH over-expressed as inclusion bodies was solubilized in 50 mM Tris–Cl buffer (pH 12.5) containing 2 M urea, followed by dilution and lowering the pH in a step-wise manner to obtain the final solution in 50 mM Tris–Cl (pH 9.5). The cGH was purified by Q-Sepharose chromatography followed by gel filtration with a recovery yield of 39% on the basis of total cell proteins. The product thus obtained showed a single band by SDS–PAGE analysis. MALDI-TOF analysis showed a single peak with a mass of 21,851 dalton, which is very close to its calculated molecular weight. A bioassay based on proliferation of Nb2 rat lymphoma cells showed that the purified cGH was biologically active.     

Influence of temperature on the production of an archaeal thermoactive alcohol dehydrogenase from Pyrococcus furiosus with recombinant Escherichia coli

The heterologous production of a thermoactive alcohol dehydrogenase (AdhC) from Pyrococcus furiosus in Escherichia coli was investigated. E. coli was grown in a fed-batch bioreactor in minimal medium to high cell densities (cell dry weight 76 g/l, OD₆₀₀ of 150). Different cultivation strategies were applied to optimize the production of active AdhC, such as lowering the cultivation temperature from 37 to 28°C, heat shock of the culture from 37 to 42°C and from 37 to 45°C, and variation of time of induction (induction at an OD₆₀₀ of 40, 80 and 120). In addition to the production of active intracellular protein, inclusion bodies were always observed. The maximal activity of 30 U/l (corresponding to 6 mg/l active protein) was obtained after a heat shock from 37 to 42°C, and IPTG induction of the adhC expression at an OD₆₀₀ of 120. Although no general rules can be provided, some of the here presented variations may be applicable for the optimization of the heterologous production of proteins in general, and of thermozymes in particular.     

Strategies for high titre plasmid DNA production in Escherichia coli DH5α

The production of plasmid pEGFP-N1 in Escherichia coli DH5α was optimised. A strategy evaluating different media components separately was not successful (OD < 2.5, low plasmid titres), a statistical approach via a Plackett Burman design (11 parameters) allowed some improvement (7 mg/L plasmid, OD₆₀₀ 8.5). Generally, high biomass did not correlate with high plasmid titres. When conditions were transferred to the bioreactor (batch operation) little improvement in plasmid titres (10 mg/L plasmid, OD₆₀₀ 20) was observed. By switching to a fed-batch procedure with linear feeding these values increased to 20 mg/L plasmid (OD₆₀₀ 50). By using an adaptive feeding strategy, plasmid titres could be increased to 50 mg/L. Finally, by combining a growth controlled (reduced temperature (35 °C), low dO₂) initial batch phase with an adaptive feeding strategy in the fed-batch phase (37 °C, glucose-/dO₂-limitation) we were reproducibly able to produce up to 250 mg/L of plasmid DNA in cultures that reached a final OD₆₀₀ of 80.     

Influence of bacterial density during preculture on <Emphasis Type="Italic">Agrobacterium</Emphasis>-mediated transformation of tomato

An improved bacterial preculture protocol for Agrobacterium-mediated genetic transformation was developed for an economic tomato cultivar (Solanum lycopersicum L. cv. Zhongshu No. 4). Frequencies of transient gene expression and stable transformation were influenced by the density of Agrobacterium preculture and not the density of Agrobacterium used for infection. The improved protocol presented in this study depends on the use of an overnight-grown Agrobacterium preculture density of OD_600 nm = 1.0, diluted 1/10th with Luria-Bertani (LB) liquid medium, and grown for an additional 4 h. Cultures are collected and resuspended in a liquid cocultivation medium-I, adjusted to OD_600 nm = 0.1. Using this modified Agrobacterium preparation, transient β-glucuronidase expression was higher than 90%, and transformation efficiency reached 44.7%. This improved transformation is simple, repeatable, does not require a feeder layer, and most notably, the transformation frequency is stable and highly efficient.     

Rapid Isolation of a Single-Chain Antibody against the Cyanobacterial Toxin Microcystin-LR by Phage Display and Its Use in the Immunoaffinity Concentration of Microcystins from Water

A naïve (unimmunized) human semisynthetic phage display library was employed to isolate recombinant antibody fragments against the cyanobacterial hepatotoxin microcystin-LR. Selected antibody scFv genes were cloned into a soluble expression vector and expressed in Escherichia coli for characterization against purified microcystin-LR by competition enzyme-linked immunosorbent assay (ELISA). The most sensitive single-chain antibody (scAb) isolated was capable of detecting microcystin-LR at levels below the World Health Organization limit in drinking water (1 μg liter⁻¹) and cross-reacted with three other purified microcystin variants (microcystin-RR, -LW, and -LF) and the related cyanotoxin nodularin. Extracts of the cyanobacterium Microcystis aeruginosa were assayed by ELISA, and quantifications of microcystins in toxic samples showed good correlation with analysis by high-performance liquid chromatography. Immobilized scAb was also used to prepare immunoaffinity columns, which were assessed for the ability to concentrate microcystin-LR from water for subsequent analysis by high-performance liquid chromatography. Anti-microcystin-LR scAb was immobilized on columns via a hexahistidine tag, ensuring maximum exposure of antigen binding sites, and the performance of the columns was evaluated by directly applying 150 ml of distilled water spiked with 4 μg of purified microcystin-LR. The procedure was simple, and a recovery rate of 94% was achieved following elution in 1 ml of 100% methanol. Large-scale, low-cost production of anti-microcystin-LR scAb in E. coli is an exciting prospect for the development of biosensors and on-line monitoring systems for microcystins and will also facilitate a range of immunoaffinity applications for the cleanup and concentration of these toxins from environmental samples.     

Heterologous production of a temperature and pH-stable laccase from Bacillus vallismortis fmb-103 in Escherichia coli and its application

To enhance laccase yield, the laccase gene from Bacillus vallismortis fmb-103 was cloned and heterologously expressed in Escherichia coli BL21 (DE3) cells. The auto-induction strategy was applied during fermentation, and the process was controlled, as follows: Cu²⁺ was added when the optical density at 600 nm (OD₆₀₀) was 0.3, the fermentation temperature was adjusted to 16 °C when the OD₆₀₀ was 0.9, and fermentation was stopped after 50 h. The yield of recombinant laccase was up to 3420 U/L, as assayed by 2,2-azino-bis(3-ethylbenzothiazoline-6-sulfonic acid). Recombinant laccase was purified 4.47-fold by heating for 10 min at 70 °C and dialyzing against 50–60% ammonium sulfate, retained more than 50% activity after 10 h at 70 °C, and demonstrated broad pH stability. Malachite green was efficiently degraded by recombinant laccase, especially in combination with mediators. These results provided a basis for the future application of recombinant laccase to malachite green degradation.     

High cell density production of <Emphasis Type="Italic">Deinococcus radiodurans</Emphasis> under optimized conditions

Deinococcus radiodurans is a bacterium being investigated for mechanisms of extreme radiation resistance and for bioremediation of environmental radioactive waste sites. In both fundamental and applied research settings, methods for large-scale production of D. radiodurans are needed. In this study, a systematic investigation was carried out to optimize D. radiodurans production at the 20-L fermentor scale. In defined medium, the phosphate buffer typically used was found to be inhibitory to D. radiodurans growth, and caused cell aggregation. Substitution of HEPES and MOPS buffers for phosphate buffer improved D. radiodurans growth characteristics. Several antifoaming agents were investigated to support large-scale production with submerged aeration, and the defoamer KFO 673 was chosen based on its ability to prevent foaming without affecting D. radiodurans growth. The conventional undefined rich medium tryptone/glucose/yeast extract (TGY) maximally supported D. radiodurans growth to an OD₆₀₀ of 10. Using a ‘design of experiments’ approach, we found glucose, Mg and Mn to be critical in supporting high-density growth of D. radiodurans. The optimal pH and temperature for D. radiodurans growth in large-scale preparations were 7.0 and 37°C, respectively. Growth was carried out in a 20-L fermentor using the newly developed media under the optimal conditions. With addition of 10 g/L glucose, 0.5 g/L MgSO₄ · 7H₂O, 5 μM MnCl₂ into TGY media, an OD₆₀₀ of 40 was achieved.     

High-level expression of a functional humanized anti-CTLA4 single-chain variable fragment antibody in <Emphasis Type="Italic">Pichia pastoris</Emphasis>

The administration of antibodies against the cytotoxic T lymphocyte-associated antigen-4 (CTLA-4) is a promising approach in the upregulation of immune responses in many cancers and infectious diseases. The single-chain variable fragment of antibody against CTLA4 is also useful in developing immunotoxins that might be used in the treatment of cancer, transplant rejection, and autoimmune diseases. Here, we report the production of a soluble and functional scFv antibody against CTLA4 by using Pichia pastoris as the expression system. The gene encoding scFv hS83 with an additional 6His-tag at the 5’-end was inserted into the expression vector pPIC9K. Then, the transformants were double-screened on plates containing 0.25 mg/mL and 1.5 mg/mL of neomycin G418 and many clones with different levels of G418-resistance were selected for further studies on expression. After induction by the addition of methanol, various levels of hS83 were detected in the supernatant of P. pastoris containing pPIC9K-hS83. Clones with low G418-resistance produced more hS83 than those with higher G418-resistance. Under the optimized conditions (initial inoculum, 40 A_600nm AU/mL; pH 6.0; methanol concentration, 3.0%; induction time, 72 h), approximately 16–20 mg protein could be recovered from 1 L of the culture. The purified hS83 had a stronger binding ability towards CTLA4-positive Raji cells than CTLA4-negative ECV304 cells. This finding indicates that the antibody produced by P. pastoris is functional and may be used in immunotherapy for cancer, infection, transplant rejection, and autoimmune diseases. Huawei Cai and Lihong Chen contributed equally to this work.     

High‐level conversion of L‐lysine into 5‐aminovalerate that can be used for nylon 6,5 synthesis

L ‐Lysine is a potential feedstock for the production of bio‐based precursors for engineering plastics. In this study, we developed a microbial process for high‐level conversion of L ‐lysine into 5‐aminovalerate (5AVA) that can be used as a monomer in nylon 6,5 synthesis. Recombinant Escherichia coli WL3110 strain expressing Pseudomonas putida delta‐aminovaleramidase (DavA) and lysine 2‐monooxygenase (DavB) was grown to high density in fed‐batch culture and used as a whole cell catalyst. High‐density E. coli WL3110 expressing DavAB, grown to an optical density at 600 nm (OD₆₀₀) of 30, yielded 36.51 g/L 5AVA from 60 g/L L ‐lysine in 24 h. Doubling the cell density of E. coli WL3110 improved the conversion yield to 47.96 g/L 5AVA from 60 g/L of L ‐lysine in 24 h. 5AVA production was further improved by doubling the L ‐lysine concentration from 60 to 120 g/L. The highest 5AVA titer (90.59 g/L; molar yield 0.942) was obtained from 120 g/L L ‐lysine by E. coli WL3110 cells grown to OD₆₀₀ of 60. Finally, nylon 6,5 was synthesized by bulk polymerization of ?‐caprolactam and δ‐valerolactam prepared from microbially synthesized 5AVA. The hybrid system demonstrated here has promising possibilities for application in the development of industrial bio‐nylon production processes.     

Development of highly efficient genetic transformation protocols for table grape Sugraone and Crimson Seedless at low <Emphasis Type="Italic">Agrobacterium</Emphasis> density

Highly efficient genetic transformation protocols and the regeneration of transgenic plants of Sugraone and Crimson Seedless grapevines (Vitis vinifera L.) were achieved from embryogenic calli co-cultured with low Agrobacterium tumefaciens densities. The sensitivity of embryogenic cultures to kanamycin, as well as the effect of Agrobacterium strains, C58(pMP90) or EHA105, and the bacterial concentration (0.06 or 0.2 at Optical Density OD₆₀₀) on transformation efficiency were studied. Embryogenic cultures showed different kanamycin sensitivities and the total suppression of embryo differentiation at 20 and 50 mg/l kanamycin for Crimson Seedless and Sugraone, respectively. sgfp gene expression was evaluated in callus co-cultured with each bacterial strain. Although GFP transient expression was higher with A. tumefaciens EHA105 in both cultivars at the beginning of the culture, there were no significant differences 28 days post-inoculation. However, the concentration of Agrobacterium did affected transformation efficiency: 0.06 OD₆₀₀ being more effective for the transformation of Crimson Seedless and 0.2 OD₆₀₀ for Sugraone. By following the optimised procedure, 21 and 26 independent transgenic plants were generated from Sugraone and Crimson Seedless respectively, three to five months post-infection. PCR analyses were carried out to verify the integration of the sgfp and nptII genes into grapevine genome and the stable integration of the sgfp gene was confirmed by Southern blot.     

STATISTICAL OPTIMIZATION OF GREEN FLUORESCENT PROTEIN PRODUCTION FROM Escherichia coli BL21(DE3)

An optimized cultivation condition is needed to maximize the functional green fluorescent protein (GFP) production. Six process variables (agitation rate, temperature, initial medium pH, concentration of inducer, time of induction, and inoculum density) were screened using the fractional factorial design. Three variables (agitation rate, temperature, and time of induction) exerted significant effects on functional GFP production in E. coli shake flask cultivation and were optimized subsequently using the Box–Behnken design. An agitation rate of 206 rpm at 31°C and induction of the protein expression when the cell density (OD_600nm) reaches 1.04 could enhance the yield of functional GFP production from 0.025 g/L to 0.241 g/L, which is about ninefold higher than the unoptimized conditions. Unoptimized cultivation conditions resulted in protein aggregation and hence reduced the quantity of functional GFP. The model and regression equation based on the shake flask cultivation could be applied to a 2-L bioreactor for maximum functional GFP production.     

High-level production of heterologous proteins using untreated cane molasses and corn steep liquor in Escherichia coli medium

To develop an economical industrial medium, untreated cane molasses (UCM) was tested as a carbon source for fermentation culturing of Escherichia coli. To test the industrial application of this medium, we chose a strain co-expressing a carbonyl reductase (PsCR) and a glucose dehydrogenase (BmGDH). Although corn steep liquor (CSL) could be used as an inexpensive nitrogen source to replace peptone, yeast extract could not be replaced in E. coli media. In a volume of 40 ml per 1-l flask, a cell concentration of optical density (OD₆₀₀) 15.1 and enzyme activities of 6.51 U/ml PsCR and 3.32 U/ml BmGDH were obtained in an optimized medium containing 25.66 g/l yeast extract, 3.88 g/l UCM, and 7.1% (v/v) CSL. When 3.88 g/l UCM was added to the medium at 6 h in a fed-batch process, the E. coli concentration increased to OD₆₀₀ of 24, and expression of both PsCR and BmGDH were twofold higher than that of a batch process. Recombinant cells from batch or fed-batch cultures were assayed for recombinant enzyme activity by testing the reduction of ethyl 4-chloro-3-oxobutanoate to ethyl (S)-4-chloro-3-hydroxybutanoate (CHBE). Compared to cells from batch cultures, fed-batch cultured cells showed higher recombinant enzyme expression, producing 560 mM CHBE in the organic phase with a molar yield of 92% and an optical purity of the (S)-isomer of >99% enantiomeric excess.     

Temperature gradient-based high-cell density fed-batch fermentation for the production of pyruvate oxidase by recombinant E. coli

Pyruvate oxidase (PyOD) is a very powerful enzyme for clinical diagnostic applications and environmental monitoring. Influences of temperature on cell growth, plasmid stability, and PyOD expression during the PyOD fermentation process by recombinant Escherichia coli were investigated. Based on the influences of temperature on the physiological metabolism, a novel high-cell density fed-batch cultivation with gradient temperature decrease strategy for effective PyOD production was achieved, under which the biomass (OD₆₀₀) of recombinant E. coli could reach to 71 and the highest PyOD activity in broth could reach to 3,307 U/L in 26?hr fermentation.     

Improved expression characteristics of single-chain Fv fragments when fused downstream of the Escherichia coli maltose-binding protein or upstream of a single immunoglobulin-constant domain

The expression of single-chain Fv fragments (scFv) targeted to the periplasm of Escherichia coli often results in very low yields of soluble protein frequently accompanied by host cell growth arrest and sometimes lysis. Single-chain antibody fragments (scAb) are scFv with a human kappa light chain constant (HuCkappa) domain attached C-terminally and share similar problems of expression. By fusing the E. coli maltose-binding protein (mbp) gene either 3' or 5' to a scAb specific for the herbicide atrazine, a reduction in growth arrest was observed that was dependent on the order of gene fusion. The scAb-mbp fusion delayed the onset of growth arrest following induction while the mbp-scAb fusion appeared to ablate growth arrest completely. Cell fractionation revealed barely detectable levels of scAb-mbp in the periplasm while mbp-scAb was detected at equivalent levels as scAb in the periplasmic compartment, indicating that periplasmic scAb solubility is unrelated to propensity to cause growth arrest. IMAC purification of scAb and mbp-scAb proteins followed by liquid competition ELISA revealed the IC(50) for atrazine to be approximately 1 nM for both proteins demonstrating that 5'-mbp fusion does not alter antigen binding. The equivalent scFv and mbp-scFv vectors expressed far less material in both periplasmic and insoluble fractions indicating that the HuCkappa domain can have a positive effect on scFv expression when expressed either alone or as a mbp fusion. The ablation of growth arrest by a 5'-mbp fusion and enhancement of expression by a 3'-HuCkappa domain fusion were extended to a second scFv specific for the herbicide diuron. Therefore, by expressing scFv as tripartite fusions (mbp-scFv-HuCkappa) enhanced levels of soluble periplasmic expression can be achieved without causing growth arrest of the host cell, realizing the potential for constitutive expression of hapten-binding scFv in the E. coli periplasm.     

Non-linear population dynamics in chemostats associated with live-dead cell cycling in Escherichia coli strain K12-MG1655

Bacterial populations conditionally display non-linear dynamic behaviour in bioreactors with steady inputs, which is often attributed to varying habitat conditions or shifting intracellular metabolic activity. However, mathematical modelling has predicted that such dynamics also might simply result from staggered birth, growth, and death events of groups of cells within the population, causing density oscillations and the cycling of live and dead cells within the system. To assess this prediction, laboratory experiments were performed on Escherichia coli strain K12-MG1655 grown in chemostats to first define fine-scale population dynamics over time (minutes) and then determine whether the dynamics correlate with live–dead cell cycles in the system. E. coli populations displayed consistent oscillatory behaviour in all experiments. However, close synchronisation between OD₆₀₀ and live–dead cell oscillations (within ~33–38 min cycles) only became statistically significant (p < 0.01) when pseudo-steady state operations approaching carrying capacity existed in the bioreactor. Specifically, live cells were highest at local OD₆₀₀ maxima and lowest at local OD₆₀₀ minima, showing that oscillations followed live–dead cell cycles as predicted by the model and also consistent with recent observations that death is non-stochastic in such populations. These data show that oscillatory dynamic behaviour is intrinsic in bioreactor populations, which has implications to process operations in biotechnology.     

An altered camelid-like single domain anti-idiotypic antibody fragment of HM-1 killer toxin: acts as an effective antifungal agent

Phage-display and competitive panning elution leads to the identification of minimum-sized antigen binders together with conventional antibodies from a mouse cDNA library constructed from HM-1 killer toxin neutralizing monoclonal antibody (nmAb-KT). Antigen-specific altered camelid-like single-domain heavy chain antibody (scFv K2) and a conventional antibody (scFv K1) have been isolated against the idiotypic antigen nmAb-KT. The objectives of the study were to examine (1) their properties as compared to conventional antibodies and also (2) their antifungal activity against different pathogenic and non-pathogenic fungal species. The alternative small antigen-binder, i.e., the single-domain heavy chain antibody, was originated from a conventional mouse scFv phage library through somatic hyper-mutation while selection against antigen. This single-domain antibody fragment was well expressed in bacteria and specifically bound with the idiotypic antigen nmAb-KT and had a high stability and solubility. Experimental data showed that the binding affinity for this single-domain antibody was 272-fold higher (K _d = 1.07 × 10⁻¹⁰ M) and antifungal activity was three- to fivefold more efficient (IC₅₀ = 0.46 × 10⁻⁶ to 1.17 × 10⁻⁶ M) than that for the conventional antibody (K _d = 2.91 × 10⁻⁸ M and IC₅₀ = 2.14 × 10⁻⁶ to 3.78 × 10⁻⁶ M). The derived single-domain antibody might be an ideal scaffold for anti-idiotypic antibody therapy and the development of smaller peptides or peptide mimetic drugs due to their less complex antigen-binding site. We expect that such single-domain synthetic antibodies will find their way into a number of biotechnological or medical applications.     

High cell density cultivation and recombinant protein production with <Emphasis Type="Italic">Escherichia coli</Emphasis> in a rocking-motion-type bioreactor

Background

Single-use rocking-motion-type bag bioreactors provide advantages compared to standard stirred tank bioreactors by decreased contamination risks, reduction of cleaning and sterilization time, lower investment costs, and simple and cheaper validation. Currently, they are widely used for cell cultures although their use for small and medium scale production of recombinant proteins with microbial hosts might be very attractive. However, the utilization of rocking- or wave-induced motion-type bioreactors for fast growing aerobic microbes is limited because of their lower oxygen mass transfer rate. A conventional approach to reduce the oxygen demand of a culture is the fed-batch technology. New developments, such as the BIOSTAT^® CultiBag RM system pave the way for applying advanced fed-batch control strategies also in rocking-motion-type bioreactors. Alternatively, internal substrate delivery systems such as EnBase^® Flo provide an opportunity for adopting simple to use fed-batch-type strategies to shaken cultures. Here, we investigate the possibilities which both strategies offer in view of high cell density cultivation of E. coli and recombinant protein production.

Results

Cultivation of E. coli in the BIOSTAT^® CultiBag RM system in a conventional batch mode without control yielded an optical density (OD₆₀₀) of 3 to 4 which is comparable to shake flasks. The culture runs into oxygen limitation. In a glucose limited fed-batch culture with an exponential feed and oxygen pulsing, the culture grew fully aerobically to an OD₆₀₀ of 60 (20 g L^-1 cell dry weight). By the use of an internal controlled glucose delivery system, EnBase^® Flo, OD₆₀₀ of 30 (10 g L^-1 cell dry weight) is obtained without the demand of computer controlled external nutrient supply. EnBase^® Flo also worked well in the CultiBag RM system with a recombinant E. coli RB791 strain expressing a heterologous alcohol dehydrogenase (ADH) to very high levels, indicating that the enzyme based feed supply strategy functions well for recombinant protein production also in a rocking-motion-type bioreactor.

Conclusions

Rocking-motion-type bioreactors may provide an interesting alternative to standard cultivation in bioreactors for cultivation of bacteria and recombinant protein production. The BIOSTAT^® Cultibag RM system with the single-use sensors and advanced control system paves the way for the fed-batch technology also to rocking-motion-type bioreactors. It is possible to reach cell densities which are far above shake flasks and typical for stirred tank reactors with the improved oxygen transfer rate. For more simple applications the EnBase^® Flo method offers an easy and robust solution for rocking-motion-systems which do not have such advanced control possibilities.

     

High cell density transient transfection of CHO cells for TGF‐β1 expression

High cell densities for transient transfection with polyethyleneimine (PEI) can be used for rapid and maximal production of recombinant proteins. High cell densities can be obtained by different cultivation systems, such as batch or perfusion systems. Herein, densities up to 18 million cells/mL were obtained by centrifugation for transfection evaluation. PEI transfection efficiency was easily determined by transfected enhanced green fluorescence protein (EGFP) reporter plasmid DNA (pDNA). A linear correlation between fluorescence intensity and transfection efficiency was improved. The transfection efficiency of PEI was highly dependent on the transfection conditions and directly related to the level of recombinant protein. Several factors were required to optimize the transient transfection process; these factors included the media type (which is compatible with low or high cell density transfection), the preculture CHO‐K1 suspension cell density, and the pDNA to PEI level. Based on design of experiment (DoE) analyses, the optimal transfection conditions for 10 × 10⁶ cells/mL in the CHOMACS CD medium achieved 73% transfection efficiency and a cell viability of over 80%. These results were confirmed for the production of transforming growth factor‐beta 1 (TGF‐β1) in a shake flask. The purified TGF‐β1 protein concentration from 60 mL supernatant was 27 µg/mL, and the protein was biologically active.