Refolding and purification of recombinant L-asparaginase from inclusion bodies of E. coli into active tetrameric protein.

A tetrameric protein of therapeutic importance, Escherichia coli L-asparaginase-II was expressed in Escherichia coli as inclusion bodies (IBs). Asparaginase IBs were solubilized using low concentration of urea and refolded into active tetrameric protein using pulsatile dilution method. Refolded asparaginase was purified in two steps by ion-exchange and gel filtration chromatographic techniques. The recovery of bioactive asparaginase from IBs was around 50%. The melting temperature (Tm) of the purified asparaginase was found to be 64°C. The specific activity of refolded, purified asparaginase was found to be comparable to the commercial asparaginase (190 IU/mg). Enzymatic activity of the refolded asparaginase was high even at four molar urea solutions, where the IB aggregates are completely solubilized. From the comparison of chemical denaturation data and activity at different concentrations of guanidine hydrochloride, it was observed that dissociation of monomeric units precedes the complete loss of helical secondary structures. Protection of the existing native-like protein structure during solubilization of IB aggregates with 4 M urea improved the propensity of monomer units to form oligomeric structure. Our mild solubilization technique retaining native-like structures, improved recovery of asparaginase in bioactive tetrameric form.

Optimization of human granulocyte macrophage-colony stimulating factor (hGM-CSF) expression using asparaginase and xylanase gene's signal sequences in Escherichia coli.

The toxicity of the recombinant protein towards the expression host remains a significant deterrent for bioprocess development. In this study, the expression of human granulocyte macrophage-colony stimulating factor (hGM-CSF), which is known to be toxic to its host, was enhanced many folds using a combination of genetic and bioprocess strategies in Escherichia coli. The N terminus attachment of endoxylanase and asparaginase signal sequences from Bacillus subtilis and E. coli, respectively, in combination with and without His-tag, considerably improved expression levels. Induction and media optimization studies in shake flask cultures resulted in a maximal hGM-CSF concentration of 365 mg/L in the form of inclusion bodies (IBs) with a specific product yield (Y (P/X)) of 120 mg/g dry cell weight in case of the asparaginase signal. Culturing the cells in nutrient rich Terrific broth maintained the specific product yields (Y (P/X)) while a 6.6-fold higher volumetric concentration of both product and biomass was obtained. The purification and refolding steps were optimized resulting in a 95% pure protein with a fairly high refolding yield of 45%. The biological activity of the refolded protein was confirmed by a cell proliferation assay on hGM-CSF dependent human erythroleukemia TF-1 cells. This study demonstrated that this indeed is a viable route for the efficient production of hGM-CSF.

Single chain Fv fragment specific for human GM-CSF: selection and expression using a bacterial expression library.

Single chain antibodies (scFvs) are replacing whole antibody molecules since they are easy to produce on large scale and amenable to genetic modifications. Here we report the development of an anti-human granulocyte macrophage colony-stimulating factor (hGM-CSF) scFv as an immunoassay bio-reagent, utilizing an easily scalable bacterial expression system. For this, the V(H) and V(L) gene repertoires were amplified from the immunoglobulin complementary DNA, derived from total RNA of mice splenocytes, pre-sensitized with the antigen. The scFv library was expressed under the strong T7 promoter in BL21 (DE3) Escherichia coli cells. Preliminary screening led to the selection of four potential candidates, which were later subjected to light chain shuffling. Cross-reactivity analysis involving the original and shuffled candidates resulted in the selection of one scFv (scFv196) with no cross-reactivity against E. coli antigens. The binding affinity of the scFv196 for hGM-CSF, measured by surface plasmon resonance, was found to be within the physiological range (K(D) =1.5 µM). The refolded scFv was also shown to recognize and bind the glycosylated antigen, a closer mimic of the physiological GM-CSF, potentiating its use in immunoassays. Expression studies using shake flasks suggested periplasmic export of the scFv196 protein.

Kinetic studies of recombinant human interferon-gamma expression in continuous cultures of E. coli.

A series of continuous cultures was performed to understand the product formation kinetics of recombinant human interferon gamma (rhIFN-gamma) in Escherichia coli at different dilution rates ranging from 0.1 to 0.3 h(-1) in different media. A T7 promoter-based vector was used for expression of IFN-gamma in E. coli BL21 (DE3) cells. The recombinant protein was produced as inclusion bodies, thus allowing a rapid buildup of rhIFN-gamma inside the cell, with the specific product yield (Y(p/X)) reaching a maximum value of 182 mg g(-1) dry cell weight (DCW). In all the media tested, the specific product formation rate (q(p)) was found to be strongly correlated with the specific growth rate (mu), demonstrating the growth-associated nature of product formation. The q(p) values show no significant decline with time postinduction, even though the recombinant protein has been over produced inside the cell. The maximum q(p) level of 75.5 mg g(-1) h(-1) was achieved at the first hour of induction at the dilution rate of 0.3 h(-1). Also, this correlation between q(p) and mu was not critically dependent on media composition, which would made it possible to grow cells in defined media in the growth phase and then push up the specific growth rate just before induction by pulse addition of glucose and yeast extract. This would ensure the twin objectives of high biomass and high specific productivities, leading to high volumetric product concentration.

Kinetic studies of constitutive human granulocyte-macrophage colony stimulating factor (hGM-CSF) expression in continuous culture of Pichia pastoris.

Extracellular human granulocyte-macrophage colony stimulating factor (hGM-CSF) expression was studied under the control of the GAP promoter in recombinant Pichia pastoris in a series of continuous culture runs (dilution rates from 0.025 to 0.2 h(-1)). The inlet feed concentration was also varied and the steady state biomass concentration increased proportionally demonstrating efficient substrate utilization and constancy of the biomass yield coefficient (Y(x/s)) for a given dilution rate. The specific product formation rate (q(P)) showed a strong correlation with dilution rates demonstrating growth associated product formation of hGM-CSF. The volumetric product concentration achieved at the highest feed concentration (4x) and a dilution rate of 0.2 h(-1) was 82 mg l(-1) which was 5-fold higher compared to the continuous culture run with 1x feed concentration at the lowest dilution rate thus translating to a 40 fold increase in the volumetric productivity. The specific product yield (Y(P/X)) increased slightly from 2 to 2.5 mg g(-1), with increasing dilution rates, while it remained fairly invariant, for all feed concentrations demonstrating negligible product degradation or feed back inhibition. The robust nature of this expression system would make it easily amenable to scale up for industrial production.

Development of expression vectors for Escherichia coli based on the pCR2 replicon.

BACKGROUND: Recent developments in metabolic engineering and the need for expanded compatibility required for co-expression studies, underscore the importance of developing new plasmid vectors with properties such as stability and compatibility. RESULTS: We utilized the pCR2 replicon of Corynebacterium renale, which harbours multiple plasmids, for constructing a range of expression vectors. Different antibiotic-resistance markers were introduced and the vectors were found to be 100% stable over a large number of generations in the absence of selection pressure. Compatibility of this plasmid was studied with different Escherichia coli plasmid replicons viz. pMB1 and p15A. It was observed that pCR2 was able to coexist with these E. coli plasmids for 60 generations in the absence of selection pressure. Soluble intracellular production was checked by expressing GFP under the lac promoter in an expression plasmid pCR2GFP. Also high level production of human IFNgamma was obtained by cloning the h-IFNgamma under a T7 promoter in the expression plasmid pCR2-IFNgamma and using a dual plasmid heat shock system for expression. Repeated sub-culturing in the absence of selection pressure for six days did not lead to any fall in the production levels post induction, for both GFP and h-IFNgamma, demonstrating that pCR2 is a useful plasmid in terms of stability and compatibility. CONCLUSION: We have constructed a series of expression vectors based on the pCR2 replicon and demonstrated its high stability and sustained expression capacity, in the absence of selection pressure which will make it an efficient tool for metabolic engineering and co-expression studies, as well as for scale up of expression.

Process optimization of constitutive human granulocyte-macrophage colony-stimulating factor (hGM-CSF) expression in Pichia pastoris fed-batch culture.

Human granulocyte-macrophage colony-stimulating factor (hGM-CSF) is a therapeutically important cytokine that is poorly expressed because of its toxic effects on the host cells. Extracellular expression of hGM-CSF was obtained by cloning its gene in Pichia pastoris under the constitutive glyceraldehyde-3-phosphate dehydrogenase (GAP) promoter with an N-terminal alpha peptide sequence for its extracellular production. The clones obtained were screened for a hyper producer following which media and cultivation conditions were optimized in shake flasks. Batch and fed-batch studies were performed in a bioreactor where different feed compositions were fed exponentially to obtain high biomass concentrations. Feeding of complex media allowed us to maintain a high specific growth rate of 0.2 h(-1) for the longest time period, and a final biomass of 98 g DCW/l was obtained in 34 h. Product formation was found to be growth associated, and the product yield with respect to biomass (Y (P/X)) was approximately 2.5 mg/g DCW. The above fed-batch strategy allowed us to obtain fairly pure glycosylated hGM-CSF at a final product concentration of 250 mg/l in the culture supernatant with a high volumetric productivity of 7.35 mg l(-1) h(-1).

Overexpression and purification of recombinant human interferon alpha2b in Escherichia coli.

Overexpression of rhIFN-alpha2b was obtained by synthesizing a codon optimized gene for IFN-alpha2b and expressing it in the form of inclusion bodies (IBs) in Escherichia coli. The recombinant plasmid pRSET-IFNalpha, which had the IFN-alpha2b gene under the T7 promoter, was coexpressed with plasmid pGP1-2, which carried the gene for T7 RNA polymerase under the heat inducible lambdaP(L) promoter. This two plasmid expression system was optimized with respect to heat shock time, media, and time of induction in shake flask cultures. This was then scaled up into a bioreactor to get a maximum volumetric product yield of 5.2g/L at a final OD(600) of 67. At this point, the IBs represented approximately 40% of the total cellular protein. This high specific product yields eased the further downstream processing steps and improved product recoveries. The IBs were isolated and purified through ion exchange followed by step refolding to give a final product yield of approximately 3g/L, which is maximum reported in the literature. The bioassay of the refolded protein gave a specific activity of approximately 3 x 10(9)IU/mg protein.

Optimization of extracellular production of recombinant asparaginase in Escherichia coli in shake-flask and bioreactor.

Various host-vector combinations were tested to maximize the extracellular production of recombinant asparaginase in Escherichia coli. Expression of recombinant asparaginase fused to pelB leader sequence under the inducible T7lac promoter in BLR (DE3) host cells resulted in optimum extracellular production in shake-flasks. Fed-batch studies were carried out using this recombinant strain and an exponential feeding strategy was used to maintain a specific growth rate of 0.3 h(-1). To check the effect of the time of induction on expression, cultures were induced with 1 mM isopropyl-beta-D-thiogalactopyranoside at varying cell optical densities (OD(600): 33, 60, 90, 135). Although the specific product formation rates declined with increasing OD of induction, a maximum volumetric activity of 8.7 x 10(5) units l(-1), corresponding to approximately 5.24 g l(-1) of recombinant asparaginase, was obtained when induction was done at an OD(600) of 90. The recombinant protein was purified directly from the culture medium, using a rapid two-step purification strategy, which resulted in a recovery of approximately 70% and a specific activity of approximately 80% of that of the native enzyme.

Extracellular expression and single step purification of recombinant Escherichia coli L-asparaginase II.

L-Asparaginase (isozyme II) from Escherichia coli is an important therapeutic enzyme used in the treatment of leukemia. Extracellular expression of recombinant asparaginase was obtained by fusing the gene coding for asparaginase to an efficient pelB leader sequence and an N-terminal 6x histidine tag cloned under the T7lac promoter. Media composition and the induction strategy had a major influence on the specificity and efficiency of secretion of recombinant asparaginase. Induction of the cells with 0.1 mM IPTG at late log phase of growth in TB media resulted in fourfold higher extracellular activity in comparison to growing the cells in LB media followed by induction during the mid log phase. Using an optimized expression strategy a yield of 20,950 UI/L of recombinant asparaginase was obtained from the extracellular medium. The recombinant protein was purified from the culture supernatant in a single step using Ni-NTA affinity chromatography which gave an overall yield of 95 mg/L of purified protein, with a recovery of 86%. This is approximately 8-fold higher to the previously reported data in literature. The fluorescence spectra, analytical size exclusion chromatography, and the specific activity of the purified protein were observed to be similar to the native protein which demonstrated that the protein had folded properly and was present in its active tetramer form in the culture supernatant.

Studies of single-chain antibody expression in quiescent Escherichia coli.

Quiescent Escherichia coli cells are generated by overexpressing the Rcd transcript in an hns-205 mutant host. The resulting nongrowing, metabolically active cells were used here to express a single-chain antibody fragment (scFv) in shake flask and fermentor cultures. The expression system is based on two plasmids; one carries the product gene expressed from lambdaP(L) under the control of the cI857 temperature-sensitive repressor, while the second expresses Rcd from lambdaP(R). Shifting the culture from 30 to 42 degrees C induces Rcd expression and product expression simultaneously. Our scFv carried a PelB leader, and 90% of the protein was secreted into the culture supernatant. In a batch culture, the supernatant concentration of scFv in the quiescent-cell culture (optical density at 600 nm [OD(600)] of 3.5) was 37 mg x liter(-1), compared to a maximum of 13 mg x liter(-1) in the control culture (final OD(600) of 20). In a fed-batch fermentor culture, quiescent cells were held at an OD(600) of 20 for 24 h and the extracellular scFv concentration reached a maximum of 150 mg x liter(-1). A control culture with a similar feed reached an OD(600) of 80, but despite the higher density, the extracellular scFv concentration did not exceed 35 mg x liter(-1). Quiescent cells at an OD(600) of 50 exhibited a small decline in the specific product formation rate, but nevertheless, an extracellular scFv concentration of 160 mg x liter(-1) was achieved in 8 h. The rate of extracellular accumulation was 10-fold greater in the quiescent culture than in the control culture. This study demonstrates that it is possible to establish high-density quiescent E. coli cultures that are capable of efficient synthesis, folding, and export of proteins.

Stability studies of recombinant Saccharomyces cerevisiae in the presence of varying selection pressure.

A recombinant yeast plasmid carrying the Ieu2 gene for auxotrophic complementation and a reporter gene for beta-galactosidase under the control of Gal10 promoter was studied in Saccharomyces cerevisiae. Growth, product formation, and plasmid stability were studied in defined, semi-defined, and complex media. The biomass concentration and specific activity were higher in complex medium than in defined medium, which was selective for the growth of plasmid-containing cells, leading to a 10-fold increase in volumetric activity. However, plasmid instability was very high in complex media with 50% plasmid-free cells emerging in the culture within 75 h of cultivation. In order to control instability, the growth rates of the plasmid-containing and plasmid-free cells were determined in semi-defined media, which consisted of defined medium supplemented with different concentrations of yeast extract. Below a critical concentration of yeast extract (0.05 g/L), the plasmid-containing cells had a growth rate advantage over the plasmid-free cells. This was possibly because, at this concentration of yeast extract, the availability of leucine became the rate-determining factor in the specific growth rate of plasmid-free cells. A feeding strategy was designed which maintained a low concentration of the residual yeast extract in the medium and thus continuously provided the plasmid-containing cells with a competitive advantage over the plasmid-free cells. This resulted in high stability as well as high cell density under non-selective conditions, which led to a 10-fold increase in the volumetric activity compared to that achieved in defined selective media. A simple mathematical model was formulated to verify the experimental data. The important state variables and process parameters, i.e., biomass concentration, beta-galactosidase expression, sucrose consumption, yeast extract consumption, and specific growth rates of the two cell populations, were evaluated. These variables and parameters along with the differential equations based on material balances as well as the experimental results obtained were used in a mathematical model for the fed-batch cultivation. These correctly verified the experimental data and clearly illustrated the concept behind the success of the fed-batch strategy under yeast extract starvation.

Stable maintenance of plasmid in continuous culture of yeast under non-selective conditions.

A recombinant yeast plasmid containing the gene for beta-galactosidase was tested for stability in a host auxotrophic for leucine. Plasmid loss was studied at different dilution rates in continuous culture under selective as well as non-selective conditions. It was observed that the instability of the culture was higher at low dilution rates in selective medium, while the pattern was reversed when complex non-selective medium was used, with plasmid-containing cells competing effectively with plasmid-free cells at low dilution rates. This was attributed to a low residual yeast extract concentration in the medium at low dilution rates. Since yeast extract was the sole source of leucine, this limited the growth of plasmid-free cells, which were auxotrophic for leucine. Growth rate studies also indicated a competitive advantage of the plasmid-containing cells over the plasmid-free cells at low yeast extract concentrations in semi-defined medium. Using the above data, a modified continuous culture was run using non-selective medium at a low dilution rate of 0.05 h(-1). This resulted in stable coexistence of plasmid-containing and plasmid-free cells and hence sustained expression of beta-galactosidase at approximately 330 OD420l(-1) h(-1) throughout the period of cultivation (134 h).

Cloning, characterization, and expression of xylanase gene from Bacillus lyticus in Escherichia coli and Bacillus subtilis.

A genomic library of Bacillus lyticus was constructed in lambda GEM 11 vector and screened for the xylanase gene using Congo red plate assay. A 16-kb fragment containing the xylanase gene was obtained which was further subcloned using Mbo I partial digestion in an E. coli pUC 19 vector. A 1.3-kb sub-fragment was obtained which coded for a xylanase gene of Mr 23,650 Da. This fragment was sequenced and the homology was checked with known xylanases. The maximum homology was 97%, which was obtained with an endo xylanase gene from Bacillus species at the DNA level, while the translated sequence showed only one amino acid change from alanine to serine at position number 102. Expression was checked in E. coli, using the native promoter, and an extracellular activity of 5.25 U/mL was obtained. Cloning of the gene was done in Bacillus subtilis using a shuttle vector pHB 201, which resulted in increasing the basal level xylanase activity from 14.02 to 22.01 U/mL.

Enhancing recombinant protein yields in Escherichia coli using the T7 system under the control of heat inducible lambda PL promoter.

A recombinant plasmid containing the complete lacZ gene downstream of the T7 promoter was used to transform Escherichia coli containing another plasmid which had the T7 RNA polymerase gene under the control of heat inducible lambda PL promoter. This recombinant E. coli containing the two plasmids was studied in order to enhance beta-galactosidase expression. The heat shock time which effectively regulates the T7 RNA polymerase was optimized and best expression of beta-galactosidase was obtained with 2 min heat shock. Substrate feeding increased the duration of log phase and allowed induction at a higher cell density without affecting the specific activity. A high cell density (7 g l-1) and high specific activity (approximately 20,000 U) were achieved which effectively increased the product concentration 18-fold.

A single step purification process for cyclodextrin glucanotransferase from a Bacillus sp. isolated from soil.

Cyclodextrin glucanotransferase (CGTase) is a commercially important enzyme which catalyses the formation of cyclodextrins (CDs) from starch. A CGTase producing bacterium was isolated from soil which gave a fairly high enzyme activity of 7.5 U mL(-1) after 24 h of growth which was further increased to 22 U mL(-1) by proper media design. The enzyme was purified to homogeneity by a novel single affinity precipitation step which resulted in a very high recovery of more than 90%. The molecular weight, as determined by SDS-PAGE, was found to be 68 kDa. The pH optimum was found to be 6.6 while a temperature optimum of 65 degrees C was observed. The enzyme exhibited a fairly high degree of functional stability with little loss of activity, even after 8 h of incubation at 65 degrees C. Ca++ had little effect on the activity of the enzyme while urea at 10 mM concentration increased the activity of the enzyme by more than 200%, suggesting that it is a unique enzyme.

Construction of vector of Brevibacterium lactofermentum and study of its stability in continuous culture.

A 5.7-kb vector plasmid pBK2 was constructed by ligating the kanamycin resistance gene from Escherichia coli plasmid pACYC177 to an endogenous cryptic 4.4-kb plasmid of Brevibacterium lactofermentum ATCC 21086. The vector replicates efficiently and is stably maintained in the host and other coryneforms. However, the copy number varied from 50 to 10 per chromosome-equivalent under different culture conditions. Continuous culture studies showed instability when low dilution rates were used. Co-culture experiments were performed at various dilution rates to measure the growth rate ratio (alpha) of the plasmid-free cells to the plasmid-containing cells. It was observed that at low dilution rates the value of alpha was higher than that at high dilution rates. Thus, the instability of the plasmid can be attributed to the increase in alpha at low dilution rates. Modelling of instability using a random partitioning model of plasmid segregation and experimentally obtained values of alpha showed agreement with experimental data. This demonstrated that active partitioning is not the operative mechanism for plasmid segregation in this case.