Recombinant enterokinase light chain with affinity tag: expression from Saccharomyces cerevisiae and its utilities in fusion protein technology.

Enterokinase and recombinant enterokinase light chain (rEK(L)) have been used widely to cleave fusion proteins with the target sequence of (Asp)(4)-Lys. In this work, we show that their utility as a site-specific cleavage agent is compromised by sporadic cleavage at other sites, albeit at low levels. Further degradation of the fusion protein in cleavage reaction is due to an intrinsic broad specificity of the enzyme rather than to the presence of contaminating proteases. To offer facilitated purification from fermentation broth and efficient removal of rEK(L) after cleavage reaction, thus minimizing unwanted cleavage of target protein, histidine affinity tag was introduced into rEK(L). Utilizing the secretion enhancer peptide derived from the human interleukin 1 beta, the recombinant EK(L) was expressed in Saccharomyces cerevisiae and efficiently secreted into culture medium. The C-terminal His-tagged EK(L) was purified in a single-step procedure on nickel affinity chromatography. It retained full enzymatic activity similar to that of EK(L), whereas the N-terminal His-tagged EK(L) was neither efficiently purified nor had any enzymatic activity. After cleavage reaction of fusion protein, the C-terminal His-tagged EK(L) was efficiently removed from the reaction mixture by a single passage through nickel-NTA spin column. The simple affinity tag renders rEK(L) extremely useful for purification, post-cleavage removal, recovery, and recycling and will broaden the utility and the versatility of the enterokinase for the production of recombinant proteins.     

Expression,purification, and characterization of a biologically active bovine enterokinase catalytic subunit in Escherichia coli

Enterokinase (EC 3.4.21.9) is a serine proteinase in the duodenum that exhibits specificity for the sequence (Asp)(4)-Lys. It converts trypsinogen to trypsin. Its high specificity for the recognition site makes enterokinase (EK) a useful tool for in vitro cleavage of fusion proteins. cDNA encoding the catalytic chain of Chinese bovine enterokinase was cloned and its encoding amino acid sequence is identical to the previously reported sequence although there are two one-base mutations which do not change the encoded amino acid. The EK catalytic subunit cDNA was cloned into plasmid pET32a, and fused downstream to the fusion partner thioredoxin (Trx) and the following DDDDK enterokinase recognition sequence. The recombinant bovine enterokinase catalytic subunit was expressed in Escherichia coli BL21(DE3), and most products existed in soluble form. After an in vivo autocatalytic cleavage of the recombinant Trx-EK catalytic domain fusion protein, intact, biologically active EK catalytic subunit was released from the fusion protein. The recombinant intact EK catalytic subunit was purified to homogeneity with a specific activity of 720 AUs/mg protein through ammonium sulfate precipitation, DEAE chromatography, and gel filtration. The purified intact EK catalytic subunit has a K(m) of 0.17 mM, and K(cat) is 20.8s(-1). From 100 ml flask culture, 4.3 mg pure active EK catalytic subunits were obtained.     

Enhancement of Taxol production and excretion in Taxus chinensis cell culture by fungal elicitation and medium renewal

An endophytic fungus, Aspergillus niger, isolated from the inner bark of a Taxus chinensis tree, was used as an elicitor to stimulate the Taxol (paclitaxel) production in a Taxus chinensis cell suspension culture. Different elicitor doses and elicitation times were tested in a batch culture; and the highest volumetric Taxol yield was achieved when 40 mg of the fungal elicitor (carbohydrate equivalent) l(-1) was added to the culture during the late exponential-growth phase. The elicitation resulted in a more than two-fold increase in the Taxol yield and about a six-fold increase in total secretion. The Taxol yield was further improved substantially by applying medium renewal and re-elicitation to the culture. In particular, with repeated medium renewal (in a way similar to medium perfusion) and a second elicitation of the culture, the volumetric Taxol yield was increased to 67.1+/-7.5 mg l(-1), which was about seven times the amount obtained in the non-elicited batch culture. The Taxol productivity of the perfusion-like culture with repeated fungal elicitation was 1.5 mg l(-1) day(-1), which was about 40% higher than that of the elicitor-treated batch culture and three times the productivity of the non-elicited batch culture.     

Hirudin as a novel fusion tag for efficient production of lunasin in Escherichia coli

Fusion expression provides an effective means for the biosynthesis of longer peptides in Escherichia coli. However, the commonly used fusion tags are primarily suitable for laboratory scale applications due to the high cost of commercial affinity resins. Herein, a novel approach exploiting hirudin as a multipurpose fusion tag in combination with tobacco etch virus (TEV) protease cleavage has been developed for the efficient and cost-effective production of a 43-amino acid model peptide lunasin in E. coli at preparative scale. A fusion gene which allows for lunasin to be N-terminally fused to the C-terminus of hirudin through a flexible linker comprising a TEV protease cleavage site was designed and cloned in a secretion vector pTASH. By cultivation in a 7-L bioreactor, the fusion protein was excreted into the culture medium at a high yield of ~380?mg/L, which was conveniently recovered and purified by inexpensive HP20 hydrophobic chromatography at a recovery rate of ~80%. After polishing and cleavage with TEV protease, the finally purified lunasin was obtained with ≥95% purity and yield of ~86?mg/L culture medium. Conclusively, this hirudin tagging strategy is powerful in the production of lunasin and could be applicable for the production of other peptides at preparative scale.     

The expression and purification of human rhinovirus protease 3C

Human rhinovirus type 14 protease 3C was expressed as a soluble and active protein in Escherichia coli. The protease was purified by a cationic-exchange step followed by gel filtration on a TSK 3000 column. The final yield of purified protease was in the range 0.5-1.0 mg/l culture grown to A550 = 1.0. Sequence analysis revealed that greater than 90% of the N-terminal residues were methionine. The enzyme activity of the purified protease was measured by cleavage of a synthetic peptide representing a predicted Gln/Gly viral polyprotein cleavage site. A mutant protease (Cys146----Ser) was produced and purified in the same way. The yield of mutant protease 3C was approximately 150 micrograms/l from a culture grown to A550 = 1.0. This mutant protease 3C did not cleave the synthetic peptide substrate.     

Purification and refolding optimization of recombinant bovine enterokinase light chain overexpressed in Escherichia coli

The nucleotide sequence encoding bovine enterokinase light chain (EK) from Chinese northern yellow bovine was isolated. Two single-nucleotide mutations, namely, C245G and A528T were identified. The gene encoding the Pro82Arg/Glu176Asp variant of known bovine EK was fused with glutathione S-transferase and overexpressed mainly as an inclusion body in Escherichia coli BL21 (DE3), upon induction with IPTG and glucose. Effective fusion protein purification, refolding, auto-catalytic cleavage and mature EK recovery were described. The specific activity of the purified EK was determined as 110+/- 10 U/mg, which was comparable to a specific activity of > or =20 U/mg of the E. coli expressed EK sample provided by Sigma (Cat. No. E4906). This procedure produced approximately 53 mg of EK per 500 mL of cell culture, which was much higher than previous reports, thus providing a basis for large-scale production of EK and for further applications in biotechnology.     

Production of tissue plasminogen activator (t-PA) in Aspergillus niger

A protease-deficient strain of Aspergillus niger has been used as a host for the production of human tissue plasminogen activator (t-PA). In defined medium, up to 0.07 mg t-PA (g biomass)(-1) was produced in batch and fed-batch cultures and production was increased two- to threefold in two-phase batch cultures in which additional glucose was provided as a single pulse at the end of the first batch growth phase. Production was increased [up to 1.9 mg t-PA (g biomass)(-1)] by the addition of soy peptone to the defined medium. The rate of t-PA production in batch cultures supplemented with soy peptone (0.2 to 0.6 mg t-PA L(-1) h(-1)) was comparable to rates observed previously in high-producing mammalian or insect cell cultures. In glucose-limited chemostat culture supplemented with soy peptone, t-PA was produced at a rate of 0.7 mg t-PA L(-1) h(-1). Expression of t-PA in A. niger resulted in increased expression of genes (bipA, pdiA, and cypB) involved in the unfolded protein response (UPR). However, when cypB was overexpressed in a t-PA-producing strain, t-PA production was not increased. The t-PA produced in A. niger was cleaved into two chains of similar molecular weight to two-chain human melanoma t-PA. The two chains appeared to be stable for at least 16 h in culture supernatant of the host strain. However, in general, <1% of the t-PA produced in A. niger was active, and active t-PA disappeared from the culture supernatant during the stationary phase of batch cultures, suggesting that the two-chain t-PA may have been incorrectly processed or that initial proteolytic cleavage occurred within the proteolytic domain of the protein. Total t-PA (detected by enzyme-linked immunoassay) also eventually disappeared from culture supernatants, confirming significant extracellular proteolytic activity, even though the host strain was protease-deficient.     

Expression of recombinant chinese bovine enterokinase catalytic subunit in P. pastoris and its purification and characterization

EK (enterokinase) is a serine proteinase which consistsof a heavy chain and a light chain linked by a disulfidebond. The light chain of EK contains a chymotrypsin-likeserine proteinase domain sufficient for the normal recog-nition and cleavage of EK subst…     

Expression of human parathyroid hormone-(1-84) in Escherichia coli as a factor X-cleavable fusion protein

Recombinant human parathyroid hormone (hPTH)-(1-84) was obtained from Escherichia coli using a cleavable fusion protein strategy. The fusion protein contains residues 1-138 of human growth hormone as the amino-terminal region and residues 1-84 of hPTH as the carboxyl-terminal region. A 7-residue linker containing the recognition/cleavage sequence of the site-specific blood coagulation protease activated factor X (factor Xa) joins the two regions. Intact hPTH-(1-84) is released from this fusion protein by cleavage in vitro with factor Xa. The fusion protein was produced at a high level and formed inclusion bodies which allowed it to be easily purified by low speed centrifugation, with a yield of approximately 50 mg/liter of culture. After factor Xa cleavage and high performance liquid chromatography purification, highly purified hPTH was obtained, with a final yield of 1.5-3 mg/liter. Physical and biological characterization of the purified hormone demonstrated that it was intact and active hPTH-(1-84).     

Efficient callus formation and plant regeneration of goosegrass [<Emphasis Type="Italic">Eleusine indica </Emphasis>(L.) Gaertn.]

Efficient methods in totipotent callus formation, cell suspension culture establishment and whole-plant regeneration have been developed for the goosegrass [ Eleusine indica (L.) Gaertn.] and its dinitroaniline-resistant biotypes. The optimum medium for inducing morphogenic calli consisted of N6 basal salts and B5 vitamins supplemented with 1-2 mg l(-1) 2,4-dichlorophenoxyacetic acid (2,4-D), 2 mg l(-1) glycine, 100 mg l(-1) asparagine, 100 mg l(-1) casein hydrolysate, 30 g l(-1) sucrose and 0.6% agar, pH 5.7. The presence of organogenic and embryogenic structures in these calli was histologically documented. Cell suspension cultures derived from young calli were established in a liquid medium with the same composition. Morphogenic structures of direct shoots and somatic embryos were grown into rooted plantlets on medium containing MS basal salts, B5 vitamins, 1 mg l(-1) kinetin (Kn) and 0.1 mg l(-1) indole-3-acetic acid (IAA), 3% sucrose, 0.6% agar, pH 5.7. Calli derived from the R-biotype of E. indica possessed a high resistance to trifluralin (dinitroaniline herbicide) and cross-resistance to a structurally non-related herbicide, amiprophosmethyl (phosphorothioamidate herbicide), as did the original resistant plants. Embryogenic cell suspension culture was a better source of E. indica protoplasts than callus or mesophyll tissue. The enzyme solution containing 1.5% cellulase Onozuka R-10, 0.5% driselase, 1% pectolyase Y-23, 0.5% hemicellulase and N(6) mineral salts with an additional 0.2 M KCl and 0.1 M CaCl(2) (pH 5.4-5.5) was used for protoplast isolation. The purified protoplasts were cultivated in KM8p liquid medium supplemented with 2 mg l(-1) 2,4-D and 0.2 mg l(-1) Kn.     

Expression, purification, and characterization of the recombinant calcium-binding equine lysozyme secreted by the filamentous fungus Aspergillus niger: comparisons with the production of hen and human lysozymes.

Equine lysozyme (EqL) has been expressed from a synthetic gene and secreted from a heterologous host, the filamentous fungus Aspergillus niger. By including 100 mM Ca2+ in the growth medium, secreted yields of more than 50 mg/liter could be achieved using polyvinylpyrrolidone (PVP) complete medium. In a soya medium yields of up to 150 mg/liter were achieved. The production of recombinant human lysozyme (HuL) from A. niger with yields of over 40 mg/liter was also achieved using PVP medium. Addition of Ca2+ to the growth medium reduced the yield of both HuL and hen egg white lysozyme (HEWL). Sequence differences between the three lysozymes, EqL, HuL, and HEWL, resulted in different susceptibilities to cleavage by A. niger proteases. An improved procedure for the purification of EqL and HuL from A. niger allowed separation of the proteins from pigments produced by the fungus. Detailed spectroscopic analysis, including 2D 1H NMR, for recombinant EqL and recombinant HuL confirm that both proteins possess their native structure and are purified to homogeneity.     

In vitro control of fasciation in proliferating nucellar embryos of Mangifera indica L. var totapari red small for cloning

Nucellar tissue contained in ovular halves of young fruits of Mangifera indica L. totapari red small, a dwarfing rootstock, differentiated fasciated embryonal structures in presence of 6-benzylaminopurine [BAP(0.15 mg l(-1))], 6-(gamma-gamma-dimethylallylamino) purine [2iP(0.15 mg l(-1))] and indole-3-acetic acid [(IAA(0.5 mg l(-1))] incorporated in the semisolid medium during 50-60 days. Due to embryonal fasciation, hardly 2-3 well-formed embryos could be obtained per culture of proliferating embryos. Of the 3 ethylene inhibitors [L-alpha-(2-aminoethoxyvinyl)-glycine-HCl (AVG), AgNO3 and salicylic acid (SA)] used, embryonal fasciation and necrosis of intervening tissue was completely controlled by 3-4 subcultures of fasciated mass of embryos under the influence of AVG (0.05 mg l(-1)) in presence of adenine sulphate [AdS (50 mg l(-1))] incorporated in the same medium. Almost synchronized development of isolated embryos, measuring ca 2 cm in length, was observed in a different medium used in liquid stationary state and supplemented, particularly with stress-producing substances [abscisic acid (ABA, 0.01 mg l(-1)); and polyethylene glycol (PEG, 100 mg l(-1))] besides certain other modifications. About 34% convertibility of processed embryos was obtained during a period of 90 days. The plantlets had well-developed roots along with laterals which were longer than leafy shoots. In vitro raised plants survived ex vitro for about 2 months.     

An improved strategy for high-level production of TEV protease in Escherichia coli and its purification and characterization

Because of its stringent sequence specificity, tobacco etch virus (TEV) protease emerges as a useful reagent with wide application in the cleavage of recombinant fusion proteins. However, the solubility of TEV protease expressed in Escherichia coli is extremely low. In the present study, we introduced a more efficient system to improve and facilitate the soluble production of TEV protease in E. coli. Optimal expression of soluble His6-TEV was achieved by examining the contribution of chaperone co-expression and lower temperature fermentation. When further purified by Ni(2+) affinity chromatography, 65mg of His6-TEV was isolated with purity over 95% from 1L of culture. The enzyme activity of His6-TEV was generally characterized by using GST-EGFP and His6-L-TNF fusion protein as substrates, which contained a TEV cleavage site between two moieties.     

Growth-rate-independent production of recombinant glucoamylase by Fusarium venenatum JeRS 325

Most recombinant proteins generated in filamentous fungi are produced in fed-batch cultures, in which specific growth rate normally decreases progressively with time. Because of this, such cultures are more suited to the production of products that are produced efficiently at low-growth rates (e.g., penicillin) than to products which are produced more efficiently at high-growth rates (e. g., glucoamylase). Fusarium venenatum A3/5 has been transformed (JeRS 325) to produce Aspergillus niger glucoamylase (GAM) under the control of the Fusarium oxysporum trypsin-like protease promoter. No glucoamylase was detected in the culture supernatant during exponential growth of F. venenatum JeRS 325 in batch culture. In glucose-limited chemostat cultures, GAM concentration increased with decrease in dilution rate, but the specific production rate of GAM (g GAM [g biomass](-1) h(-1)) remained approximately constant over the dilution-rate range 0.05 h to 0.19 h(-1), i.e., the recombinant protein was produced in a growth-rate-independent manner. The specific production rate decreased at dilution rates of 0.04 h(-1) and below. Specific production rates of 5.8 mg and 4.0 mg GAM [g biomass](-1) h(-1) were observed in glucose-limited chemostat cultures in the presence and absence of 1 g mycological peptone L(-1). Compared to production in batch culture, and for the same final volume of medium, there was no increase in glucoamylase production when cultures were grown in fed-batch culture. The results suggested that a chemostat operated at a slow dilution rate would be the most productive culture system for enzyme production under this trypsin-like promoter.     

Enhanced kefiran production by mixed culture of Lactobacillus kefiranofaciens and Saccharomyces cerevisiae

In a batch mixed culture of Lactobacillus kefiranofaciens and Saccharomyces cerevisiae, which could assimilate lactic acid, cell growth and kefiran production rates of L. kefiranofaciens significantly increased, compared with those in pure cultures. The kefiran production rate was 36 mg l(-1) h(-1) in the mixed culture under the anaerobic condition, which was greater than that in the pure culture (24 mg l(-1) h(-1)). Under the aerobic condition, a more intensive interaction between these two strains was observed and higher kefiran production rate (44 mg l(-1) h(-1)) was obtained compared with that under the anaerobic condition. Kefiran production was further enhanced by an addition of fresh medium in the fed-batch mixed culture. In the fed-batch mixed culture, a final kefiran concentration of 5.41 g l(-1) was achieved at 87 h, thereby attaining the highest productivity at 62 mg l(-1) h(-1). Simulation study considered the reduction of lactic acid in pure culture was performed to estimate the additional effect of coculture with S. cerevisiae. Slightly higher cell growth and kefiran production rates in the mixed culture than those expected from pure culture by simulation were observed. These results suggest that coculture of L. kefiranofaciens and S. cerevisiae not only reduces the lactic acid concentration by consumption but also stimulates cell growth and kefiran production of L. kefiranofaciens.     

甘蓝下胚轴原生质体再生植株

经纯化后,甘蓝下胚轴原生质体的产量为1．5×10⁶g^-1(Fw),采用液体浅层培养的方法进行培养。2～3d后,发生第一次分裂,第10天,统计分裂频率为6l％,5周内形成大量的细胞团和小愈伤组织,统计植板率为1．1％,把小愈伤组织转到与原生质体培养基相同激素的MS固体培养基上增殖。当愈伤组织长到3～5mm大小时,接到分化培养基上,芽分化率为46.7％．分化出来的芽长到3～4cm长时,从基部切下,插入生根培养基,两星期左右即可长成完整植株。     

A novel and simple method for high-level production of reverse transcriptase from Moloney murine leukemia virus (MMLV-RT) in <Emphasis Type="Italic">Escherichia coli</Emphasis>

A novel protocol for producing recombinant Moloney murine leukemia virus (MMLV-RT) in Escherichia coli is reported. The optimized coding sequence for mature MMLV-RT was cloned into pET28a and over-expressed as an N-terminal His6-tagged fusion protein. An enterokinase (EK) recognition site was introduced between the His6-tag and MMLV-RT to release tag-free enzyme. Optimal expression of soluble His6-MMLV-RT was achieved by chaperone co-expression and lower temperature fermentation. The His6-tagged enzyme was first purified by Ni²⁺ affinity chromatography. The bound enzyme was then eluted by EK digestion and the eluate was purified on an anion-exchange Q column to remove DNA and EK. Twenty-one milligram MMLV-RT was obtained from 1 l of bacterial culture.     

Integrated bioprocess for production of human proinsulin C-peptide via heat release of an intracellular heptameric fusion protein

An integrated bioprocess has been developed suitable for production of recombinant peptides using a gene multimerization strategy and site-specific cleavage of the resulting gene product. The process has been used for production in E. coli of the human proinsulin C-peptide via a fusion protein BB-C7 containing seven copies of the 31-residues C-peptide monomer. The fusion protein BB-C7 was expressed at high level, 1.8 g l(-1), as a soluble gene product in the cytoplasm. A heat treatment procedure efficiently released the BB-C7 fusion protein into the culture medium. This step also served as an initial purification step by precipitating the majority of the host cell proteins, resulting in a 70% purity of the BB-C7 fusion protein. Following cationic polyelectrolyte precipitation of the nucleic acids and anion exchange chromatography, native C-peptide monomers were obtained by enzymatic cleavage at flanking arginine residues. The released C-peptide material was further purified by reversed-phase chromatography and size exclusion chromatography. The overall yield of native C-peptide at a purity exceeding 99% was 400 mg l(-1) culture, corresponding to an overall recovery of 56%. The suitability of this process also for the production of other recombinant proteins is discussed.     

Production of 2-hydroxy-4-methoxybenzaldehyde in roots of tissue culture raised and acclimatized plants of Decalepis hamiltonii Wight & Arn., an endangered shrub endemic to Southern India and evaluation of its performance vis-a-vis plants from natural habitat

Axillary buds obtained from field grown plants of D. hamiltonii were used to initiate multiple shoots on Murashige and Skoog's medium (MS) supplemented with 2 mg L(-1) 6-benzyl aminopurine (BA) and 0.5 mg L(-1) indole-3-acetic acid (IAA). Profuse rooting was achieved when the actively growing shoots were cultured on MS medium supplemented with 1.0 mg l(-1) indole-3-butyric acid (IBA). Regenerated plants were grown successfully in the plains, in contrast to wild growth in high altitudes and rocky crevices of hilly regions. Roots of different sizes from one-year-old tissue culture raised field grown plants had the same profile of 2-hydroxy-4-methoxybenzaldehyde as that of wild plants. A maximum of 0.14% and 0.12% 2-hydroxy-4-methoxybenzaldehyde was produced in roots of one year old tissue culture derived plants and greenhouse grown plants respectively.     

Purification and partial characterization of azoreductase from Enterobacter agglomerans

Azoreductase, an enzyme catalyzing the reductive cleavage of the azo bond of methyl red (MR) and related dyes, was purified to electrophoretic homogeneity from Enterobacter agglomerans. This bacterial strain, isolated from dye-contaminated sludge, has a higher ability to grow, under aerobic conditions, on culture medium containing 100mg/L of MR. The enzyme was purified approximately 90-fold with 20% yield by ammonium sulfate precipitation, followed by three steps of column chromatography (gel-filtration, anion-exchange, and dye-affinity). The purified enzyme is a monomer with a molecular weight of 28,000 Da. The maximal azoreductase activity was observed at pH 7.0 and at 35 degrees C. This activity was NADH dependent. The K(m) values for both NADH and MR were 58.9 and 29.4 microM, respectively. The maximal velocity (V(max)) was 9.2 micromol of NADH min(-1)mg(-1). The purified enzyme is inhibited by several metal ions including Fe(2+) and Cd(2+).