Efficient production of a functional mouse/human chimeric Fab′ against human urokinase-type plasminogen activator by Bacillus brevis

Expression/secretion vectors for the production of Fab′ and single-chain (sc) Fab′ by Bacillus brevis have been constructed. For the production of Fab′, the cDNAs encoding the L chain and Fd′ fragment (Fd with the hinge region) of a mouse-human chimeric Fab′ against human urokinase-type plasminogen activator were fused directly with the translation-start and signal-peptide-encoding regions of the mwp gene, the gene for one of the major cell-wall proteins of Bacillus brevis. The two fused genes were placed tandemly downstream from the promoter of the cell-wall protein gene operon (cwp) of B. brevis. For the production of scFab′, the two cDNAs were linked with a synthetic oligonucleotide encoding a flexible peptide linker of 17 or 24 amino acids, and fused with the translation start and signal-peptide-encoding regions of the mwp gene. Fab′ was efficiently produced by B. brevis, being accumulated at a level of 100 mg/l in the culture medium in a simple shake-flask culture, which is the highest level obtained so far for a gram-positive bacterium. On the other hand, the scFab′ remained at a level of a few milligrams per liter in the culture medium. The Fab′ produced by B. brevis showed comparable antigen-binding activity to that of the parental antibody. The L chain and Fd′ fragment, constituting the Fab′, had the correct N-terminal amino acid sequences. These results indicate that B. brevis is a very promising host for the production of native Ig fragments. Received: 25 April 1997 / Received revision: 3 June 1997 / Accepted: 29 June 1997     

Direct high-level secretion into the culture medium of tuna growth hormone in biologically active form byBacillus brevis

The characteristic features of theBacillus brevis system developed by us are very high productivity of heterologous proteins and very low extracellular proteinase activity. However, the production level of eucaryotic proteins with this system was generally one or two orders of magnitude lower than that of bacterial proteins. Therefore, we have explored methods for increasing the production efficiency as to animal proteins. Signal peptide modification was found to be very effective for high-level secretion of tuna growth hormone (tGH). Modification of the signal peptide with higher basicity in the amino terminal region and higher hydrophobicity in the middle region brought about a ten-fold increase in tGH production. Further elevation of the tGH yield to 240 mg/l was achieved by using a low proteinase mutant and a stable plasmid, and by culturingB. brevis under optimal conditions with the addition of some chemicals. Thus, biologically active tGH can be efficiently produced directly in the medium with thisB. brevis system.     

Propeptide of Bacillus subtilis amylase enhances extracellular production of human interferon-α in Bacillus subtilis

The Gram-positive bacterium, Bacillus subtilis and related species are widely used industrially as hosts for producing enzymes. These species possess a high potential to produce secreted proteins into the culture medium. Nevertheless, the secretion of heterologous proteins by these species is frequently inefficient. In this study, the human interferon-α2b (hIFN-α2b) was used as a heterologous model protein, to investigate the effect of B. subtilis AmyE propeptide in enhancing the secretion of heterologous proteins in B. subtilis. We found that the secretion production and activity of hIFN-α2b with AmyE propeptide increased by more than threefold, compared to that without AmyE propeptide. The maximum amount of secreted hIFN-α2b with propeptide was 14.8 ± 0.6 μg ml⁻¹. In addition, the pro-hIFN-α2b bioactivity reached 5.4 ± 0.5 × 10⁷ U mg⁻¹, which is roughly the same level as that of the non-propeptide hIFN-α2b. These results indicated that AmyE propeptide enhanced the secretion of the hIFN-α2b protein from B. subtilis. This study provides a useful method to enhance the extracellular production of heterologous proteins in B. subtilis.     

Hollow-fibre bioreactors compared to batch and chemostat culture for the production of a recombinant toxoid by a marine Vibrio

Bioreactor selection is important for maximising the productivity of recombinant organisms. In this paper a comparison is made between growth and recombinant protein synthesis in three types of bioreactor containing a marine Vibrio capable of heterologous expression and secretion of the non-toxic B-subunit pentamer of Escherichia coli heat-labile enterotoxin, EtxB. The heterologous gene was located on the plasmid pMMB68. Resistance to carbenicillin was used to select for plasmid-containing cells. In batch and continuous culture, volumetric productivities were highest when cells were grown in the presence of carbenicillin. Without antibiotic selection, the highest volumetric productivity (9.4 mg EtxB⁻¹ h⁻¹) was observed in hollow-fibre bioreactors, and the production phase could be maintained for over 50 h. The highest specific productivity under these conditions was found in batch culture, but the maximal production phase was only of 5 h duration. In hollow-fibre reactors the type of fibre used significantly affected productivity, both with regards to the maintenance of reactor integrity and by allowing passage of the recombinant toxoid through the selectively permeable membrane. Where contamination of the product with carbenicillin is to be avoided, these bioreactors are superior to batch or continuous culture. Received: 29 January 1997 / Received revision: 9 April 1997 / Accepted: 13 April 1997     

Secretion of Human Interleukin-2 in Biologically Active Form by Bacillus brevis Directly into Cultute Medium

We constructed an efficient system for synthesis and secretion of human interleukin-2 (IL-2) by Bacillus brevis. The secretion vector we constructed had strong promoters and contained the region coding for the signal peptide of the gene for B. brevis 47 cell-wall protein, followed directly by the gene encoding mature IL-2. Modification of the signal peptide and use of a protease-deficient mutant of B. brevis HPD31 increased productivity. When the signal peptide was more basic near its amino terminal and more hydrophobic in the middle region, IL-2 production increased 20 fold. Production by the mutant harboring the secretion vector was four fold that of the parent harboring the same plasmid. The yield of IL-2 increased further to 0.12 g/liter, when cultural conditions were made optimal, such by the addition of Tween 40 to the medium. The IL-2 produced by B. brevis had the same biological activity as authentic IL-2. Biologically active human IL-2 was produced efficiently and secreted directly into the medium by B. brevis.     

Influence of cell immobilization on the production of benzaldehyde and benzyl alcohol by the white-rot fungi Bjerkandera adusta, Ischnoderma benzoinum and Dichomitus squalens

Three white-rot basidiomycetes, Bjerkandera adusta, Ischnoderma benzoinum and Dichomitus squalens, were cultivated on a liquid medium supplemented with l-phenylalanine, a precursor for benzaldehyde (bitter almond aroma) and benzyl alcohol. Remarkable amounts of benzaldehyde (587 mg l⁻¹) were found in cultures of B. adusta. Immobilization of this fungus on polyurethane foam cubes allowed an 8.3-fold increase of the production of benzaldehyde and a 15-fold increase of the productivity as compared with non-immobilized cells. Aryl-alcohol oxidase activity was only detected in B. adusta. This activity was also significantly enhanced in immobilized cells, suggesting that it plays an important role in benzaldehyde biosynthesis. Conversely, consistent amounts of benzyl alcohol (340 mg l⁻¹ for B. adusta and I. benzoinum and 100 mg l⁻¹ for D. squalens) were produced by the three fungi when immobilized. Laccase activity was found only in the strains I. benzoinum and D. squalens. This activity was markedly enhanced in free cells cultures. Immobilization of the fungi did not promote benzyl alcohol production by comparison with free cell cultures (500 mg l⁻¹). Received: 10 December 1996 / Received revision: 17 February 1997 / Accepted: 22 February 1997     

Optimization of compactin fermentation

A compactin producer Penicillium sp strain was isolated from soil in our screening program. The compactin-biosynthesising capacity of the strain was improved from 5 μg ml⁻¹ to 250 μg ml⁻¹ by mutation-selection method. We investigated the effect of the medium composition on compactin productivity. A central, orthogonal three-factor experimental design by Box and Wilson was used in the investigation. The results were analysed by non-linear regression analysis. The composition of the production medium was optimized according to the calculated mathematical model using the steepest ascent method. The compactin productivity was increased to 400 μg ml⁻¹ by applying this method. Received 08 October 1997/ Accepted in revised form 04 December 1997     

Growth-associated production of poly(hydroxybutyric acid) by Azotobacter beijerinckii from organic nitrogen substrates

Poly(hydroxybutyric acid) (PHB) was produced by a selectant of Azotobacter beijerinckii in media containing only organic nitrogen sources such as N substrates. The chosen compounds were casein peptone, yeast extract, casamino acids and urea, each combined with carbon substrates glucose or sucrose. The PHB was synthesized under growth-associated conditions. The concentrations amounted to more than 50% of cell dry mass on casein peptone/glucose as well as urea/glucose medium within 45 h fermentation time. Corresponding to these yields, productivities of about 0.8 g PHB l⁻¹ h⁻¹ were discovered. The highest values increased to 1.06 g PHB l⁻¹ h⁻¹ on casein peptone/glucose medium and 1.1 g PHB l⁻¹ h⁻¹ on yeast extract/glucose medium after a period of 20 h. It was found that oxygen limitation was essential for successful product formation, as demonstrated earlier. These data from basic research may support further investigations into the use of technical proteins from renewable sources as substrates for PHB production by a strain of A. beijerinckii. Received: 3 June 1997 / Received revision: 29 August 1997 / Accepted: 15 September 1997     

Growth-associated synthesis of recombinant human glucagon and human growth hormone in high-cell-density cultures of Escherichia coli

Synthesis of two recombinant proteins (human glucagon and human growth hormone) was investigated in fed-batch cultures at high cell concentrations of recombinant Escherichia coli. The glucose-limited growth was achieved without accumulation of metabolic by-products and hence the cellular environment is presumed invariable during growth and recombinant protein synthesis. Via exponential feeding in the two-phase fed-batch operation, the specific cell growth rate was successfully controlled at the desired rates and the fed-batch mode employed is considered appropriate for examining the correlation between the specific growth rate and the efficiency of recombinant product formation in the recombinant E. coli strains. The two recombinant proteins were expressed as fusion proteins and the concentration in the culture broth was increased to 15 g fusion growth hormone l⁻¹ and 7 g fusion glucagon l⁻¹. The fusion growth hormone was initially expressed as soluble protein but seemed to be gradually aggregated into inclusion bodies as the expression level increased, whereas the synthesized fusion glucagon existed as a cytoplasmic soluble protein during the whole induction period. The stressful conditions of cultivation employed (i.e. high-cell-density cultivation at low growth rate) may induce the increased production of various host-derived chaperones and thereby enhance the folding efficiency of synthesized heterologous proteins. The synthesis of the recombinant fusion proteins was strongly growth-dependent and more efficient at a higher specific growth rate. The mechanism linking specific growth rate with recombinant protein productivity is likely to be related to the change in cellular ribosomal content. Received: 27 May 1997 / Received last revision: 31 October 1997 / Accepted: 21 November 1997     

An autoselection system in recombinant Kluyveromyces lactis enhances cloned gene stability and provides freedom in medium selection

An autoselection system for increasing plasmid stability in Kluyveromyces lactis, based on the blockage of the pyrimidine de novo and salvage pathways, was investigated. In a manner analogous to that used in Saccharomyces cerevisiae, a putative “fur1” mutation was selected in a uraA K. lactis strain using 5-fluorouracil and 5-fluorocytosine plates. Survival of the mutant required expression of a plasmid-borne URA3 gene regardless of the culture medium employed, verifying the efficacy of this autoselection system in K. lactis. The expression of heterologous invertase, encoded by the S. cerevisiae SUC2 gene, was studied during long-term sequential batch cultures (70 generations) in complex yeast/peptone/glucose medium. The fur1 mutant successfully retained the plasmid; invertase specific activity remained above 90% of the initial level. Furthermore, no mutation reversion was observed. In contrast, for the control non-fur1 strain, only 4% of the cells retained the plasmid after 70 generations, and invertase specific activity dropped to less than 10% of the initial level. Experiments comparing growth and activity in different media indicated the potential for improving productivity through medium enrichment using this autoselection system. Received: 1 April 1997 / Received revision: 16 August 1997 / Accepted: 11 September 1997     

Efficient secretion of Trichoderma reesei cellobiohydrolase II in Schizosaccharomyces pombe and characterization of its products

A cbh2 cDNA encoding Trichoderma reesei QM9414 cellobiohydrolase II, located on the expression vector whose copy number is controlled by the level of gentamicin, was successfully expressed under the control of a human cytomegalovirus promoter in the fission yeast, Schizosaccharomyces pombe. The 24-amino-acid leader peptide of the cbh2 gene was recognized by the yeast, enabling the efficient secretion of the heterologous cellobiohydrolase. The transformed S. pombe strain produced over 115 μg cellobiohydrolase proteins/ml rich medium supplemented with malt extract and 100 μg/ml gentamicin. The molecular masses of the recombinant cellobiohydrolases, secreted as two molecular species, were estimated to be 70 kDa and 72 kDa by sodium dodecyl sulfate/polyacrylamide gel electrophoresis (SDS-PAGE). Deglycosylation treatments revealed that the recombinant enzymes were overglycosylated and scarcely susceptible to α-mannosidase. The recombinant enzymes showed no carboxymethylcellulase activity, but showed similar characteristics to those of a native enzyme purified from T. reesei in their optimum pH and temperature, pH and temperature stabilities, and V _max values toward phosphoric-acid-swollen cellulose as substrate, except that their K _m values were about fourfold higher than that of the native enzyme. Received: 4 August 1997 / Received revision: 13 October 1997 / Accepted: 31 October 1997     

Determination of the kinetic parameters during continuous cultivation of the lipase-producing thermophile Bacillus sp. IHI-91 on olive oil

A thermostable lipase was produced in continuous cultivation of a newly isolated thermophilic Bacillus sp. strain IHI-91 growing optimally at 65 °C. Lipase activity decreased with increasing dilution rate while lipase productivity showed a maximum of 340 U l⁻¹ h⁻¹ at a dilution rate of 0.4 h⁻¹. Lipase productivity was increased by 50% compared to data from batch fermentations. Up to 70% of the total lipase activity measured was associated to cells and by-products or residual substrate. Kinetic and stoichiometric parameters for the utilisation of olive oil were determined. The maximal biomass output method led to a saturation constant K _S of 0.88 g/l. Both batch growth data and a washout experiment yielded a maximal specific growth rate, μ_max, of 1.0 h⁻¹. Oxygen uptake rates of up to 2.9 g l⁻¹h⁻¹ were calculated and the yield coefficient, Y _X/O, was determined to be 0.29 g dry cell weight/g O₂. From an overall material balance the yield coefficient, Y _X/S, was estimated to be 0.60 g dry cell weight/g olive oil. Received: 8 January 1997 / Received revision: 30 April 1997 / Accepted: 4 May 1997     

Expression of Human Growth Hormone by the Eukaryotic Alga, Chlorella

A method to use Chlorella to express a recombinant heterologous protein that can be recovered from the extracellular medium has been developed. Plasmids are constructed with an extracellular secretion signal sequence inserted between a promoter region and a gene for human growth hormone (hGH). The plasmids also contain a Kan^r region which confers resistance to the antibiotic G418. Protoplasts are prepared by enzymatic treatment, and the plasmid is introduced by incubation of the protoplasts with polyethylene glycol and dimethyl sulfoxide. Cells are then grown in the presence of G418, and the medium is collected from 6 days after transfection. hGH is measured by immunoassay, and values for expressed hGH of about 200–600 ng/ml are obtained. Received: 5 November 1998 / Accepted: 25 January 1999     

Analysis of the exopolysaccharides produced by Lactobacillus delbrueckii subsp. bulgaricus NCFB 2772 grown in continuous culture on glucose and fructose

The exopolysaccharides produced by Lactobacillus delbrueckii subsp. bulgaricus NCFB 2772 grown in defined medium were investigated. At equal cell densities, the strain produced 95 mg l⁻¹ exopolysaccharides with glucose and 30 mg l⁻¹ with fructose as the carbohydrate source. High-performance size-exclusion chromatography of the exopolysaccharides produced on glucose showed the presence of two fractions with relative molecular masses (M _r) of 1.7 × 10⁶ and 4 × 10⁴ in almost equal amounts. The exopolysaccharides produced on fructose contained mainly a fraction of low M _r of 4 × 10⁴. The high-M _r fraction of the purified exopolysaccharides produced on glucose appeared to have a sugar composition of galactose, glucose and rhamnose in the molar ratio of 5:1:1, whereas the low-M _r weight fraction contained galactose, glucose and rhamnose in the molar ratio of approximately 11:1:0.4. The purified exopolysaccharide fractions produced on fructose showed comparable ratios. The high-molecular-mass fractions contained terminally linked galactose, 1,2,3-linked galactose, 1,3,4-linked galactose, 1,3-linked glucose and terminally linked rhamnose. The low-molecular-mass fractions contained mainly 1,3-linked galactose and 1,6-linked galactose and lower amounts of other sugar linkages. The production of the high-M _r fractions appeared to be dependent on the carbohydrate source, whereas the low-M _r fractions were produced more continuously. Received: 30 April 1997 / Received revision: 11 June 1997 / Accepted: 14 June 1997     

Repeated batch cultivation of the microalga Spirulina platensis

Summary The cultivation of photosynthetic microorganisms such as the microalga Spirulina platensis can provide an alternative source of food. The water in Mangueira Lagoon (Rio Grande do Sul state, southern Brazil) has several required nutrients for the growth of Spirulina and could be added to culture medium to reduce the cost of producing S. platensis. Although little studied, repeated batch cultivation is a very useful technique because it has a better cost–benefit ratio than other cultivation methods. In a series of runs, we studied the influence of cell concentration, renewal rate and strain on the specific growth rate and biomass productivity of S. platensis during repeated batch cultivation, the runs taking place in 2-l Erlenmeyer flasks for 2160 h at 30 °C and a light intensity of 2500 lux under a 12 h photoperiod. The three factors studied had a significant (P < 0.05) effect on the results (specific growth rate and productivity). Using Zarrouk’s medium, the highest specific growth rate (μ_X) was 0.111 day⁻¹ while the biomass productivity (P _X) was 0.0423 g l⁻¹ day⁻¹, while Mangueira Lagoon water supplemented with 10% Zarrouk’s medium gave μ_X = 0.113 day⁻¹ and a productivity P _X = 0.0467 g l⁻¹ day⁻¹. These values were two to three times higher than the results obtained in batch cultivation, indicating that the repeated batch cultivation of S. platensis is attractive and convenient.     

Pullulan production from deproteinized whey by Aureobasidium pullulans

Aureobasidium pullulans P56 was investigated using an adaptation technique and a mixed culture system. The adaptation of A. pullulans and the mixed cultures of A. pullulans and/or Lactobacillus brevisX20, Debaryomyces hansenii 194 and Aspergillus niger did not increase the production of polysaccharide. Enzymic hydrolysis of lactose in deproteinized whey gave a higher polysaccharide concentration and polysaccharide yield than acidic hydrolysed lactose. Maximum polysaccharide concentration (11.0 ± 0.5 g L⁻¹), biomass dry weight (10.5 ± 0.4 g L⁻¹), polysaccharide yield (47.2 ± 1.8%) and sugar utilization (93.2 ± 2.8%) were achieved using enzyme-hydrolysed whey (pH 6.5) containing 25 g L⁻¹ lactose and supplemented with K₂HPO₄ 0.5%, L-glutamic acid 1%, olive oil 2.5%, and Tween 80 0.5%. In this case the pullulan content of the crude polysaccharide was 40%. Received 16 December 1997/ Accepted in revised form 12 March 1999     

Production of 1,3-propanediol by Clostridium butyricum in continuous culture with cell recycling

The continuous fermentation of 1,3-propanediol from glycerol by Clostridium butyricum was subjected to cell recycling by filtration using hollow-fibre modules made from polysulphone. The performance of the culture system was checked at a retention ratio (dilution rate/bleed rate) of 5, dilution rates between 0.2 h⁻¹ and 1.0 h⁻¹ and glycerol input concentrations of 32 g l⁻¹ and 56 g l⁻¹. The near-to-optimum propanediol concentration of 26.5 g l⁻¹ (for 56 g l⁻¹ glycerol) was maintained up to a dilution rate of 0.5 h⁻¹ and then decreased while the propanediol productivity was highest at 0.7 h⁻¹. The productivity could be increased by a factor of four in comparison to the continuous culture without cell recycling. By application of the model of Zeng and Deckwer [(1995) Biotechnol Prog 11: 71–79] for cultures under substrate excess, it was shown that the limitations resulted exclusively from product inhibition and detrimental influences from the cell recycling system, such as shear stress, were not involved. Received: 20 October 1997 / Received revision: 12 December 1997 / Accepted: 14 December 1997     

Induction of submerged conidiation of the biocontrol agent Penicillium oxalicum

Induction of submerged conidiation of Penicillium oxalicum has been examined using a range of synthetic and complex media and complex media supplemented with by-products of the brewing industry. Only one method (Morton's method), consisting of growth in a glucose/salts-based medium (C:N ratio 62.5, medium A) for 24 h and then transference to the same medium without a nitrogen source (medium B), induced conidiation. Levels of sporulation were significantly (P = 0.05) increased by addition of calcium or poly(ethylene glycol) 6000 to medium B. The optimum age for transference of the mycelium was 24 h and the optimum pH was 6. Calcium was an induction factor when added to medium A (C:N ratio 62.5) of Morton's method. It was concluded that nitrogen depletion and calcium addition to a medium with high C:N ratio are the factors inducing conidiation of P. oxalicum. Maximum levels of conidiation (35 × 10⁶ spores ml⁻¹) were obtained when the nitrogen level in medium A of Morton's method was further reduced (C:N ratio 142.9) and calcium (20 mM) was added. These results are the essential starting point to investigate liquid fermentation systems for the biocontrol agent P. oxalicum. Received: 19 November 1996 / Received revision: 25 March 1997 / Accepted: 27 March 1997     

Construction of a food-grade multiple-copy integration system for Lactococcus lactis

A food-grade vector system was developed that allows stable integration of multiple plasmid copies in the chromosome of Lactococcus lactis. The vector consists of the plus origin of replication (Ori⁺) of the lactococcal plasmid pWV01, the sucrose genes of the lactic acid bacterium Pediococcus pentosaceus PPE1.0 as selectable marker, a multiple-cloning site, and a lactococcal DNA fragment of a well-characterized chromosomal region. The system includes two L. lactis strains, LL108 and LL302, which produce the pWV01 RepA protein essential for replication of the Ori⁺ vectors. These helper strains allow the construction and isolation of the replicating form of the integration plasmids from a homologous background. Single-cross-over integration of the plasmids in L. lactis MG1363 resulted in amplifications to a level of approximately 20 copies/chromosome after selection of the transformants on medium containing sucrose as the only fermentable sugar. The amplifications were stable under selective growth conditions. In glucose-containing medium a limited loss of integrated plasmid copies was detected at a rate of (7.5–15) × 10⁻² copies per generation. One strain, MG124, was isolated that had retained 11 integrated copies after a period of 120 generations of non-selective growth. These results show that the single-cross-over integration system described here represents a simple procedure for the engineering of stable food-grade strains carrying multiple copies of a gene of interest. Received: 23 September 1997 / Received revision: 21 November 1997 / Accepted: 21 November 1997     

The adverse effect of nitrogen limitation and excess-cellobiose on Fibrobacter succinogenes S85

Fibrobacter succinogenes S85 cultures that were cellobiose-limited converted cellobiose to succinate and acetate, produced little glucose or cellotriose, maintained an intracellular ATP concentration of 4.1 mM and a membrane potential of 140 mV for 24 h, did not lyse at a rapid rate once they had reached stationary phase, and had a most probable number of viable cells that was greater than 10⁶/ml. When the cellobiose concentration was increased 6-fold (5 mM to 30 mM), ammonia was depleted and the cultures left 10 mM cellobiose. Cultures provided with excess cellobiose produced succinate and acetate while they were growing, but there was little increase in fermentation acids after the ammonia was depleted and growth ceased. The stationary-phase, cellobiose-excess cultures had a lysis rate that was 7-fold faster than that of the cellobiose-limited cultures, and the most probable number was only 3.3 × 10³ cells/ml. The stationary-phase, cellobiose-excess cultures had 2.5 times as much cellular polysaccharide as the cellobiose-limited cultures, but the intracellular ATP and membrane potential were very low (0.1 mM and 40 mV respectively). Methylglyoxal, a potentially toxic end-product of carbohydrate fermentation, could not be detected, and fresh inocula grew rapidly in spent medium that was supplemented with additional ammonia. Stationary-phase, cellobiose-excess cultures converted cellobiose to glucose and cellotriose, but the apparent K _m of cellotriose formation was 15-fold lower than the K _m of glucose production (0.7 mM compared to 10 mM). Received: 26 June 1997 / Received revision: 12 August 1997 / Accepted: 29 August 1997