Genetic construction of Xanthomonas campestris and xanthan gum production from whey

Summary Plasmids pUR291 and pNZ521 containing lacZ gene, maturation protein and proteinase P genes, were transferred into X. campestris either by conjugation or by transformation. Plasmid pNZ521 was also conjugally transferred into X. campestris XMT1 a transformant carrying plasmid pUR291. All the constructed strains were evaluated for xanthan gum production in either a medium of 50% whey or the same medium supplemented with 1.5% lactose or 1.5% glucose. Mixed cultures either with transconjugants or with transformants were tested for xanthan gum production as well.     

Characterization of optimal growth conditions and carotenoid production of strain Rhodotorula mucilaginosa HP isolated from larvae of Pieris rapae

Yeasts have been studied because of their production of a pigment known as carotenoid with potential application in food and feed supplements. A carotenoid‐producing yeast was isolated from the larvae of Pieris rapae, named HP. The strain HP was identified as Rhodotorula mucilaginosa classified by its carbohydrate fermentation pattern and physiological tests. Rhodotorula mucilaginosa HP produces several exogenous enzymes: alkaline phosphatase, esterase, leucine arylamidase, valine arylamidase, acid phosphatase and β‐glucosidase. Using response surface methodology, selected medium components (yeast extract, malt extract, peptone, glucose) were tested to find the optimum conditions for carotenoid production and the growth of R. mucilaginosa HP. Central composite design was used to control the concentrations of medium components. Peptone and glucose had the largest effects on carotenoid production and cell growth of R. mucilaginosa HP, respectively. The estimated optimal growth conditions of R. mucilaginosa HP were: yeast extract 3.23%, malt extract 2.84%, peptone 6.99% and glucose 12.86%. The estimated optimal conditions for carotenoid production were: yeast extract 2.17%, malt extract 2.11%, peptone 5.79% and glucose 12.46%. These results will assist in the formulation of an appropriate culture medium for optimal carotenoid production of R. mucilaginosa HP for commercial use.     

Expression of capsule-associated genes of Cryptococcus neoformans

Cryptococcus neoformans produces an extracellular polysaccharide capsule that is related to its virulence. The production of capsular components was reported to be accelerated when cultured on media with lower amount of glucose. In this study, relationship between capsule synthesis and expression of capsule-associated genes (CAP genes) was investigated by quantitative real-time PCR analysis. Normally encapsulated strains and a stable acapsular strain were cultured in 1% polypepton medium with 0.1% or 15% glucose. The results of assessment of the capsule size showed that the capsule of yeast cells cultured in the medium with low amount of glucose was thicker than that with high amount of glucose. The CAP gene expressions of normally encapsulated strains were higher in the medium with 0.1% glucose than in the medium with 15% glucose. Furthermore, CAP10, CAP59 and CAP60 genes were expressed very low in a stable acapsular strain, and CAP64 gene was not expressed. Results of assessment of capsule size and CAP gene expressions by quantitative real-time PCR analysis indicated that CAP gene expressions might be related to the production of capsule, and that glucose concentration in culture media might be related to the expression of CAP genes.     

The capacity of orotic acid production in pyrimidinedeficient mutants ofBrevibacterium ammoniagenes

Eight uracil-dependent mutants ofBrevibacterium ammoniagenes CCEB 364 and three mutants ofCorynebacterium sp. 9366 were checked for the production of precursors of nucleic acids. Four of the strains liberated into the medium a substantial amount of orotic acid. The production of orotic acid by a mutant ofBrevibacterium ammoniagenes (1043) was examined on mineral media containing varying amounts of glucose in the presence of uracil. The optimum concentration of glucose for the production of orotic acid was found to be 5–8%. On media to which natural substrates were added the orotic acid production increased substantially. The maximum production (6.5 g orotic acid/liter) was reached in a medium containing 0.5% yeast extract and 5% glucose; addition of uracil to this medium had no effect on the production. The maximum rate of production occurred between 24 and 72 h of fermentation. After this period the concentration of orotic acid in the medium decreases.     

Expression of the <Emphasis Type="BoldItalic">Escherichia coli pntAB</Emphasis> genes encoding a membrane-bound transhydrogenase in <Emphasis Type="BoldItalic">Corynebacterium glutamicum</Emphasis> improves <Emphasis Type="SmallCaps">l</Emphasis>-lysine formation

A critical factor in the biotechnological production of l-lysine with Corynebacterium glutamicum is the sufficient supply of NADPH. The membrane-integral nicotinamide nucleotide transhydrogenase PntAB of Escherichia coli can use the electrochemical proton gradient across the cytoplasmic membrane to drive the reduction of NADP⁺ via the oxidation of NADH. As C. glutamicum does not possess such an enzyme, we expressed the E. coli pntAB genes in the genetically defined C. glutamicum lysine-producing strain DM1730, resulting in membrane-associated transhydrogenase activity of 0.7 U/mg protein. When cultivated in minimal medium with 10% (w/v) carbon source, the presence of transhydrogenase slightly reduced glucose consumption, whereas the consumption of fructose, glucose plus fructose, and, in particular, sucrose was stimulated. Biomass was increased by pntAB expression between 10 and 30% on all carbon sources tested. Most importantly, the lysine concentration was increased in the presence of transhydrogenase by ∼10% on glucose, ∼70% on fructose, ∼50% on glucose plus fructose, and even by ∼300% on sucrose. Thus, the presence of a proton-coupled transhydrogenase was shown to be an efficient way to improve lysine production by C. glutamicum. In contrast, pntAB expression had a negative effect on growth and glutamate production of C. glutamicum wild type.     

Enhancement of human granulocyte-colony stimulating factor production in recombinant E. coli using batch cultivation

Development of inexpensive and simple culture media is always favorable for recombinant protein over-expression in E. coli. The effects of medium composition on the production of recombinant human granulocyte-colony stimulating factor (rh-GCSF) were investigated in batch culture of E. coli BL21 (DE3) [pET23a-hgcsf]. First, the optimum medium for production of rh-GCSF was determined; and, then it was shown that mixture of amino acid addition at induction time, which was determined on the basis of amino acids frequency in the recombinant protein, increases recombinant protein expression level significantly. Furthermore, the effect of glucose concentration on productivity of rh-GCSF was investigated; 20 g/l of glucose will result in maximum attainable biomass and rh-GCSF in this process. At optimum conditions, a cell dry weight of 10.5 g/l, an expression level of about 35% of total cellular protein, rh-GCSF concentration of 1.75 ± 0.1 g/l, and overall rh-GCSF yield of 165 ± 5 mg/g were obtained.     

Enhanced recombinant protein production in pyruvate kinase mutant of Bacillus subtilis

Previous work demonstrated that acetate production was substantially lower in pyruvate kinase (pyk) mutant of Bacillus subtilis. The significantly lower acetate production in the pyk mutant is hypothesized to have positive effect on recombinant protein production either by lifting the inhibitory effect of acetate accumulation in the medium or redirecting the metabolic fluxes beneficial to biomass/protein synthesis. In this study, the impact of the pyk mutation on recombinant protein production was investigated. Green fluorescent protein (GFP+) was selected as a model protein and constitutively expressed in both the wild-type strain and a pyk mutant. In batch cultures, the pyk mutant produced 3-fold higher levels of recombinant protein when grown on glucose as carbon source. Experimental measurements and theoretical analysis show that the higher protein yield of the mutant is not due to removal of an acetate-associated inhibition of expression or gene dosage or protein stability but a much lower acetate production in the mutant allows for a greater fraction of carbon intake to be directed to protein synthesis.     

Development of production and purification processes of recombinant fragment of pneumococcal surface protein A in <Emphasis Type="Italic">Escherichia coli</Emphasis> using different carbon sources and chromatography sequences

Pneumococcal surface protein A (PspA) is essential for Streptococcus pneumoniae virulence and its use either as a novel pneumococcal vaccine or as carrier in a conjugate vaccine would improve the protection and the coverage of the vaccine. Within this context, the development of scalable production and purification processes of His-tagged recombinant fragment of PspA from clade 3 (rfPspA3) in Escherichia coli BL21(DE3) was proposed. Fed-batch production was performed using chemically defined medium with glucose or glycerol as carbon source. Although the use of glycerol led to lower acetate production, the concentration of cells were similar at the end of both fed-batches, reaching high cell density of E. coli (62 g dry cell weight/L), and the rfPspA3 production was higher with glucose (3.48 g/L) than with glycerol (2.97 g/L). A study of downstream process was also carried out, including cell disruption and clarification steps. Normally, the first chromatography step for purification of His-tagged proteins is metal affinity. However, the purification design using anion exchange followed by metal affinity gave better results for rfPspA3 than the opposite sequence. Performing this new design of chromatography steps, rfPspA3 was obtained with 95.5% and 75.9% purity, respectively, from glucose and glycerol culture. Finally, after cation exchange chromatography, rfPspA3 purity reached 96.5% and 90.6%, respectively, from glucose and glycerol culture, and the protein was shown to have the expected alpha-helix secondary structure.     

Factors affecting sporulation by Phomopsis phaeolorum

Light and nutrition are the important factors in the production of pycnidia and conidia by cowpea isolates of the Phomopsis state of Diaporthe phaseolorum. The highest number of pycnidia and conidia were produced on plant tissue exposed to cool-white fluorescent light. In semisynthetic media more pycnidia were formed at high glucose concentrations, but they matured more slowly than those formed at lower glucose concentrations. Both the level of conidiation and the percentage of pycnidia that formed conidia were higher at lower glucose concentrations. The best artificial medium for inducing a high number of pycnidia containing abundant conidia was one that contained 0.4% glucose and 0.4% NaNO₃. A number of carbon sources could replace glucose in this medium.     

Potential of solid state fermentation for production of L(+)-lactic acid by Rhizopus oryzae

Production of l(+)-lactic acid by Rhizopus oryzae NRRL 395 was studied in solid medium on sugar-cane bagasse impregnated with a nutrient solution containing glucose and CaCO₃. A comparative study was undertaken in submerged and solid-state cultures. The optimal concentrations in glucose were 120 g/l in liquid culture and 180 g/l in solid-state fermentation corresponding to production of l(+)-lactic acid of 93.8 and 137.0 g/l, respectively. The productivity was 1.38 g/l per hour in liquid medium and 1.43 g/l per hour in solid medium. However, the fermentation yield was about 77% whatever the medium. These figures are significant for l(+)-lactic acid production.     

Influence of pectin and glucose on growth and polygalacturonase production by Aspergillus niger in solid-state cultivation

The solid-state production of endo- and exo-polygalacturonases (PG) by Aspergillus niger was studied in a media containing wheat bran, salts, and different citric pectin and/or glucose concentrations. Kinetic analysis of the process indicated that the formation of PG and the growth of A. niger are associated processes. By increasing citric pectin from 0 to 16% (w/w), the maximum A. niger concentration (X _m) was raised from 94 to 121 mg/g dry medium suggesting that pectin can be used by A. niger as a growth substrate besides its role as an inducer. With 16% (w/w) pectin, 281 U exo-PG/gdm and 152 U endo-PG/gdm were obtained. Otherwise, pectin concentrations from 20 to 30% (w/w) hindered both production and growth. A. niger concentrations of 108–113 mg/gdm were achieved in runs with glucose from 5 to 12% (w/w), whereas at 16 and 20% (w/w) glucose, lower X _m values (ca. 100 mg/gdm) were measured. The addition of glucose to the wheat bran medium, up to 10% (w/w) led to maximum endo-PG titers slightly lower than those found in the absence of glucose. Nevertheless, exo-PG formation in these media was strongly increased and activities over 370 U/gdm were achieved. The results suggest that in experiments with pectin concentrations until 16% (w/w), exo-PG production was repressed by pectin-degradation products although these same substances had favored biomass growth. When glucose concentrations over 10% (w/w) were added to the media, the maximum activities of both enzymes decreased drastically, suggesting that glucose at high concentrations also exerts a repressive effect on PG production.     

Critical factors in chitin production by fermentation of shrimp biowaste

Factors affecting Lactobacillus fermentation of shrimp waste for chitin and protein liquor production were determined. The objective of the fermentation is medium conditioning by Lactobacillus through production of proteases and lowering of the pH. The efficiency was tested by conducting fermentation of biowaste in 1-l beakers with or without pH adjustment using different acids. Addition of 5% glucose to the biowaste supported the growth of lactic acid bacteria and led to better fermentation. Among four acids tested to control pH at the start and during fermentation, acetic acid and citric acid proved to be the most effective. In biowaste fermented with 6.7% L. plantarum inoculum, 5% glucose, and pH 6.0 adjusted with acetic acid, 75% deproteination and 86% demineralization was achieved. Replacement of acetic acid by citric acid gave 88% deproteination and 90% demineralization. The fermentation carried out in the presence of acetic acid resulted in a protein fraction that smelled good and a clean chitin fraction. Received: 4 April 2000 / Received revision: 9 June 2000 / Accepted: 9 June 2000     

Some factors affecting lipase production by yeasts and filamentous fungi

Summary The highest activity of extracellular lipases was obtained after 24 h of cultivation of R. miehei NH in the medium with 0.5% beef tallow and medium working volume of 100 ml (2302U/ug of protein). For yeast after 36h of cultivation for Y.lipolytica 2, in 50 ml medium with 0.5% beef tallow (1796 U/ug of protein). Lipases activity increased by lowering the working volume of medium and decreasing the glucose content.     

Production of Actinomycin D in Complex Media

The production of actinomycin D was examined using Streptomyces antibioticus growing on a complex medium based on glucose and casein hydrolyzate. Purification of the medium to remove calcium increased actinomycin production by about one-third and prevented production of a characteristic brown pigment. The sensitivity to magnesium concentrations was less than was reported by Katz et al.,¹¹⁾ while similar requirements were found for zinc and iron.     

Pyranose 2-oxidase (P2O): Production from Trametes versicolor in Stirred Tank Reactor andits Partial Characterization

Abstract

Optimization of pyranose-2-oxidase (P2O) production conditions from Trametes versicolor was carried out in shaking cultures containing glucose, malt, and yeast extracts; the optimum concentration values were found to be 1.5% glucose, 1.0% yeast extract, and 1.0% malt extract, pH 5.0, temperature, 26°C, and agitation rate 150 rpm. For the first time, P2O production was also carried out in a stirred tank reactor (STR) with 2.2 L working volume in the optimized medium composition, and biomass, P2O activity, protein, nitrogen and glucose concentrations were also monitored besides pH and dissolved oxygen (DO). In the STR, P2O activity peaked on day 9. Partial enzyme characterization occurred and optimum pH and temperature were detected as 7.0 and 37°C, respectively. K _m value was found to be 1.009 mM.     

Growth and β-Glucan 10C3K Production by a Mutant of Alcaligenes faecalis var. myxogenes in Defined Medium

A defined medium was developed in which Alcaligenes faecalis var. myxogenes 10C3 mutant K produced a large quantity of β-glucan 10C3K. The medium contained 4% glucose together with 0.1% citrate, succinate or fumarate as the carbon source, 0.15% (NH₄)₂HPO₄ as the nitrogen source and mineral salts. When NaNH₄HPO₄, KNO₃ or urea was used at a concentration of 0.03% nitrogen as the sole nitrogen source, salts of organic acid were not needed in addition to glucose.

In culture medium containing phosphate buffer (M/15, pH 6.5~8.0) large amounts of polysaccharide were formed and its yield from the 4% glucose added was about 50%. Thus, it was shown that polysaccharide production is enhanced greatly if a suitable pH for polysaccharide production is maintained during incubation.     

Amino acid supplementation improves heterologous protein production by Saccharomyces cerevisiae in defined medium

Supplementation of a chemically defined medium with amino acids or succinate to improve heterologous xylanase production by a prototrophic Saccharomyces cerevisiae transformant was investigated. The corresponding xylanase production during growth on ethanol in batch culture and in glucose-limited chemostat culture were quantified, as the native ADH2 promoter regulating xylanase expression was derepressed under these conditions. The addition of a balanced mixture of the preferred amino acids, Ala, Arg, Asn, Glu, Gln and Gly, improved both biomass and xylanase production, whereas several other individual amino acids inhibited biomass and/or xylanase production. Heterologous protein production by the recombinant yeast was also improved by supplementing the medium with succinate. The production of heterologous xylanase during growth on ethanol or glucose could thus be improved by supplementing metabolic precursors in the carbon- or nitrogen-metabolism.     

Solid state fermentation for L-glutamic acid production using Brevibacterium sp.

Summary Solid state fermentation system was used to cultivate Brevibacterium sp. on sugar cane bagasse impregnated with a medium containing glucose, urea, mineral salts and vitamins for producing L-glutamic acid. Maximum yields (80 mg glutamic acid per g dry bagasse with biomass and substrate - mg/gds) were obtained when bagasse of mixed particle size was moistened at 85–90 % mositure level with the medium containing 10 % glucose. This is the first report on the cultivation of Brevibacterium sp. in solid cultures for production of glutamic acid.     

Phytase production by fermentation of recombinant Pichia pastoris in monosodium glutamate wastewater

A novel method is proposed to produce both phytase and single-cell protein in recombinant Pichia pastoris fermentation using monosodium glutamate wastewater (MSGW) as the basal medium. Recombinant P. pastoris MR33 transformed with a phytase gene (AppA-m) from Escherichia coli was constructed and showed capability to utilize ammonium as the only nitrogen source. The fermentation medium was optimized in shake flasks by single-factor test and response surface methodology. A fed-batch system containing 30% MSGW, 50 g/l glucose, 1.58 g/l CaSO₄, 5.18 g/l MgSO₄ and 6.67 g/l KH₂PO₄ was developed in a 3.7-l bioreactor. The maximum phytase activity in the MSGW medium reached 3,380 U/ml, 84.2% of that in chemically defined medium, and the dry cell weight was 136 g/l. The single-cell protein (SCP; 46.66% dry cell weight) contains a variety of amino acids and is low in fat, which is ideal for utilization in animal feed. Thus, it is feasible to use MSGW medium for the production of enzymes that can be expressed in P. pastoris.