Production of the <Emphasis Type="Italic">Aspergillus aculeatus</Emphasis> endo-1,4-β-mannanase in <Emphasis Type="Italic">A. niger</Emphasis>

The β-mannanase gene (man1) from Aspergillus aculeatus MRC11624 (Izuka) was patented for application in the coffee industry. For production of the enzyme, the gene was originally cloned and expressed in Saccharomyces cerevisiae. However the level of production was found to be economically unfeasible. Here we report a 13-fold increase in enzyme production through the successful expression of β-mannanase of Aspergillus aculeatus MRC11624 in Aspergillus niger under control of the A. niger glyceraldehyde-3-phosphate dehydrogenase promoter (gpd _P) and the A. awamori glucoamylase terminator (glaA_T). The effect of medium composition on mannanase production was evaluated, and it was found that the glucose concentration and the organic nitrogen source had an effect on both the volumetric enzyme activity and the specific enzyme activity. The highest mannanase activity levels of 16,596 nkat ml⁻¹ and 574 nkat mg⁻¹ dcw were obtained for A. niger D15[man1] when cultivated in a process-viable medium containing corn steep liquor as the organic nitrogen source and high glucose concentrations.     

Improved productivity of <Emphasis Type="Italic">β</Emphasis>-fructofuranosidase by a derepressed mutant of <Emphasis Type="Italic">Aspergillus niger</Emphasis> from conventional and non-conventional substrates

Summary Wild-type cultures of Aspergillus niger produced a basal level of β-fructofuranosidase on glucose of 1 IU l⁻¹ h⁻¹. In contrast, a catabolite-derepressed mutant strain of the same organism produced a markedly higher level (25 IU l⁻¹ h⁻¹) of this enzyme when grown on the same carbon source. Wheat bran induced both the wild type (252 IU l⁻¹ h⁻¹) and the mutant strain (516 IU l⁻¹ h⁻¹) to produce 252- to 516-fold higher levels of this enzyme than was observed with the wild-type grown on glucose and was the best carbon source. When corn steep liquor served as a nitrogen source, the wild-type organism showed a higher activity of enzyme on monosaccharides and disaccharides comparable to that produced by corncobs in the basal medium and that mutant was a potentially improved (> 2-fold) organism for the production of β-fructofuranosidase on all carbon sources. Enhanced substrate consumption and product formation kinetic parameters suggest that the mutant organism may be exploited for bulk production of this useful enzyme.     

The intra- and extracellular proteome of <Emphasis Type="Italic">Aspergillus niger</Emphasis> growing on defined medium with xylose or maltose as carbon substrate

Background  

The filamentous fungus Aspergillus niger is well-known as a producer of primary metabolites and extracellular proteins. For example, glucoamylase is the most efficiently secreted protein of Aspergillus niger, thus the homologous glucoamylase (glaA) promoter as well as the glaA signal sequence are widely used for heterologous protein production. Xylose is known to strongly repress glaA expression while maltose is a potent inducer of glaA promoter controlled genes. For a more profound understanding of A. niger physiology, a comprehensive analysis of the intra- and extracellular proteome of Aspergillus niger AB1.13 growing on defined medium with xylose or maltose as carbon substrate was carried out using 2-D gel electrophoresis/Maldi-ToF and nano-HPLC MS/MS.     

Glucoamylase production by Aspergillus niger on rice bran is improved by adding nitrogen sources

Corn steep liquor, peptone or NH _inf4 ^sup+ salts increased the yield of glucoamylase from Aspergillus niger growing in a solid-state fermentation on rice bran up to 360 IU/g dry substrate over 96 h at 30°C.The authors are with the Biotechnology Unit, Regional Research Laboratory, CSIR, Trivandrum-695 019, India;     

Influence of water activity on growth and activity of Aspergillus niger for glycoamylase production in solid-state fermentation

Growth of Aspergillus niger and glucoamylase production correlated well with the water activity of the substrate (wheat bran plus corn flour) in a solid-state fermentation. Both were maximal at an initial water activity of 0.936. Glycoamylase reached 550 units/g dry substrate after 96 h.The authors are with the Biotechnology Unit, Regional Research Laboratory, CSIR, Trivandrum-695 019, India     

Kinetics of Enhanced Substrate Consumption and Endo-β-xylanase Production by a Mutant Derivative of Humicola lanuginosa in Solid-state Fermentation

Summary Industrial byproducts namely canola meal, rice bran, sunflower meal, and wheat straw were used as substrates for endo-xylanase production by Humicola lanuginosemutant TH1 through solid substrate fermentation. The enzyme was secreted extracellularly by both wild and mutant cultures. Rice bran supported the maximum production of endo-xylanase followed by wheat straw, canola meal and sunflower meal. The highest activity was achieved after 72 h of culture and the highest yields from the above substrates were 842, 840, 610 and 608 IU per g substrate consumed respectively. The highest productivity (281 IU flask⁻¹ h⁻¹ corresponding to 5620 l⁻¹ h^-1) of endo-xylanase by the mutant of H. lanuginosa was 1.6-fold more than that produced by the parental organism in solid-state fermentation of rice bran at 45 °C. Maximum specific activity (180 IU mg⁻¹ protein) and substrate consumption rates were significantly more than those reported by previous researchers on Humicola sp. The mutant possessed markedly low accompanying cellulase activity. Thermodynamic studies revealed that the mutant required significantly lower activation energy for enzyme production and higher for thermal inactivation which signified that the endogenous metabolic machinery of mutant cells exerted more protection against thermal inactivation during product formation than that needed by its parental cultures.     

Xylanases from <Emphasis Type="Italic">Aspergillus niger,Aspergillus niveus</Emphasis> and <Emphasis Type="Italic">Aspergillus ochraceus</Emphasis> produced under solid-state fermentation and their application in cellulose pulp bleaching

This study describes the production of xylanases from Aspergillus niveus, A. niger, and A. ochraceus under solid-state fermentation using agro-industrial residues as substrates. Enzyme production was improved using a mixture of wheat bran and yeast extract or peptone. When a mixture of corncob and wheat bran was used, xylanase production from A. niger and A. ochraceus increased by 18%. All cultures were incubated at 30 °C at 70–80% relative humidity for 96 h. For biobleaching assays, 10 or 35 U of xylanase/g dry cellulose pulp were incubated at pH 5.5 for 1 or 2 h, at 55 °C. The delignification efficiency was 20%, the brightness (percentage of ISO) increased two to three points and the viscosity was maintained confirming the absence of cellulolytic activity. These results indicated that the use of xylanases could help to reduce the amount of chlorine compounds used in cellulose pulp treatment.     

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.     

Expression and secretion of barley α-amylase and A.niger glucoamylase in Saccharomyces cerevisiae

cDNAs of barley α-amylase andA. niger glucoamylase were cloned in oneE. coli-yeast shuttle plasmid resulting in the construction of expression secretion vector pMAG15. pMAG15 was transformed intoS. cerevisiae GRF18 by protoplast transformation. The barley α-amylase andA. niger glucoamylase were efficiently expressed under the control of promoter and terminator of yeast PGK gene and their own signal sequence. Over 99% of the enzyme activity expressed was secreted to the medium. The recombinant yeast strain, S.cerevisiae GRF18 (pMAG15), hydrolyzes 99% of the starch in YPS medium containing 15% starch in 47 h. The glucose produced can be used for the production of ethanol. Project supported by the Guangdong Natural Science Foundation.     

Cellulolytic enzymes on lignocellulosic substrates in solid state fermentation by <Emphasis Type="Italic">Aspergillus niger</Emphasis>

The production of cellulolytic enzymes by Aspergillus niger on lignocellulosic substrates groundnut fodder, wheat bran, rice bran and sawdust in solid state fermentation in a laboratory scale was compared. Czapek Dox liquid broth amended with cellulose (0.5%) was used to moisten lignocellulosic solid supports for cultivation of Aspergillus niger. The production of filter paperase, carboxymethyl cellulase and -glucosidase were monitored at daily intervals for 5 days. The peak production of the enzymes occurred within 3 days of incubation. Among solid supports used in the study, wheat bran was the best solid matrix followed by groundnut fodder in production of cellulolytic enzymes in solid state fermentation. Groundnut fodder supported significant production of FPase (2.09 FPU/g), CMCase (1.36 U/g) and -glucosidase activity (0.0117 U/g) in solid state fermentation. Considerable secretion of protein (5.10 mg/g) on groundnut fodder at peak time interval 1st day of incubation was recorded.     

Culture condition for production of glucoamylase from rice bran byAspergillus terreus

Summary Optimal conditions for the production of glucoamylase from rice bran usingAspergillus terreus in stationary culture were a medium containing 20 g rice bran/l, 0.3% (w/v) (NH₄)₂SO₄ and 0.2% (w/v) peptone at 30°C with an initial pH of 3.0. Enzymatic activity was maximal after 4 d. Glucose was the major reducing sugar produced by hydrolysis of starch. Carbohydrates favouring induction of glucoamylase were, in order: maltose, starch, cellobiose, lactose, glucose, fructose and galactose. Amino acids, in particular glycine, lysine, isoleucine and histidine, were vital for glucoamylase synthesis. Tween 80 and Triton X-100 enhanced the growth but suppressed glucoamylase synthesis.

---

Conditions de culture pour la production de glucoamylase à partir de son de riz parAspergillus terreus

Résumé Les conditions optimales pour la production de glucoamylase à partir de son de riz en utilisantAspergillus terreus en culture en état stationnaire, consistent en un milieu contenant 20 g de son de riz par litre, 0.3 % (poids/vol.) de (NH₄)₂ SO₄ et 0.2 % (poids/vol.) de peptone, à 30 °C avec un pH initial de 3.0. L'activité enzymatique est maximum après 4 jours. Le glucose est le principal sucre réducteur produit par hydrolyse de l'amidon. Les hydrates de carbone qui favorisent l'induction de la glucoamylase, sont, dans l'ordre: le maltose, l'amidon, la cellobiose, le lactose, le glucose, le fructose et le galactose. Les acides aminés, en particulier la glycine, la lysine, l'isoleucine et l'histidine sont vitales pour la synthèse de glucoamylase. Le tween 80 et le triton X-100 augmentent la croissance mais suppriment la synthèse de glucoamylase.

     

Bioenergetic consequences of glucoamylase production in carbon-limited chemostat cultures ofAspergillus niger

Aspergillus niger has been grown in glucose- and maltose-limited continuous cultures to determine the bioenergetic consequences of the production of the extracellular enzyme glucoamylase. Growth yields (g biomass per mol substrate) were high, indicating that growth was very efficient and protein production for biomass was not exceedingly energy consuming. It has been found that the energy costs for the production of this extracellular enzyme is very high. Depending on the efficiency of energy conservation the glucoamylase protein yield on ATP is between 1.3 and 2.6 g protein per mol ATP, which is equal or less than 10% of the theoretical maximum of 25.5. These high energy costs most probably have to be invested in the process of excretion. A comparison between an industrial over-producing strain and the wild typeAspergillus niger showed that this over-producing strain most probably is a regulatory mutant. Two regions of specific growth rates could be determined (one at specific growth rates lower and one at specific growth rates higher than 0.1 h^-1), which are characterized by differences in mycelium morphology and a significant deviation from linearity in the linear equation for substrate utilization. Analysis of the region of specific growth rates higher than 0.1 h^-1 yielded maintenance requirements of virtual zero. It has been concluded that for a good analysis of the growth behaviour of filamentour fungi the linear equation for substrate utilization is not suitable, since it contains no term for the process of differentiation.     

Glucoamylase production in batch, chemostat and fed-batch cultivations by an industrial strain of Aspergillus niger

The Aspergillus niger strain BO-1 was grown in batch, continuous (chemostat) and fed-batch cultivations in order to study the production of the extracellular enzyme glucoamylase under different growth conditions. In the pH range 2.5–6.0, the specific glucoamylase productivity and the specific growth rate of the fungus were independent of pH when grown in batch cultivations. The specific glucoamylase producivity increased linearly with the specific growth rate in the range 0–0.1 h⁻¹ and was constant in the range 0.1–0.2 h⁻¹. Maltose and maltodextrin were non-inducing carbon sources compared to glucose, and the maximum specific growth rate was 0.19 ± 0.02 h⁻¹ irrespective of whether glucose or maltose was the carbon source. In fed-batch cultivations, glucoamylase titres of up to 6.5 g l⁻¹ were obtained even though the strain contained only one copy of the glaA gene. Received: 5 May 1999 / Received revision: 7 September 1999 / Accepted: 17 September 1999     

Characteristics and applications of recombinant thermostable amylopullulanase of Geobacillus thermoleovorans secreted by Pichia pastoris

The 3′-deleted amylopullulanase gene from the extreme thermophile Geobacillus thermoleovorans (Gt-apuΔC) was expressed extracellularly in Pichia pastoris under both methanol-inducible AOX1 and constitutive GAP promoters. The expression of the gene (Gt-apuΔC) was higher under GAP promoter (36.2 U ml⁻¹, α-amylase; 33.5 U ml⁻¹, pullulanase) than that under AOX1 promoter (32.5 and 28.6 U ml⁻¹). The heavily glycosylated Gt-apuΔC from the recombinant P. pastoris displays higher substrate specificity, thermal stability and starch saccharification efficiency than that expressed in Escherichia coli. The enzyme hydrolyses maltotriose and maltotetraose unlike that expressed in E. coli. The enzyme action on wheat bran liberates maltose and glucose without detectable amount(s) of maltooligosaccharides. The sugars released from wheat bran (glucose and maltose) could be fractionated by ultrafiltration, as confirmed by TLC and HPLC analysis. This is the first report on the production of recombinant amylopullulanase extracellularly in P. pastoris.

     

Magnetite-alginate beads for purification of some starch degrading enzymes

Starch degrading enzymes, viz., β-amylase, glucoamylase, and pullulanase, were purified using magnetite-alginate beads. In each case, the enzyme activity was eluted by using 1.0 M maltose. β-Amylase (sweet potato), glucoamylase (Aspergillus niger), and pullulanase (Bacillus acidopullulyticus) from their crude preparations were purified 37-, 31-, and 49-fold with 86, 87, and 95% activity recovery, respectively. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis analysis showed single band in each case.     

Determination of the maximum product yield from glucoamylase-producing Aspergillus niger grown in the recycling fermentor

Aspergillus niger has been grown in glucose- and maltose-limited recycling cultures to determine the maximum growth yield, the maximum product yield for glucoamylase production, and the maintenance requirements at very slow specific growth rates. Using the linear equation for substrate utilization, and using the experimental data from both recycling experiments, both the maximum growth yield, Y_xsm, and the maximum product yield, Y_psm, could be determined. The values estimated were 157 g biomass per mol maltose for Y_xsm and 100 g protein per mol maltose for Y_psm. Expressed on a C₁-basis these values are 0.52 and 0.36 C-mole per C-mol for respectively Y_xsm and Y_psm. The found value for Y_psm is half the value found for alkaline serine protease production in Bacillus lichoniformis, and it can be concluded that formation of extracellular protein is more energy consuming in filamentous fungi than in prokaryotic organisms. Maintenance requirements are no significant factor during growth of Aspergillus niger, and reported maintenance requirements are most probably due to differentiation.     

Heterotrophic high-cell-density fed-batch and continuous-flow cultures of <Emphasis Type="Italic">Galdieria sulphuraria</Emphasis> and production of phycocyanin

Production of biomass and phycocyanin (PC) were investigated in highly pigmented variants of the unicellular rhodophyte Galdieria sulphuraria, which maintained high specific pigment concentrations when grown heterotrophically in darkness. The parental culture, G. sulphuraria 074G was grown on solidified growth media, and intensely coloured colonies were isolated and grown in high-cell-density fed-batch and continuous-flow cultures. These cultures contained 80–110 g L⁻¹ biomass and 1.4–2.9 g L⁻¹ PC. The volumetric PC production rates were 0.5–0.9 g L⁻¹ day⁻¹. The PC production rates were 11–21 times higher than previously reported for heterotrophic G. sulphuraria 074G grown on glucose and 20–287 times higher than found in phototrophic cultures of Spirulina platensis, the organism presently used for commercial production of PC.     

Production of Fusarium solani f. sp. pisi cutinase in Fusarium venenatum A3/5

Fusarium venenatum A3/5 was transformed using the Aspergillus niger expression plasmid, pIGF, in which the coding sequence for the F. solani f. sp. pisi cutinase gene had been inserted in frame, with a KEX2 cleavage site, with the truncated A. niger glucoamylase gene under control of the A. niger glucoamylase promoter. The transformant produced up to 21 U cutinase l⁻¹ in minimal medium containing glucose or starch as the primary carbon source. Glucoamylase (165 U l⁻¹ or 8 mg l⁻¹) was also produced. Both the transformant and the parent strain produced cutinase in medium containing cutin.     

Regulation and genetic enhancement of beta-amylase production in Clostridium thermosulfurogenes.

We studied the general mechanism for regulation of beta-amylase synthesis in Clostridium thermosulfurogenes. beta-Amylase was expressed at high levels only when the organism was grown on maltose or other carbohydrates containing maltose units. Three kinds of mutants altered in beta-amylase production were isolated by using nitrosoguanidine treatment, enrichment on 2-deoxyglucose, and selection of colonies with large clear zones on iodine-stained starch-glucose agar plates. beta-Amylase was produced only when maltose was added to cells growing on sucrose in wild-type and catabolite repression-resistant mutant strains, but the differential rate of enzyme synthesis in constitutive mutants was constant regardless of the presence of maltose. In carbon-limited chemostats of wild-type and catabolite repression-resistant mutant stains, beta-amylase was expressed on maltose but not on glucose or sucrose. beta-Amylase synthesis was immediately repressed by the addition of glucose. Therefore, we concluded that beta-amylase synthesis in C. thermosulfurogenes was inducible and subject to catabolite repression. The addition of cAMP did not eliminate the repressive effect of glucose. The mutants were generally characterized in terms of beta-amylase production, growth properties, fermentation product formation, and alterations in glucose isomerase and glucoamylase activities. A hyperproductive mutant produced eightfold more beta-amylase on starch medium than the wild type and more rapidly fermented starch to ethanol.