Efficient separation of solids from fermentation broth in bacterial α-amylase production

Various coagulating-flocculating agents were tried in different combinations for the clarification of bacterial broth having high α-amylase enzyme activity. Best separation was achieved using a combination of calcium chloride, sodium hydroxide and sodium alginate.     

Banana waste as substrate for α-amylase production by Bacillus subtilis (CBTK 106) under solid-state fermentation

 Bacillus subtilis CBTK 106, isolated from banana wastes, produced high titres of α-amylase when banana fruit stalk was used as substrate in a solid-state fermentation system. The effects of initial moisture content, particle size, cooking time and temperature, pH, incubation temperature, additional nutrients, inoculum size and incubation period on the production of α-amylase were characterised. A maximum yield of 5 345 000 U mg^-1 min^-1 was recorded when pretreated banana fruit stalk (autoclaved at 121 °C for 60 min) was used as substrate with 70% initial moisture content, 400 μm particle size, an initial pH of 7.0, a temperature of 35 °C, and additional nutrients (ammonium sulphate/sodium nitrate at 1.0%, beef extract/peptone at 0.5%, glucose/sucrose/starch/maltose at 0.1% and potassium chloride/sodium chloride at 1.0%) in the medium, with an inoculum-to-substrate ratio of 10% (v/w) for 24 h. The enzyme yield was 2.65-fold higher with banana fruit stalk medium compared to wheat bran. Received: 18 April 1995/Received last revison: 6 May 1996/Accepted: 9 May 1996     

Hyperactive α-amylase production by Aspergillus oryzae IFO 30103 in a new bioreactor

Aims: To improve the α‐amylase production in solid‐state fermentation (SSF) condition utilizing a new bioreactor (NB) system. Methods and Results: In NB system, 20 g of wheat bran moistened with liquid medium in 1 : 1 ratio (w/v) was taken on the tray present inside the upper vessel and an additional 80 ml medium was supplemented into the lower vessel. Oxygen uptake rate was improved by supplying compressed air that lifted the liquid medium into the upper vessel and touched the substrate bed. This condition probably facilitated the heat transfer to liquid medium, reduce water loss and catabolite repression. With 1% glucose supplementation, maximum α‐amylase activity of 22 317 Ugds^?1 was produced by Aspergillus oryzae IFO 30103 within a very short incubation period (48 h) at 2‐cm bed height with air flow rate of 0·1 l min^?1 g^?1 wheat bran at 32°C and initial medium pH of 6. Conclusions: Within a short incubation period, significantly high α‐amylase activity was obtained and it is higher than those reported to date at bioreactor scale operating with a fungal strain. Significance and Impact of the Study: The reactor is novel and can overcome some of the major problems associated with SSF process. A. oryzae IFO 30103 is reported as the best fungal source for α‐amylase production.     

Comparative profiles of α-amylase production in conventional tray reactor and GROWTEK bioreactor

GROWTEK bioreactor was used as modified solid-state fermentor to circumvent many of the problems associated with the conventional tray reactors for solid-state fermentation (SSF). Aspergillus oryzae IFO-30103 produced very high levels of α-amylase by modified solid-state fermentation (mSSF) compared to SSF carried out in enamel coated metallic trays utilizing wheat bran as substrate. High α-amylase yield of 15,833 U g⁻¹ dry solid in mSSF were obtained when the fungus were cultivated at an initial pH of 6.0 at 32°C for 54 h whereas α-amylase production in SSF reached its maxima (12,899 U g⁻¹ dry solid ) at 30°C after 66 h of incubation. With the supplementation of 1% NaNO₃, the maximum activity obtained was 19,665 U g⁻¹ dry solid (24% higher than control) in mSSF, whereas, in SSF maximum activity was 15,480 U g⁻¹ dry solid in presence of 0.1% Triton X-100 (20% higher than the control).     

Bioprocess exploration for thermostable α-amylase production of a deep-sea thermophile Geobacillus sp. in high-temperature bioreactor

Geobacillus sp. 4j, a deep-sea high-salt thermophile, was found to produce thermostable α-amylase. In this work, culture medium and conditions were first optimized to enhance the production of thermostable α-amylase by statistical methodologies. The resulting extracellular production was increased by five times and reached 6.40?U/ml. Then, a high-temperature batch culture of the thermophile in a 15?l in-house-designed bioreactor was studied. The results showed that a relatively high dissolved oxygen (600?rpm and 15?l/min) and culture temperature of 60°C facilitated both cell growth and α-amylase production. Thus, an efficient fermentation process was established with initial medium of pH 6.0, culture temperature of 60°C, and dissolved oxygen above 20%. It gave an α-amylase production of 79?U/ml and productivity of 19804?U/l·hr, which were 10.8 and 208 times higher than those in shake flask, respectively. This work is useful for deep-sea high-salt thermophile culture, where efforts are lacking presently.     

Stability during fermentation of a recombinant α-amylase plasmid in Bacillus subtilis

Summary We have studied the stability during fermentation of a hybrid plasmid carrying a Bacillus -amylase gene in Bacillus subtilis. In the absence of antibiotic selection plasmid loss was associated largely with the post-exponential phases of growth and decline. In fermentations containing selective antibiotics, various deleted plasmids were recovered during late stationary phase, regardless of whether the host was rec ⁺ or recE. We therefore propose that the plasmid loss observed during late growth in antibiotic-free fermentations is due to deletion events which include the origin of plasmid replication. The structure of the deleted plasmids was determined and the sequences in the vicinity of the end-points analysed. When the deleted plasmids were subjected to further fermentations in the absence of selective antibiotics, they were completely stable.     

Continuous production of α-amylase byBacillus amyloliquefaciens in a two-stage fermentor

Summary The production of a secondary metabolite (-amylase) by a highly aerobic bacterium (Bacillus amyloliquefaciens) was examined in batch, single-stage chemostat, two-stage stirred tank, and two-stage stirred tank/tubular reactor configurations. The relative performance of these reactor systems as measured by product concentration and volumetric productivity was compared, and the effect of aeration rate on the extent of plug flow in the tubular reactor was examined.     

Solid state fermentation for production of α-amylase byBacillus megaterium 16M

Summary The ratio of buffer to wheat bran, incubation temperature and initial pH influence -amylase production byBacillus megaterium 16M under solid state fermentation. The enzyme, with pH and temperature optima at 6.0 and 70°C, is formed at a level of 30,000 units/g dry bacterial bran without coproduction of proteases and cellulases.     

Phosphate effects in the fermentation of α-amylase by Bacillus amyloliquefaciens

Summary The effects of phosphate on -amylase fermentation byBacillus amyloliquefaciens were investigated. It was observed through batch culture that optimal phosphate level which maximizes -amylase biosynthesis exists. High concentration of phosphate level promotes maltose uptake and growth of the microorganism, while high maltose uptake rate in the microorganism at the same time represses the enzyme biosynthesis presumably due to catabolite repression inside the microorganism. In continuous cultivation, a steady state of -amylase biosynthesis was obtained by maintaining phosphate level at a certain level. In fed-batch culture, by intermittant feeding of phosphate as well as maltose, higher activity of -amylase in the broth was obtained compared to the result from single nutrient feeding.     

Selective growth of a mutant in continuous culture of Bacillus caldolyticus for production of α-amylase

Summary In a continuous culture of Bacillus caldolyticus strain SP, which requires maltose as an inducer for production of -amylase in batch culture, a predominant mutant strain M1 which produced high amounts of -amylase in the absence of maltose in batch culture, developed. The change of cell population from strain SP to strain M1 in maltose-casitone medium was linear with time in the transient state after the change from batch to continuous culture at a dilution rate of 0.17 h^-1, and was completed in about 11 generations of bacterial growth. The dilution rate effect of continuous culture on -amylase activity was almost the same with both strains SP and M1. The maximum -amylase activity of 380 units/ml was observed at an intermediate dilution rate that was 11.5 times higher than -amylase activity at the end of a batch culture using the same medium. It was deduced that the enhancement of -amylase production in continuous culture was attributed partly to the predominant growth of a mutant strain with higher -amylase productivity.     

Efficient production of human α-amylase by a Bacillus brevis mutant

Summary A cDNA for mature human salivary -amylase was directly joined to a sequence encoding the signal peptide of the middle wall protein (MWP) gene of Bacillus brevis 47. This hybrid gene was placed downstream from the multiple promoter region of the MWP gene on a low copy-number plasmid vector, pHW1. B. brevis 47 carrying the plasmid produced 0.9 mg/l of active human -amylase in the medium. A B. brevis 47 mutant obtained on mutagenesis with N-methyl-N-nitro-N-nitrosoguanidine produced an increased amount of the -amylase (6 mg/l). When the fused gene was inserted into a high copy-number expression vector, pNU200, and then introduced into the mutant, a large amount (60 mg/l) of the -amylase was produced in the medium. The -amylase showed approximately the same specific activity and molecular weight as those of the natural enzyme. The mutant showed higher sensitivity to various antibiotics than the original strain, and altered cell wall and cytoplasmic membrane protein compositions. The results of reversion analysis suggested that a single mutation is responsible for the above phenotypes and hyper-productivity of human -amylase. Offprint requests to: H. Yamagata     

Continuous production of β-galactosidase in repeated batch culture of Penicillium multicolor with a membrane bioreactor

In crossflow filtration (CFF) of a culture broth of Penicillium multicolor, several types of membranes were tested with respect to permeate flux and the permeability of β-galactosidase, an extracellular enzyme. Membranes with surface pore sizes of 0.5 and 0.08 μm were selected because of the high flux and high β-galactosidase permeability. They were combined with a 3 × 10⁻² m³ fermentor as a system of repeated batch culture with crossflow filtration. With this system, β-galactosidase was continuously produced for 6 d and its productivity was about 3 times higher than that in fed-batch culture.     

Association of haplotype diversity in the α-amylase gene amy1 with malting quality parameters in barley

Amylases play an essential role in the germination and malting process. Therefore, these genes are interesting candidates for marker development in order to improve malting quality as an important breeding aim. The intervarietal diversity of the α-amylase gene amy1 mapping to chromosome 6H was investigated. A total of six single nucleotide polymorphisms (SNPs) were detected which defined four haplotypes. Associations between SNP-markers and important malting parameters were discovered in a collection of 117 European spring and winter barley cultivars, representing the current commercial germplasm. Haplotype amy1_H2 was significantly associated with a number of malting related traits and explained 19% of the phenotypic variation of the malting quality index (MQI) for all varieties and 35% in a subset of 72 winter barleys. The diagnostic SNP3 was associated with a 45% difference in the MQI. Within the spring barleys, the average value of haplotype amy1_H1 for friability was significantly higher than that of amy1_H4. All discovered SNPs were converted into high-throughput markers for pyrosequencing and can be used for marker assisted selection. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Ability of a solid state fermentation technique to significantly minimize catabolic repression of α-amylase production by Bacillus licheniformis M27

Summary The production of -amylase by Bacillus licheniformis M27 in submerged fermentation was completely inhibited due to catabolic repression in medium containing 1% glucose. In contrast, the enzyme production in a solid state fermentation system was 19,550 units/ml extract even when the medium contained 15% glucose. The peak in enzyme titre was, however, shifted from 48 to 72 h. The ability of the solid state fermentation system to significantly overcome catabolic repression was not known earlier and is probably conferred by various physico-chemical factors and culture conditions specific to the system. Offprint requests to: B. K. Lonsane     

N-glycosylation deficiency enhanced heterologous production of a Bacillus licheniformis thermostable α-amylase in Saccharomyces cerevisiae

Expression of foreign enzymes in yeast is a traditional genetic engineering approach; however, useful secretory enzymes are not produced in every case. The hyperthermostable α-amylase encoded by the AmyL gene of Bacillus licheniformis was expressed in Saccharomyces cerevisiae; however, it was only weakly produced and was degraded by the proteasome. To determine the cause of low α-amylase production, AmyL was expressed in a panel of yeast mutants harboring knockouts in non-essential genes. Elevated AmyL production was observed in 44 mutants. The knockout genes were classified into six functional categories. Remarkably, all non-essential genes required for N-linked oligosaccharide synthesis and a gene encoding an oligosaccharyl transferase subunit were identified. Immunoblotting demonstrated that differently underglycosylated forms of AmyL were secreted from oligosaccharide synthesis-deficient mutants, while a fully glycosylated form was produced by wild-type yeast, suggesting that N-linked glycosylation of AmyL inhibited its secretion in yeast. Mutational analysis of six potential N-glycosylation sites in AmyL revealed that the N33Q and N309Q mutations remarkably affected AmyL production. To achieve higher AmyL production in yeast, all six N-glycosylation sites of AmyL were mutated. In wild-type yeast, production of the resulting non-glycosylated form of AmyL was threefold higher than that of the glycosylated form.     

β-Glucosidase production in agitated solid fermentation,study of its properties

Summary -Glucosidase production by Aspergillus phoenicis was studied in dynamic solid fermentation, on sugar beet pulps. The assays were conducted in agitated tank reactor which allowed for the homogenization of the medium and the regulation of essential parameters: temperature, aeration, pH and humidity.In order to compare some properties of the -glucosidase produced in both liquid and solid cultures, A. phoenicis was also grown on starch in submerged culture. The enzymes produced in solid and liquid cultures have the same optimum pH of about 4.5. -Glucosidase synthetized in solid culture is significantly more thermostable than that from liquid culture and is maximally active at 65°C compared to 60°C for enzyme from liquid culture.     

Thermal denaturation: is solid-state fermentation really a good technology for the production of enzymes?

The potential for thermal denaturation to cause enzyme losses during solid-state fermentation processes for the production of enzymes was examined, using the protease of Penicillium fellutanum as a model system. The frequency factor and activation energies for the first-order denaturation of this enzyme were determined as 3.447 x 10(59) h(-1) and 364,070 Jmol(-1), respectively. These values were incorporated into a mathematical model of enzyme deactivation, which was used to investigate the consequences of subjecting this protease to temporal temperature profiles reported in the literature for mid-height in a 34 cm high packed-bed bioreactor of 150 mm diameter. In this literature source, temperature profiles were measured for 5, 15 and 25 liters per minute of air and enzyme activities were measured as a function of time. The enzyme activity profiles predicted by the model were distributed similarly, one relative to the other, as had been found in the experimental study, with substantial amounts of denaturation being predicted when the substrate temperature exceeded 40 degrees C, which occurred at the lower two airflow rates. A mathematical model of a well-mixed bioreactor was used to explore the difficulties that would be faced at large scale. It suggests that even with airflows as high as one volume per volume per minute, up to 85% of the enzyme produced by the microorganism can be denatured by the end of the fermentation. This work highlights the extra care that must be taken in scaling up solid-state fermentation processes for the production of thermolabile products.     

Enhancement of α-amylase production by integrating and amplifying the α-amylase gene of Bacillus amyloliquefaciens in the genome of Bacillus subtilis

Summary The -amylase gene of Bacillus amyloliquefaciens was integrated into the genome of Bacillus subtilis by homologous recombination. In the first transformation step, several strains were obtained carrying the -amylase gene as two randomly located copies. These strains produced -amylase in the quantities comparable with that of the multicopy plasmid pKTH10, carrying the same -amylase gene. With the plasmid system, however, the rate of the -amylase synthesis was faster and the production phase shorter than those of the chromosomally encoded -amylase. The two chromosomal gene copies were further multiplied either by amplification using increasing antibiotic concentration as the selective pressure or by performing a second transformation step, identical to the first integration procedure. Both methods resulted in integration strains carrying up to eight -amylase gene copies per one genome and producing up to eightfold higher -amylase activity than the parental strains. Six out of seven transformants, studied in more detail, were stable after growth of 42 h even without antibiotic selection. The number of the DNA and mRNA copies of the -amylase gene was quantitavely determined by sandwich hybridization techniques, directly from culture medium.