Sago starch as a low-cost carbon source for exopolysaccharide production by Lactobacillus kefiranofaciens

Low-cost sago starch was used as a carbon source for production of the exopolysaccharide kefiran by Lactobacillus kefiranofaciens. A simultaneous saccharification and fermentation process of sago starch for kefiran production was evaluated. Factors affecting the process such as an initial pH, temperature, starch concentration, including a mixture of α-amylase and glucoamylase were determined. The highest kefiran concentration of 0.85 g/l was obtained at the initial pH of 5.5, temperature of 30 °C, starch concentration of 4% and mixed-enzymes with activity of 100 U/g-starch. The use of a mixture of α-amylase and glucoamylase could enhance the productivity compared to the use of α-amylase alone. The optimal ratio of α-amylase to glucoamylase of 60:40 gave the highest kefiran production rate of 11.83 mg/l/h. This study showed that sago starch could serve as a low-cost substrate for kefiran production.     

Production of pullulanase by free and immobilized cells of <Emphasis Type="Italic">Bacillus licheniformis</Emphasis> NRC22 in batch and continuous cultures

The production of extracellular pullulanase by Bacillus licheniformis NRC22 was investigated using different fermentation modes. In batch culture maximal enzyme activity of 18 U/ml was obtained after 24 h of growth. In continuous fermentation by the free cells, maximal reactor productivity (4.15 KU/l/h) with enzyme concentration of 14.8 U/ml and specific productivity of 334.9 U/g wet cells/h was attained at a dilution rate of 0.28/h, over a period of 25 days. B. licheniformis NRC22 cells were immobilized on Ca-alginate. The immobilization conditions with respect to matrix concentration and cell load was optimized for maximal enzyme production. In repeated batch operation, the activity of the immobilized cells was stable during the 10 cycles and the activity remained between 9.8 and 7.7 U/ml. Continuous production of pullulanase by the immobilized cells was investigated in a packed–bed reactor. Maximal reactor productivity (7.0 KU/h) with enzyme concentration of 16.8 U/ml and specific productivity of 131.64 U/g wet cells/h was attained at dilution rate of 0.42/h. The enzyme activity in the effluent started to decline gradually to the level of 8.7 U/ml after 25 days of the operation.     

Optimization of ethanol,citric acid,and α-amylase production from date wastes by strains of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>, <Emphasis Type="Italic">Aspergillus niger</Emphasis>, and <Emphasis Type="Italic">Candida guilliermondii</Emphasis>

The present study deals with submerged ethanol, citric acid, and α-amylase fermentation by Saccharomyces cerevisiae SDB, Aspergillus niger ANSS-B5, and Candida guilliermondii CGL-A10, using date wastes as the basal fermentation medium. The physical and chemical parameters influencing the production of these metabolites were optimized. As for the ethanol production, the optimum yield obtained was 136.00 ± 0.66 g/l under optimum conditions of an incubation period of 72 h, inoculum content of 4% (w/v), sugars concentration of 180.0 g/l, and ammonium phosphate concentration of 1.0 g/l. Concerning citric acid production, the cumulative effect of temperature (30°C), sugars concentration of 150.0 g/l, methanol concentration of 3.0%, initial pH of 3.5, ammonium nitrate concentration of 2.5 g/l, and potassium phosphate concentration of 2.5 g/l during the fermentation process of date wastes syrup did increase the citric acid production to 98.42 ± 1.41 g/l. For the production of α-amylase, the obtained result shows that the presence of starch strongly induces the production of α-amylase with a maximum at 5.0 g/l. Among the various nitrogen sources tested, urea at 5.0 g/l gave the maximum biomass and α-amylase estimated at 5.76 ± 0.56 g/l and 2,304.19 ± 31.08 μmol/l/min, respectively after 72 h incubation at 30°C, with an initial pH of 6.0 and potassium phosphate concentration of 6.0 g/l.     

Anaerobic fermentation of gelatinized sago starch-derived sugars to acetone—1-butanol—Ethanol solvent byClostridium acetobutylicum

A study of the kinetics and performance of solvent-yielding batch fermentation of individual sugars and their mixture derived from enzymic hydrolysis of sago starch byClostridium acetobutylicum showed that the use of 30 g/L gelatinized sago starch as the sole carbon source produced 11.2 g/L total solvent,i.e. 1.5–2 times more than with pure maltose or glucose used as carbon sources. Enzymic pretreatment of gelatinized sago starch yielding maltose and glucose hydrolyzates prior to the fermentation did not improve solvent production as compared to direct fermentation of gelatinized sago starch. The solvent yield of direct gelatinized sago starch fermentation depended on the activity and stability of amylolytic enzymes produced during the fermentation. The pH optima for α-amylase and glucoamylase were found to be at 5.3 and 4.0–4.4, respectively. α-Amylase showed a broad pH stability profile, retaining more than 80% of its maximum activity at pH 3.0–8.0 after a 1-d incubation at 37°C. SinceC. acetobutylicum α-amylase has a high activity and stability at low pH, this strain can potentially be employed in a one-step direct solvent-yielding fermentation of sago starch. However, theC. acetobutylicum glucoamylase was only stable at pH 4–5, maintaining more than 90% of its maximum activity after a 1-d incubation at 37°C.     

Ethanol production from concentrated food waste hydrolysates with yeast cells immobilized on corn stalk

The aim of the present study was to examine ethanol production from concentrated food waste hydrolysates using whole cells of S. cerevisiae immobilized on corn stalks. In order to improve cell immobilization efficiency, biological modification of the carrier was carried out by cellulase hydrolysis. The results show that proper modification of the carrier with cellulase hydrolysis was suitable for cell immobilization. The mechanism proposed, cellulase hydrolysis, not only increased the immobilized cell concentration, but also disrupted the sleek surface to become rough and porous, which enhanced ethanol production. In batch fermentation with an initial reducing sugar concentration of 202.64 ± 1.86 g/l, an optimal ethanol concentration of 87.91 ± 1.98 g/l was obtained using a modified corn stalk-immobilized cell system. The ethanol concentration produced by the immobilized cells was 6.9% higher than that produced by the free cells. Ethanol production in the 14th cycle repeated batch fermentation demonstrated the enhanced stability of the immobilized yeast cells. Under continuous fermentation in an immobilized cell reactor, the maximum ethanol concentration of 84.85 g/l, and the highest ethanol yield of 0.43 g/g (of reducing sugar) were achieved at hydraulic retention time (HRT) of 3.10 h, whereas the maximum volumetric ethanol productivity of 43.54 g/l/h was observed at a HRT of 1.55 h.     

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.     

Novel strategy for yeast construction using δ-integration and cell fusion to efficiently produce ethanol from raw starch

We developed a novel strategy for constructing yeast to improve levels of amylase gene expression and the practical potential of yeast by combining δ-integration and polyploidization through cell fusion. Streptococcus bovis α-amylase and Rhizopus oryzae glucoamylase/α-agglutinin fusion protein genes were integrated into haploid yeast strains. Diploid strains were constructed from these haploid strains by mating, and then a tetraploid strain was constructed by cell fusion. The α-amylase and glucoamylase activities of the tetraploid strain were increased up to 1.5- and tenfold, respectively, compared with the parental strain. The diploid and tetraploid strains proliferated faster, yielded more cells, and fermented glucose more effectively than the haploid strain. Ethanol productivity from raw starch was improved with increased ploidy; the tetraploid strain consumed 150 g/l of raw starch and produced 70 g/l of ethanol after 72 h of fermentation. Our strategy for constructing yeasts resulted in the simultaneous overexpression of genes integrated into the genome and improvements in the practical potential of yeasts.     

Purification and Characterization of Novel α-Amylase from <Emphasis Type="Italic">Bacillus subtilis</Emphasis> KIBGE HAS

Purification of extracellular α-amylase from Bacillus subtilis KIBGE HAS was carried out by ultrafiltration, ammonium sulfate precipitation and gel filtration chromatography. The enzyme was purified to homogeneity with 96.3-fold purification with specific activity of 13011 U/mg. The molecular weight of purified α-amylase was found to be 56,000 Da by SDS-PAGE. Characteristics of extracellular α-amylase showed that the enzyme had a Km and V _max value of 2.68 mg/ml and 1773 U/ml, respectively. The optimum activity was observed at pH 7.5 in 0.1 M phosphate buffer at 50°C. The amino acid composition of the enzyme showed that the enzyme is rich in neutral/non polar amino acids and less in acidic/polar and basic amino acids. The N-terminal protein sequence of 10 residues was found to be as Ser-Ser-Asn-Lys-Leu-Thr-Thr-Ser-Trp-Gly (S-S-N-K-L-T-T-S-W-G). Furthermore, the protein was not N-terminally blocked. The sequence of α-amylase from B. subtilis KIBGE HAS was a novel sequence and showed no homology to other reported α-amylases from Bacillus strain.     

Repeated fermentation from raw starch using Saccharomyces cerevisiae displaying both glucoamylase and α-amylase

A diploid yeast strain displaying both α-amylase and glucoamylase was developed for repeated fermentation from raw starch. First, the construct of α-amylase was optimized for cell surface display, as there have been no reports of α-amylase-displaying yeast. The modified yeast displaying both glucoamylase and α-amylase produced 46.5 g/l of ethanol from 200 g/l of raw corn starch after 120 h of fermentation, and this was 1.5-fold higher when compared to native α-amylase-displaying yeast. Using the glucoamylase and modified α-amylase co-displaying diploid strain, we repeated fermentation from 100g/l of raw starch for 23 cycles without the loss of α-amylase or glucoamylase activity. The average ethanol productivity and yield during repeated fermentation were 1.61 g/l/h and 76.6% of the theoretical yield, respectively. This novel yeast may be useful for reducing the cost of bio-ethanol production and may be suitable for industrial-scale bio-ethanol production.     

Purification and characterization of highly thermostable α-amylase from thermophilic <Emphasis Type="Italic">Alicyclobacillus acidocaldarius</Emphasis>

In this study, the production of extracellular thermostable α-amylase by newly isolated thermophilic Alicyclobacillus acidocaldarius was detected on LB agar plates containing 1.0% soluble potato starch and incubated at 60°C. This extracellular α-amylase was purified to homogeneity by ammonium sulphate precipitation followed by Sephadex and ion-exchange chromatography. The α-amylase was purified to 8.138 fold homogeneity with a final recovery of 58% and a specific activity of 3,239 U/mg proteins. The purified α-amylase appeared as a single protein band on SDS-PAGE with a molecular mass of 94.5 kDa. Non-denaturing PAGE analysis showed one major band associated with enzyme activity, indicating the absence of isoenzymes. A TLC analysis showed maltose as major end product of the enzyme. The optimum assay temperature and pH for enzyme activity were 60°C and 6.0 respectively; however, the enzyme activity was stable over a wide range of pH and temperatures. The α-amylase retained its activity in the presence of the denaturing agents — SDS, Triton X-100, Tween-20, Tween-80, and was significantly inhibited by EDTA and urea. Calcium ions increased the enzyme activity, while Hg²⁺, Zn²⁺, and Co²⁺ had inhibitory effects. The K _m and V _max values were found to be 2.9 mg/mL and 7936 U/mL respectively.     

Repeated-batch production of glucoamylase using recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> immobilized in a fibrous bed bioreactor

The recombinant Saccharomyces cerevisiae strain C468/pGAC9 has an unstable hybrid plasmid pGAC9, which directs production of glucoamylase. A fibrous cotton material with a good adsorption capability for recombinant S. cerevisiae cells was used as the immobilization matrix in an internal loop airlift-driven fibrous bed bioreactor (ILALFBB) system. With batch cultures in the ILALFBB, the fraction of plasmid-carrying cells was 72% after more than 2 days cultivation, which was two times higher than that in the conventional free-cell culture. Correspondingly, a high activity of glucoamylase (GA; 113 U/l) was achieved with a high productivity of 43 U/l/h. The ILALFBB system also maintained a high fraction of viable plasmid-carrying of 74% for glucoamylase production during repeated-batch cultures, achieving a high glucoamylase activity of 140 U/l with a productivity of 19–130 U/l/h in all 14 batches studied during 19.8 days. The stable and long-term glucoamylase production from the ILALFBB was attributed to the effect of cell immobilization on plasmid stability. Plasmid-carrying cells were preferentially retained in the fibrous matrix because of their ability to adhere to the fiber surface and to form cell aggregates higher than those of plasmid-free cells. The repeated batch using immobilized cell of recombinant S. cerevisiae in the ALALFBB system thus provides a feasible method for stable, long-term and high-level production of glucoamylase.     

Ethanol production from starch by immobilized Aspergillus awamori and Saccharomyces pastorianus using cellulose carriers

A simultaneous saccharification and fermentation (SSF) process was investigated to produce ethanol using two kinds of cellulose carriers that were respectively suitable for immobilization of Aspergillus awamori and Saccharomyces pastorianus. The maximum ethanol concentration attained by the batch operation was 25.5 g l⁻¹. Under suitable conditions, both cellulose carriers with immobilized cells could be reused efficiently for three cycles. The total amount of ethanol production was 66.0 g (per 1 l working volume) after the repeated operation. Ethanol productivity mainly depends on a saccharification process. There is a limit in durability in the repeated batch operation, and it is important to maintain high activity of the fungus in order to produce ethanol efficiently. Journal of Industrial Microbiology & Biotechnology (2001) 27, 52–57. Received 11 December 2000/ Accepted in revised form 02 June 2001     

Characterization of an exo-acting intracellular α-amylase from the hyperthermophilic bacterium Thermotoga neapolitana

We cloned and expressed the gene for an intracellular α-amylase, designated AmyB, from the hyperthermophilic bacterium Thermotoga neapolitana in Escherichia coli. The putative intracellular amylolytic enzyme contained four regions that are highly conserved among glycoside hydrolase family (GH) 13 α-amylases. AmyB exhibited maximum activity at pH 6.5 and 75°C, and its thermostability was slightly enhanced by Ca²⁺. However, Ca²⁺ was not required for the activity of AmyB as EDTA had no effect on enzyme activity. AmyB hydrolyzed the typical substrates for α-amylase, including soluble starch, amylose, amylopectin, and glycogen, to liberate maltose and minor amount of glucose. The hydrolytic pattern of AmyB is most similar to those of maltogenic amylases (EC 3.2.1.133) among GH 13 α-amylases; however, it can be distinguished by its inability to hydrolyze pullulan and β-cyclodextrin. AmyB enzymatic activity was negligible when acarbose, a maltotetraose analog in which a maltose residue at the nonreducing end was replaced by acarviosine, was present, indicating that AmyB cleaves maltose units from the nonreducing end of maltooligosaccharides. These results indicate that AmyB is a new type exo-acting intracellular α-amylase possessing distinct characteristics that distinguish it from typical α-amylase and cyclodextrin-/pullulan-hydrolyzing enzymes.     

Efficient production of ethanol from raw starch by a mated diploid Saccharomyces cerevisiae with integrated α-amylase and glucoamylase genes

The goal of this research was to construct a stable and efficient process for the production of ethanol from raw starch, using a recombinant Saccharomyces cerevisiae, which is productive even under conditions such as non-selection or long-term operation. Three recombinant yeast strains were used, two haploid strains (MT8-1SS and NBRC1440SS) and one diploid strain (MN8140SS). The recombinant strains were constructed by integrating the glucoamylase gene from Rhizopus oryzae fused with the 3′-half of the α-agglutinin gene as the anchor protein, and the α-amylase gene from Streptococcus bovis, respectively, into their chromosomal DNA by homologous recombination. The diploid strain MN8140SS was constructed by mating these opposite types of integrant haploid strains in order to enhance the expression of integrated amylase genes. The diploid strain had the highest ethanol productivity and reusability during fermentation from raw starch. Moreover, the ethanol production rate of the integrant diploid strain was maintained when batch fermentation was repeated three times (0.67, 0.60, and 0.67 g/l/h in each batch). These results clearly show that a diploid strain developed by mating two integrant haploid strains is useful for the establishment of an efficient ethanol production process.     

Effect of growth rate on α-amylase production by Streptomyces sp. IMD 2679

The α-amylase of Streptomyces sp. IMD 2679 was subject to catabolite repression. Four different growth rates were achieved when the organism was grown at 40 °C and 55 °C in the presence and absence of cobalt, with an inverse relationship between α-amylase production and growth rate. Highest α-amylase yields (520 units/ml) were obtained at the lowest growth rate (0.062 h⁻¹), at 40 °C in the absence of cobalt, while at the highest growth rate (0.35 h⁻¹), at 55 °C in the presence of cobalt, α-amylase production was decreased to 150 units/ml. As growth rate increased, the rate of specific utilisation of the carbon source maltose also increased, from 46 to 123 μg maltose (mg biomass)⁻¹ h⁻¹. The pattern and levels of α-glucosidase (the enzyme degrading maltose) detected intracellularly in each case, indicate that growth rate effectively controls the rate of feeding of glucose to the cell, and thus catabolite repression. Received: 17 February 1997 / Received revision: 29 April 1997 / Accepted: 11 May 1997     

A proteinaceous thermo labile α-amylase inhibitor from Albizia lebbeck with inhibitory potential toward insect amylases

Insects feeding on stored grains cause considerable damage to harvested cereals and legumes every year. The use of α-amylase inhibitors to interfere with the pest’s digestion process has become an interesting alternative biocontrolling agent. In this study, we have studied the interactions of α-amylase inhibitors from Albizia lebbeck seeds with the amylases of coleopteran and lepidopteran insect pests. We isolated and purified the α-amylase inhibitor using acetone precipitation and gel filtration chromatography. Two prominent activity bands of α-amylase inhibitors were detected in electrophoretic analysis using 8% starch PAGE. We found that the α-amylase inhibitor, isolated as a monomer, had a molecular weight of 14.4 kDa. The α-amylase inhibitor was purified 36.15-fold with gel filtration chromatography. Its specific activity was determined at 14.4 U/mg/min. Feeding analysis of Tribolium confusum larvae on a diet containing purified α-amylase inhibitor from Albizia lebbeck revealed that survival of the larvae was severely affected, with the highest mortality rate occurring on the fifth day of feeding. We found that the isolated α-amylase inhibitor inhibits T. confusum and Helicoverpa armigera α-amylases in electrophoretic analysis as well as in solution assays. The isolated α-amylase inhibitor was found to be resistant to commercial protease as well as T. confusum and H. armigera digestive proteinases. The isolated α-amylase inhibitor was degraded by heating above 60°C. Our results suggest that A. lebbeck α-amylase inhibitor could be a useful future biocontrolling agent.     

Immobilization of Bacillus licheniformis cells, producers of thermostable α-amylase, on polymer membranes

Cells of Bacillus licheniformis 44MB82-G immobilized on different polymer membranes were used for production of thermostable α-amylase. The α-amylase yields of the membrane-immobilized cells were affected by the reactive chemical groups of the carriers and the spacer size. Formaldehyde-activated polysulphone membranes (PS-FA) were the most suitable for effective immobilization. The highest amylase yield (62% increase of the control) and operational stability (97% residual activity after 480 h repeated batch cultivation) were obtained with this system. This was confirmed by scanning electron micrographs. An additional increase of α-amylase production by PS-FA-membrane immobilized cells was achieved in a fluidized-bed reactor. Received 20 March 1997/ Accepted in revised form 08 January 1998     

β-Fructofuranosidase production by repeated batch fermentation with immobilized <Emphasis Type="Italic">Aspergillus japonicus</Emphasis>

The fungus Aspergillus japonicus ATCC 20236 was immobilized in vegetal fiber and used in repeated batch fermentations of sucrose (200 g/l) for the production of β-fructofuranosidases (FFase). The assays were performed during eight consecutive cycles that were completed in a total period of 216 h. After each 24-h cycle of fermentation (except for the first cycle, which lasted 48 h), the fermented broth was replaced by fresh medium, and the FFase activity was determined in the replaced medium. The average value of FFase activity was a constant 40.6 U/ml at the end of the initial seven cycles, but had decreased by 22% at the end of the eighth cycle. Concurrent with these high and constant FFase values, the hydrolyzing activity of this enzyme increased during the cycles, while the transfructosylating activity decreased. As a consequence, the maximum production of fructooligosaccharides of 134.60 g/l observed in the initial 30 h of fermentation (first cycle) had gradually decreased by the end of the subsequent cycles, reaching approximately 23% of this value during cycles 4–8. Based on these results, we conclude that the present immobilization system has a great potential for application in a semi-continuous process for the production of FFase, but further studies are necessary to maintain the FFase transfructosylation activity at high levels during the overall process.     

Identification of an extracellular thermostable glycosyl hydrolase family 13 α-amylase from <Emphasis Type="Italic">Thermotoga neapolitana</Emphasis>

We cloned the gene for an extracellular α-amylase, AmyE, from the hyperthermophilic bacterium Thermotoga neapolitana and expressed it in Escherichia coli. The molecular mass of the enzyme was 92 kDa as a monomer. Maximum activity was observed at pH 6.5 and temperature 75°C and the enzyme was highly thermostable. AmyE hydrolyzed the typical substrates for α-amylase, including soluble starch, amylopectin, and maltooli-gosaccharides. The hydrolytic pattern of AmyE was similar to that of a typical α-amylase; however, unlike most of the calcium (Ca²⁺)-dependent α-amylases, the activity of AmyE was unaffected by Ca²⁺. The specific activities of AmyE towards various substrates indicated that the enzyme preferred maltooligosaccharides which have more than four glucose residues. AmyE could not hydrolyze maltose and maltotriose. When maltoheptaose was incubated with AmyE at the various time courses, the products consisting of maltose through maltopentaose was evenly formed indicating that the enzyme acts in an endo-fashion. The specific activity of AmyE (7.4 U/mg at 75° C, pH 6.5, with starch as the substrate) was extremely lower than that of other extracellular α-amylases, which indicates that AmyE may cooperate with other highly active extracellular α-amylases for the breakdown of the starch or α-glucans into maltose and maltotriose before transport into the cell in the members of Thermotoga sp.     

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.