Purification and characterization of α-glucosidase from Aspergillus carbonarious

Summary An -glucosidase was purified from Aspergillus carbonarious CCRC 30414 over 20 fold with 37 % recovery. Its molecular mass was estimated to be 328 kDa by gel filtration with an optimum pH from 4.2 to 5.0, and pI=5.0. The optimum temperature is at 60°C over 40 min. The enzyme was partially inhibited by 5 mM Ag⁺, Hg²⁺, Ba²⁺, Pb²⁺, and Aso₄ ⁺.     

Immobilization of <Emphasis Type="Bold">β</Emphasis>-fructofuranosidase from <Emphasis Type="Italic">Aspergillus japonicus</Emphasis> on chitosan using tris(hydroxymethyl)phosphine or glutaraldehyde as a coupling agent

A partially purified -fructofuranosidase from Aspergillus japonicus was covalently immobilized on to chitosan beads using either glutaraldehyde or tris(hydroxymethyl)phosphine (THP) as a coupling agent. Compared with the glutaraldehyde-immobilized and the free enzyme, the THP-immobilized enzyme had the highest thermal stability with 78% activity retained after 12 days at 37 ° C. The THP-immobilized enzyme also had higher reusability than that immobilized by glutaraldehyde, 75% activity was retained after 11 batches (or 11 days) at 37° C for the THP immobilized enzyme system. Less yield (48%) of fructooligosaccharides (FOS) were produced by the THP-immobilized enzyme compared with the free enzyme system (58%) from 50 (w/v) sucrose at 50 ° C.     

Production of High-content Galacto-oligosaccharide by Enzyme Catalysis and Fermentation with Kluyveromyces marxianus

Of three β-galactosidases from Aspergillus oryzae, Kluyveromyces lactis and Bacillus sp., used for the production of low-content galacto- oligosaccharides (GOS) from lactose, the latter produced the highest yield of trisaccharides and tetrasaccharides. GOS production was enhanced by mixing β-galactosidase glucose oxidase. The low-content GOS syrups, produced either by β-galactosidase alone or by the mixed enzyme system, were subjected to the fermentation by Kluyveromyces marxianus, whereby glucose, galactose, lactose and other disaccharides were depleted, resulting in up to 97% and 98% on a dry weight basis of high-content GOS with the yields of 31% and 32%, respectively. An erratum to this article can be found at     

Continuous production of high-content fructooligosaccharides by a complex cell system

A complex biocatalyst system with a bioreactor equipped with a microfiltration (MF) module was employed to produce high-content fructooligosaccharides (FOS) in a continuous process initiated by a batch process. The system used mycelia of Aspergillus japonicus CCRC 93007 or Aureobasidium pullulans ATCC 9348 with beta-fructofuranosidase activity and Gluconobacter oxydans ATCC 23771 with glucose dehydrogenase activity. Calcium carbonate slurry was used to control pH to 5.5, and gluconic acid in the reaction mixture was precipitated as calcium gluconate. Sucrose solution with an optimum concentration of 30% (w/v) was employed as feed for the complex cell system, and high-content FOS was discharged continuously from a MF module. The complex cell system was run at 30 degrees C with an aeration rate of 5 vvm and produced more than 80% FOS with the remainder being 5-7% glucose and 8-10% sucrose on a dry weight basis, plus a small amount of calcium gluconate. The system worked for a 7-day continuous production process with a dilution rate of 0.04 h(-1), and the volumetric productivity for total FOS was more than 160 g L(-1) h(-1).     

The critical roles of polyamines in regulating ColE7 production and restricting ColE7 uptake of the colicin-producing Escherichia coli

The ColE7 operon is an SOS response regulon, which encodes bacteriocin ColE7 to kill susceptible Escherichia coli and its related enterobacteria under conditions of stress. We have observed for the first time that polyamines confer limited resistance against ColE7 on E. coli cells. Thus, this study aims to investigate the role of polyamines in modulating the protective effect of the E. coli cells against colicin. In the experiments, we surprisingly found that endogenous polyamines are also essential for ColE7 production, and the rate of polyamine synthesis is directly related to the SOS response. Our experimental results further indicated that exogenous polyamines suppress the expression of TolA, BtuB, OmpF, and OmpC proteins that are responsible for ColE7 uptake. Moreover, two-dimensional gel electrophoresis revealed that the production of two periplasmic proteins, PotD and OppA, is increased in E. coli cells under ColE7 exposure. Based on these observations, we propose that endogenous polyamines may play a dual role in the ColE7 system. Polyamines may participate in initiating the expression of the SOS response of the ColE7 operon and simultaneously down-regulate proteins that are essential for colicin uptake, thus conferring a survival advantage on colicin-producing E. coli under stress conditions in the natural environment.     

Purification of a trypsin inhibitor from sweet potato in an aqueous two phase system

Trypsin inhibitor from sweet potato was extracted and purified in a single step using an aqueous two-phase system of polyethylene glycol 6000 (11% w/v), phosphate (16.5% w/v), KCl (9% w/v) and at pH 6. Purity of the trypsin inhibitor was enhanced 3.7-fold, and the recovery was 95%. The purified trypsin inhibitor showed one visible band, and the molecular size was 23 kDa by SDS-PAGE.     

Unusual stability of manganese superoxide dismutase from a new species, Tatumella ptyseos ct: its gene structure, expression, and enzyme properties

A genomic DNA of 1416 bp containing an open reading frame encoding a manganese superoxide dismutase (Mn-SOD) from Tatumella ptyseos ct was cloned. Sequence analysis of this new gene revealed that it translates 205 amino acid residues. The deduced amino acid sequence showed variable identities (41-91%) with sequences of Mn-SODs from other species. The residues required to coordinate the single trivalent manganese ion and the 11 residues putatively involved in the active center are conserved as they are in other reported Mn-SODs. In addition, the gene was introduced into the expression vector, pET-20b(+), and transformed in Escherichia coli BL21(DE3). The Mn-SOD was purified by a His-tag technique. The yield was 0.9 mg from 0.5 L of culture. The specific activity was 6540 U/mg. A dimer is the major form of the enzyme in equilibrium. The half-life of dimer is approximately 50 min and its thermal inactivation rate constant k(d) was 0.015 min(-1) at 80 degrees C. The dimerization of the enzyme was inhibited under an acidic pH (below 4.0), or in the presence of SDS (above 1%) or imidazole (above 0.5 M), whereas it was not affected under an alkaline pH (above 9.0). Furthermore, the dimeric enzyme was much more resistant to proteolytic attack after 3 h of incubation at 37 degrees C with trypsin and chymotrypsin. This unusually stable enzyme can be used as cosmetic to the protection of skin against the unaesthetic effects caused by free radicals.     

Production of xylitol from Candida tropicalis by using an oxidation-reduction potential-stat controlled fermentation

An on-line device, ORP (oxidation-reduction potential)-stat, was used to control glucose-feeding for enhancing xylitol conversion from D-xylose during an oxygen-limited fermentation by Candida tropicalis. The fermentation was carried out in a 5 l jar fermenter. After glucose in the medium was depleted, a switching to a limited aeration and feeding glucose controlled by ORP-stat was performed. The maximum xylitol yield was obtained under a condition at an ORP of -180 mV and at an aeration rate of 0.2 l min(-1).     

Production of xylitol from Candida tropicalis by using an oxidation-reduction potential-stat controlled fermentation

An on-line device, ORP (oxidation-reduction potential)-stat, was used to control glucose-feeding for enhancing xylitol conversion from D-xylose during an oxygen-limited fermentation by Candida tropicalis. The fermentation was carried out in a 5 l jar fermenter. After glucose in the medium was depleted, a switching to a limited aeration and feeding glucose controlled by ORP-stat was performed. The maximum xylitol yield was obtained under a condition at an ORP of - 180 mV and at an aeration rate of 0.2 l min(-1).