Anchorage of cyclodextrin glucanotransferase on the outer membrane of Escherichia coli

The gene encoding cyclodextrin glucanotransferase (CGTase) was successfully cloned from B. macerans by PCR. A recombinant plasmid pCS005 with a gene encoding the Lpp-OmpA-CGTase trifusion protein was constructed and transformed into E. coli for the surface display of CGTase. Results of immunoblotting analysis and protease accessibility on the fractionated cell membranes confirmed that the Lpp-OmpA-CGTase trifusion protein was successfully anchored on the outer membrane of E. coli. However, only 50% of the membrane-anchored trifusion proteins were displayed on the outer surface of E. coli with the remaining 50% un-translocated. The low efficiency of surface display is attributed to the large size of CGTase. Only a trace amount of CGTase activity was detected for both the whole cells and the cell debris fractions. Because the results of the protease accessibility study suggested that the trypsin-resistant conformation of CGTase was preserved in the membrane-anchored CGTase, we believe that the lack of enzyme activity is mainly due to the inaccessibility of the CGTase active site, near the N-terminus, for substrate molecules. It can be estimated that the critical size for surface display of protein in E. coli is approximately 70 kDa.     

Characterization of a thermostable cyclodextrin glucanotransferase from <Emphasis Type="Italic">Pyrococcus furiosus</Emphasis> DSM3638

A gene that encodes the enzyme Pyrococcus furiosus cyclodextrin glucanotransferase (PFCGT) was cloned in Escherichia coli. PFCGT was highly expressed in recombinant E. coli after compensation for codon usage bias using the pRARE plasmid. Purified PFCGT was extremely thermostable with an optimal temperature and pH of 95°C and 5.0, respectively, retaining 97% of its activity at 100°C. Incubation at 60°C for 20 min during the purification process led to a 1.5-fold increase in enzymatic activity. A time course assay of the PFCGT reaction with starch indicated that cyclic α-1,4-glucans with DPs greater than 20 were produced at the beginning of the incubation followed by an increase in β-CD. The major final product of PFCGT cyclization was β-CD, and thus the enzyme is a β-CGTase.     

Immobilization on Eupergit C of cyclodextrin glucosyltransferase (CGTase) and properties of the immobilized biocatalyst

The extreme thermophilic cyclodextrin glucanotransferase (CGTase) from Thermoanaerobacter sp. was covalently attached to Eupergit C. Different immobilization parameters (incubation time, ionic strength, pH, ratio enzyme/support, etc.) were optimized. The maximum yield of bound protein was around 80% (8.1 mg/g support), although the recovery of β-cyclodextrin cyclization activity was not higher than 11%. The catalytic efficiency was lower than 15%. Results were compared with previous studies on covalent immobilization of CGTase.

The enzymatic properties of immobilized CGTase were investigated and compared with those of the soluble enzyme. Soluble and immobilized CGTases showed similar optimum temperature (80–85 °C) and pH (5.5) values, but the pH profile of the immobilized CGTase was broader at higher pH values. The thermoinactivation of the CGTase coupled to Eupergit C was slower than the observed with the native enzyme. The half-life of the immobilized enzyme at 95 °C was five times higher than that of the soluble enzyme. The immobilized CGTase maintained 40% of its initial activity after 10 cycles of 24 h each. After immobilization, the selectivity of CGTase (determined by the ratio CDs/oligosaccharides) was notably shifted towards oligosaccharide production.     

Expression of Bacillus macerans cyclodextrin glucanotransferase gene in Saccharomyces cerevisiae

Cyclodextrin glucanotransferase (CGTase) gene of Bacillus macerans was subcloned down-stream of yeast ADH1 promoter and expressed in Saccharomyces cerevisiae. Most of the CGTase expressed was in the extracellular medium with a maximum activity of about 0.28 unit ml^–1 after 48 h cultivation. The recombinant CGTase was secreted as an N-linked-glycosylated form and predominantly produced -cyclodextrin from starch.     

Establishment of the phylogenetic relationships between the microbial producers of cyclodextrin glucanotransferases using complete amino acid sequences

A phylogenetic tree was constructed on the basis of the amino acid sequences of the known cyclodextrin glucanotransferases (CDGTs), including those deduced from the nucleotide sequences ofBacillus sp. strain 6.6.3 andPaenibacillus macerans IB-7 genes encoding α- and β-CDGTs. The tree clearly demonstrates the existence of distinct phylogenetic groups of CDGT-producing microorganisms and the divergence of the α-, β-, and γ-CDGT produced by microorganisms from the generaBacillus, Paenibacillus, Brevibacillus, andThermoanaerobacter from a common ancestor, whereas the CDGT ofKlebsiella pneumoniae is independent and results from the convergence of different ancestors. The degree of homology of the leader peptide sequences of CDGTs may serve as a criterion of intraspecies relatedness between CDGT-producing microorganisms.     

Enhanced secretory production of hemolysin-mediated cyclodextrin glucanotransferase in Escherichia coli by random mutagenesis of the ABC transporter system

The hemolysin transport system was found to mediate the release of cyclodextrin glucanotransferase (CGTase) into the extracellular medium when it was fused to the C-terminal 61 amino acids of HlyA (HlyAs(61)). To produce an improved-secretion variant, the hly components (hlyAs, hlyB and hlyD) were engineered by directed evolution using error-prone PCR. Hly mutants were screened on solid LB-starch plate for halo zone larger than the parent strain. Through screening of about 1 × 10(4) Escherichia coli BL21(DE3) transformants, we succeeded in isolating five mutants that showed a 35-217% increase in the secretion level of CGTase-HlyAs(61) relative to the wild-type strain. The mutation sites of each mutant were located at HlyB, primarily along the transmembrane domain, implying that the corresponding region was important for the improved secretion of the target protein. In this study we describe the finding of novel site(s) of HlyB responsible for enhancing secretion of CGTase in E. coli.     

Catalytic properties of β-cyclodextrin glucanotransferase from alkalophilic<Emphasis Type="Italic">Bacillus</Emphasis> sp. BL-12 and intermolecular transglycosylation of stevioside

The catalytic properties of β-cyclodextrin glucanotransferase (β-CGTase) from alkalophilicBacillus sp. BL-12 specific for the intermolecular transglycosylation of stevioside were investigated. The molecular mass of purified β-CGTase by ultra-filtration and β-cyclodextrin polymer affinity chromatography was estimated to be 90 kDa, which is high compared to other known bacterial CGTases. The optimal pH and temperature were 9.0 and 50°C, respectively, and thermal stability at 40°C was elevated 10-fold in the presence of 1% maltodextrin. The kinetic parameters of the new β-CGTase from alkalophilicBacillus sp. BL-12 indicate that it is more suitable for transglycosylation than the cyclization reaction. Maltodextrin was the most suitable glycosyl donor for transglycosylation of stevioside. The transglycosylation of stevioside was carried out using 60 units of CGTase per gram of maltodextrin, 20 g/L stevioside as the glycosyl acceptor, and 50 g/L maltodextrin as the gycosyl donor at 40°C for 6 h, and a conversion yield of stevioside as high as 76% was obtained.     

Effects of environmental conditions on production of xylitol byCandida boidinii

Candida boidinii NRRL Y-17213 produced more xylitol thanC. magnolia (NRRL Y-4226 and NRRL Y-7621),Debaryomyces hansenii (C-98 M-21, C-56 M-9 and NRRL Y-7425), orPichia (Hansenula) anomala (NRRL Y-366). WithC. boidinii, highest xylitol productivity was at pH 7 but highest yield was at pH 8, using 5 g urea and 5 g Casamino acids/I. Decreasing the aeration rate decreased xylose consumption and cell growth but increased the xylitol yield. When an initial cell density of 5.1 g/l was used instead of 1.3 g/l, xylitol yield and the specific xylitol production rate doubled. Substrate concentration had the greatest effect on xylitol production; increasing xylose concentration 7.5-fold (to 150 g/l) gave a 71-fold increase in xylitol production (53 g/l) and a 10-fold increase in xylitol/ethanol ratio. The highest xylitol yield (0.47 g/g), corresponding to 52% of the theoretical yield, was obtained with 150 g xylose/l after 14 days. Xylose at 200 g/l inhibited xylitol production.E. Vandeska and S. Kuzmanova were and S. Amartey and T. Jeffries are with the Forest Products Laboratory, Institute for Microbial and Biochemical Technology, 1 Gifford Pinchot Drive, Madison, WI 53703, USA. E. Vandeska and S. Kuzmanova are now with the Faculty of Technology and Metallurgy, Rudjer Boskovic 16, 91000 Skopje, Macedonia     

Purification and characterisation of NAD+-dependent xylitol dehydrogenase from Fusarium oxysporum

An NAD⁺-dependent xylitol dehydrogenase (XDH) from Fusarium oxysporum, a key enzyme in the conversion of xylose to ethanol, was purified to homogeneity and characterised. It was homodimeric with a subunit of M _r 48 000, and pI 3.6. It was optimally active at 45 °C and pH 9–10. It was fully stable at pH 6–7 for 24 h and 30 °C. K _m values for d-xylitol and NAD⁺ were 94 mM and 0.14 mM, respectively. Mn²⁺ at 10 mM increased XDH activity 2-fold and Cu²⁺ at 10 mM inhibited activity completely.     

Production of xylitol in cell recycle fermentations of Candida tropicalis

Xylitol was produced a in two-substrate, batch fermentation with cell recycling of Candida tropicalis ATCC 13803. A series of cell-recycle experiments showed that the feeding of xylose, glucose and yeast extract in the xylitol production phase was most effective in enhancing xylitol productivity. The optimized cell recycle fermentation resulted in 0.82 g xylitol/g xylose yield, 4.94 g xylitol l^–1 h^–1 productivity, and final xylitol concentration of 189 g l^–1. These results were 1.3 times higher in volumetric xylitol productivity and 2.2 times higher in final product concentration compared with the corresponding values of the optimized two-substrate batch culture.     

Glucose repression of xylitol production in Candida tropicalis mixed-sugar fermentations

Glucose repressed xylose utilization inCandida tropicalis pre-grown on xylose until glucose reached approximately 0–5 g l^–1. In fermentations consisting of xylose (93 g l^–1) and glucose (47 g l^–1), xylitol was produced with a yield of 0.65 g g^–1 and a specific rate of 0.09 g g^–1 h^–1, and high concentrations of ethanol were also produced (25 g l^–1). If the initial glucose was decreased to 8 g l^–1, the xylitol yield (0.79 g g^–1) and specific rate (0.24 g g^–1 h^–1) increased with little ethanol formation (<5 g l^–1). To minimize glucose repression, batch fermentations were performed using an aerobic, glucose growth phase followed by xylitol production. Xylitol was produced under O₂ limited and anaerobic conditions, but the specific production rate was higher under O₂ limited conditions (0.1–0.4 vs. 0.03 g g^–1 h^–1). On-line analysis of the respiratory quotient defined the time of xylose reductase induction.     

Immobilization of Zymomonas mobilis 2716, for the protection of cellular activity

Alginate-immobilized Zymomonas mobilis cells produced 17.8% (v/v) ethanol in less than 24 h, with an ethanol yield of 97%, compared with 88% for free cells, using a fed-batch cultivation technique. The substrate, glucose, was added intermittently in powder form to foster nucleation of the CO₂ formed. Repeated-batch cultivation led to complete utilization of approximately 200 g glucose/l in 7.5 h with a 98% conversion efficiency to ethanol. Free cells used the glucose less efficiently (conversion efficiency of 78%), and even after 100 h the glucose was not fully consumed. Freeze-substitution electron microscopy studies showed that immobilized cells generally displayed lesser blebbing and membrane disruption than free cells. These studies further suggest that membrane blebbing may be due to an effect of high initial glucose levels, and not due to the accumulation of end-products ethanol and CO₂.L.A. Kirk, H.W. Doelle and R.I. Webb are with the Department of Microbiology, University of Queensland, Brisbane, QId 4072, Australia. R.I. Webb is also with the Microscopy and Microanalysis Centre, University of Queensland, Brisbane, QId 4072, Australia;     

Hydrolysate detoxification with activated charcoal for xylitol production by Candida guilliermondii

A detoxification method using activated charcoal with concentrated rice straw hemicellulosic hydrolysate improved the conversion of xylose to xylitol by the yeast Candida guilliermondii by 22%. This was achieved when the hydrolysate:charcoal ratio was 40 g g^–1, resulting in removal of 27% of phenolic compounds. Under this condition, the xylitol yield factor (0.72 g g^–1) and volumetric productivity (0.61 g l^–1 h^–1) were close to those attained in a semi-defined medium simulating hydrolysate sugars.     

Immobilization of endo-polygalacturonase from Aspergillus ustus on silica gel

Endo-polygalacturonase from Aspergillus ustus when immobilized on to modified silica gel retained 28% of its original activity. The immobilized enzyme could be re-used through 10 cycles of reaction with almost 90% retention of its original activity. It had increased thermostability over its soluble form: the half-life of the soluble enzyme at 40 °C was less than 10 h whereas the immobilized enzyme retained 82% of its activity after 10 h at 40 °C. Similarly, at 50 °C the half-life of the soluble enzyme was 30 min whereas that of the immobilized enzyme was 5 h.     

Use of a Novel Immobilization Yeast System for Winemaking

Penicillium was used to immobilize Saccharomyces cerevisiae, without using physico-chemical external supports, to form yeast biocapsules. The biocapsules, once the Penicillium was killed by the ethanol produced, were used in a grape must fermentation. Must fermentation was carried out for 160 h with the biocapsules and for 300 h with free yeast cells. Acetaldehyde (84 vs. 63 mg/l), isobutanol (217 vs. 194 mg/l), L-proline (7.7 vs. 6.5 mM) and aspartic acid (0.42 vs. 0 mM) in final wine were higher with the biocapsules than with free cells.     

Effect of inoculum level on xylitol production from rice straw hemicellulose hydrolysate byCandida guilliermondii

The effect of inoculum level on xylitol production byCandida guilliermondii was evaluated in a rice straw hemicellulose hydrolysate. High initial cell density did not show a positive effect in this bioconversion since increasing the initial cell density from 0.67 g L^–1 to 2.41 g L^–1 decreased both the rate of xylose utilization and xylitol accumulation. The maximum xylitol yield (0.71 g g^–1) and volumetric productivity (0.56 g L^–1 h^–1) were reached with an inoculum level of 0.9 g L^–1. These results show that under appropriate inoculum conditions rice straw hemicellulose hydrolysate can be converted into xylitol by the yeastC. guilliermondii with efficiency values as high as 77% of the theoretical maximum.     

Cyclodextrin production and genetic characterization of cyclodextrin glucanotranferase of <Emphasis Type="Italic">Paenibacillus graminis</Emphasis>

Paenibacillus graminis strains were described recently as cyclodextrin (CD) producers. Cyclodextrins are produced by cyclodextrin glucanotransferase (CGTase) which has not been characterized in P. graminis. Similar amounts of α- and β-CDs were produced by P. graminis (MC22.13) and P. macerans (LMD24.10^T). Primers were designed to sequence the gene encoding CGTase from P. graminis. A phylogenetic tree was constructed and P. graminis CGTase protein showed to be closer (79.4% protein identity) to P. macerans |P31835|. Hybridization studies suggested that the gene encoding CGTase is located in different positions in the genomes of P. macerans and P. graminis.     

Immobilization of cells of Nicotiana tabacum L. on polyphenyleneoxide coated with poly-L-lysine

Cells of Nicotiana tabacum L. cv. Wisconsin 38 were immobilized on poly (2,6-dimethyl)-p-phenyleneoxide in powder form (Sorfix) coated with poly-L-lysine (molecular weight 40 000 daltons). The dependence of cell immobilization on the amount of bound polyL-lysine was estimated.Abbreviations MW molecular weight - dwt dry weight - fwt fresh weight     

Effects of Immobilization Stress on the Background Impulse Activity of Locus Coeruleus Neurons

We studied in rats changes in the impulse background activity (BA) of locus coeruleus (LC) neurons after short- and long-term immobilization stress; distributions of LC neurons by the level of regularity of their BA, dynamics of spike trains, and pattern of histograms of interspike intervals (ISI) were taken into account. We also calculated the means of the main BA statistical indices. Both short- and long-lasting immobilizations resulted in drops in the mean frequency of background discharges of LC neurons to about half of the initial value. Two-hour-long immobilization evoked statistically significant shifts in the distribution of LC neurons by the level of regularity of their BA, while after longer (15 h) immobilization this distribution nearly returned to the initial pattern. Short-lasting immobilization exerted no significant effect on the dynamic characteristics of BA; statistically significant changes in this respect developed only after longer stress. After 15-h-long immobilization, we also observed a noticeable increase in the number of neurons with polymodal ISI distributions. Therefore, stress results in significant modifications of the temporal parameters of the BA of LC neurons; characteristics of the BA of these neurons should be considered neuronal correlates of the stress state.     

Immobilized cells cultivated in semi-continuous mode in a fluidized bed reactor for xylitol production from sugarcane bagasse

Summary Xylitol production from sugarcane bagasse hemicellulosic hydrolyzate was evaluated in a fluidized bed reactor operated in semi-continuous mode, using cells immobilized on porous glass. The fermentative process was performed during five successive cycles of 72 h each one. The lowest xylitol production occurred in the first cycle, where a high cell concentration (12 g l⁻¹) was observed. In the subsequent cycles the xylitol concentration was ever increasing due to the cells adaptation to the medium. In the last one, 18 g xylitol l⁻¹ was obtained with a yield factor of 0.44 g g⁻¹ and volumetric productivity of 0.32 g l⁻¹ h⁻¹.