Screening and characterization of bioflocculant produced by isolated Klebsiella sp.

Sixteen strains of polymer-producing bacteria were isolated from the activated sludge samples taken from two seafood processing plants in Southern Thailand. Their culture broths possessed the ability to flocculate kaolin suspension in the presence of 1% CaCl2. Based on the flocculating activity, the strain S11 was selected and identified to be a Klebsiella sp. using the partial 16S rRNA sequencing method. The growth of the isolated Klebsiella sp. was maximal (1.026 g l-1 dry cell mass) after 1 day cultivation while the highest polymer yield (0.973 g l-1) was achieved after 5 days cultivation. The flocculating activity of the culture broth, however, was highest after 2 days cultivation. The polymer was identified to be an acidic polysaccharide containing neutral sugar and uronic acid as its major and minor components, respectively. Results on the properties of the partially purified polysaccharide from Klebsiella sp. S11 revealed that it consisted of galactose, glucose and mannose in an approximate ratio of 5:2:1. It was soluble in acidic or basic solutions but not in organic solvents. Its molecular mass was greater than 2 x 10(6) Da. Infrared spectra showed the presence of hydroxyl, carboxyl and methoxyl groups in its molecules. Differential scanning calorimetry of the polysaccharide indicated the crystalline melting point (Tm) at 314 degrees C. The optimum dosage of polysaccharide to give the highest flocculating activity was 15 mg l-1 in the presence of 1% CaCl2.

Laboratory and clinical evaluation of two glucose meters for the neonatal intensive care unit.

OBJECTIVE: To evaluate the analytical and clinical performance of the One Touch II and Advantage glucose meters for use in neonatal specimens. DESIGN AND METHODS: For the laboratory evaluation, a total of 96 umbilical cord whole blood specimens were analyzed on the One Touch II and/or Advantage meters. Samples were centrifuged after analysis on the meters and plasma glucose was determined on the Hitachi 917. For the clinical evaluation, a total of 64 infants had specimens analyzed on each of the meters as well as on the laboratory analyzer. RESULTS: In the laboratory and clinical evaluations, both meters correlated well (r > 0.9, p < 0.001) with the plasma values for the Hitachi 917. However, the mean difference between the Advantage and Hitachi 917 was lower than that of the One Touch II in both the laboratory (-0.23 vs -0.64 mmol/L) and the clinical evaluations (-0.08 vs -0.60 mmol/L). 53.1% of One Touch and 26.6% of Advantage results from the clinical study had a discrepancy of > 0.5 mmol/L from the laboratory value. CONCLUSIONS: For neonatal specimens, glucose meters must have good low end precision, sensitivity and accuracy, In this study, the Advantage meter had fewer discordant results and better correlation with the Hitachi 917. Overall, nursing and laboratory staff preferred the performance and characteristics of the Advantage meter.

Cholesteryl ester transfer protein mediates selective uptake of high density lipoprotein cholesteryl esters by human adipose tissue.

We have determined the role of cholesteryl ester transfer protein (CETP) in selective uptake of high density lipoprotein (HDL)-derived cholesteryl esters (CE) by human adipose tissue, using organ culture or collagenase-digested adipocytes. Incubation of the fresh tissue fragments with HDL containing [3H]CE or 125I-apoprotein (apo) A-I resulted in significant uptake of HDL-CE-derived label. Addition of recombinant CETP (rCETP) increased CE uptake in a dose-response fashion. In contrast, little association of 125I-apoA-I with adipose tissue was noted, and addition of rCETP did not alter apoA-I uptake or degradation. Incubation of adipose tissue with TP2, an anti-CETP monoclonal antibody, which inhibits neutral lipid transfer, markedly reduced selective uptake of HDL-CE. Studies using human adipocytes isolated by collagenase digestion also demonstrated selective uptake of HDL-CE and enhancement of this process by rCETP. To confirm that the association of HDL-CE-derived radioactivity with adipose tissue was not due to neutral lipid exchange between adipocytes and HDL, we measured changes in HDL composition following incubation of HDL and rCETP with isolated adipocytes. A decrease in HDL-CE concentration in the medium was observed, an effect which was markedly attenuated when incubations were carried out in the presence of monoclonal antibody TP2. Furthermore, the decrease in HDL-CE was accompanied by an increase in HDL free cholesterol, likely representing efflux of adipocyte cholesterol to HDL. There were no significant changes in phospholipid, apoA-I, or apoA-II in the medium following incubation with adipocytes. These data demonstrate a novel and important role for CETP in selective uptake of HDL-cholesteryl esters by human adipocytes and suggest that this pathway may be of quantitative physiological significance in HDL remodeling and adipocyte cholesterol accumulation.

Changes in the growth and enzyme level of Zymomonas mobilis under oxygen-limited conditions at low glucose concentration.

Zymomonas mobilis growing aerobically with 20 g glucose-1 (carbon-limited) in a chemostat exhibited an increase in both the molar growth yield (Yx/s) and the maximum molar growth yield (Yx/smax) and a decrease in both the specific substrate consumption rate (qs) and the maintenance energy consumption rate (me). Stepwise increase in the input oxygen partial pressure showed that anaerobic-to-aerobic transitional adaptation occurred in four stages: anaerobic (0 mm HgO2), oxygen-limited (7.6- 230 mm HgO2), intermediate (273 mm HgO2), and oxygen excess (290 mm HgO2). The steady-state biomass concentration, Yx/s, and intracellular ATP content increased between oxygen partial pressures of 7.6 and 120 mm HgO2, accompanied by a decrease in the qs and the specific acid production rate. The membrane ATPase activity decreased with increasing oxygen partial pressure and reached its lowest levels at 273 mm HgO2, which was the highest input oxygen partial pressure where steady-state conditions were possible. Glucokinase, glucose-6-phosphate dehydrogenase, glyceraldehyde-3-phosphate dehydrogenase, and alcohol dehydrogenase activities also decreased when the oxygen partial pressure was increased above 15 mm Hg, whereas pyruvate decarboxylase was unaffected by aeration. Growth inhibition at 290 mm HgO2 was characterised by a drastic reduction in the pyruvate kinase activity and a collapse in the intracellular ATP pool. The growth and enzyme data suggest that at low glucose concentrations and oxygen-limited conditions, the increase in biomass yields is a reflection of a redirection of ATP usage rather than a net increase in energy production.

Joint venture capital investment for clean technologies and their problems in developing countries.

All technological developments are aimed at improving the quality of life of a community of people. Biotechnology is a technology which allows the exploitation of microorganisms, plants and animal cells to take place within an economic framework. Developing countries are looking for programmes achieving sustainable, economical growth conducive to a higher per capita income of the community. Any joint venture which promises social advances and economic benefits will have to be rural-based. This presentation discusses the need for a change in fermentation industry attitudes to allow joint venture capital investment in clean technologies together with the problems developing countries face for the implementation of such technologies.

Degradation of the cyanobacterial hepatotoxin microcystin by aquatic bacteria.

Bacterial degradation of the cyanobacterial cyclic peptide hepatotoxin microcystin was confirmed in natural waters and by isolated laboratory strains. Degradation of 1 mg L-1 microcystin LR typically began 2-8 days after addition to surface water samples. At concentrations greater than 1 mg L-1 there was an initial slow removal of microcystin LR, rather than a distinct lag (or conditioning) phase, before rapid degradation commenced. The lag phase was absent upon re-addition of microcystin LR to the water. Both single strains and mixed bacterial cultures capable of degrading microcystin LR were isolated from surface water samples. One single strain isolated was a gram-negative rod and appeared to be a Pseudomonas sp., although standard taxonomic tests have given inconclusive results. Degradative activity was mostly intracellular and equally active against microcystin LR and RR, but not against nodularin.

Capsule formation in Zymomonas mobilis grown on sucrose.

A capsule formed around Zymomonas mobilis grown on sucrose, increasing in thickness with higher initial sucrose concentrations. Cryofixation and freeze-substitution electron microscopy techniques preserved this polymer matrix, unlike other techniques.

Operational parameters for packed beds in solid-state cultivation.

Packed bed cultivation systems have potential for widespread application in solid-state cultivation (SSC), but they are poorly characterized. The effects of particle size and substrate loading on the growth of Rhizopus oligosporus on sago-beads in packed bed bioreactors were investigated. Pressure drop and protein were monitored as indicators of fungal growth in cultivations performed in a large column (4.9 cm internal diameter and 60 cm height) and a system of small columns (4.2 cm internal diameter and 5.2 cm height). The differential pressure drop increased to a maximum between 34 and 44 h and then decreased again. The maximum differential pressure drop attained was greatest for the smallest particle size and for the lower substrate loadings. However, since the protein content continued to increase throughout the cultivation, pressure drop could not be used to monitor growth directly.

Zymomonas mobilis--science and industrial application.

Zymomonas mobilis is undoubtedly one of the most unique bacterium within the microbial world. Known since 1912 under the names Termobacterium mobilis, Pseudomonas linderi, and Zymomonas mobilis, reviews on its uniqueness have been published in 1977 and 1988. The bacterium Zymomonas mobilis not only exhibits an extraordinarily uniqueness in its biochemistry, but also in its growth behavior, energy production, and response to culture conditions, as well as cultivation techniques used. This uniqueness caused great interest in the scientific, biotechnological, and industrial worlds. Its ability to couple and uncouple energy production in favor of product formation, to respond to physical and chemical environment manipulation, as well as its restricted product formation, makes it an ideal microorganism for microbial process development. This review explores the advances made since 1987, together with new developments in the pure scientific and applied commercial areas.

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.

A semimechanistic mathematical model for growth of Rhizopus oligosporus in a model solid-state fermentation system.

A Semimechanistic mathematical model is developed which describes the growth of Rhizopus oligosporus in a model solid-state fermentation system. Equations are presented for the release of glucoamylase, the diffusion of glucoamylase, the hydrolysis of starch, the generation and diffusion of glucose, and the uptake of glucose and conversion into new biomass. Good agreement of the model with the experimental data was obtained only after the glucoamylase diffusivity and the maximum specific glucose uptake rate were altered from their originally determined values. The model recognizes the distributed nature of the solid-state fermentation and therefore is able to predict the concentration profiles of the system components within the substrate. The model provides an insight into the possible rate-limiting steps in solid-state fermentation-the generation of glucose within the substrate and the resulting availability of glucose at the surface.

Protein enrichment of sago starch by solid-state fermentation with Rhizopus spp.

Protein enrichment of sago starch of three different diameters was investigated both in flask culture and under forced aeration in a packed-bed fermenter using two strains of Rhizopus. Protein production by R. oligosporus UQM 145F was superior to Rhizopus sp. UQM 186F in the flask culture without aeration, with both preferring larger diameter (3 to 4 mm) spherical sago-beads. In the packed-bed fermenter with forced aeration, Rhizopus sp. UQM 186F led to more rapid protein production compared to R. ollgosporus UQM 145F and produced equivalent final yields (about 10% protein on a dry wt basis).

Mode of growth ofRhizopus oligosporus on a model substrate in solid-state fermentation.

The growth ofRhizopus oligosporus on a model solid substrate consisting of cassava starch and other nutrients embedded in a kappa-carrageenan matrix was followed microscoplcally. There were two distinct growth phases: (1) germination of spores and development of mycellum to form a loose network over the whole substrate surface; (2) increase in the density of the mycellum. Although some penetrative hyphae were produced, the biomass was malnly restricted to the surface. Consequently, starch utilization was greatest near the surface. Based on these observations a descriptive model for the growth ofRhizopus ollgosporus on the model substrate was proposed. The five steps are: (1) release of glucoamylase by the mycelium; (2) diffusion of the glucoamylase to the starch; (3) hydrolysis of the starch by the glucoamylase, releasing glucose; (4) diffusion of glucose; (5) absorption of glucose by the mycellum at the surface to produce new blomass.

Optimization of physiological factors for direct saccharification of cassava starch to glucose by Rhizopus oligosporus 145f.

Direct saccharification of 2.64% cassava starch by Rhizopus oligosporus 145F was attempted under various cultural conditions. Maximum glucose yield of 18.0 g/L culture filtrate was obtained with an initial pH 3.8, 2% (v/v) inoculum of R. oligosporus spores, and an incubation temperature of 45 degrees C in shake flask cultures for 48 h. This concomitantly produced 2.7 g mycelia/100g cassava starch containing 20.2% true protein. The production of glucose and mycelia was accomplished with 92.8% starch saccharification having 67.9% starch to glucose conversion efficiency.

Microbial cultures in the utilization of cellulosic materials.

This review elaborates on the most recent microbial development in saccharification of cellulose and cellulase formation. A particular highlight is a new genetic-immunochemical approach investigating the mechanism of adhesion of bacterial cellulase to cellulose during cellulose conversion. New developments and recent reviews in hemicellulose and lignin degradation are also covered.

Use of Cibacron Blue--Sepharose 6B to detect modifications of the non-allosteric 6-phosphofructokinase from Escherichia coli K-12.

In crude cell-free extracts of aerobically grown E. coli K-12, the non-allosteric form of 6-phosphofructokinase has a tetrameric molecular weight 140 000 with a low affinity (less than 5%) for the blue dextran chromophore--Cibacron Blue. The allosteric form has the same tetrameric molecular weight, but possesses a strong affinity for the blue dextran chromophore. Under conditions of prolonged storage, purification procedures of mild heat treatment (50 degrees C), the non-allosteric form converts to an active dimer (mol. wt 67 000), which binds to Cibacron Blue (less than 90%). Acid precipitation plus heat treatment prevents the conversion to the dimeric form and retains low Cibacron Blue affinity. These results are consistent with the isolation of a low molecular weight form and suggest that the inherent lability of this enzyme might be due to both non-specific proteolytic modification and a weak quaternary structure.

Further kinetic characterization of the non-allosteric phosphofructokinase from Escherichia coli K-12.

The labile non-allosteric form of phosphofructokinase (ATP:D-fructose-6-phosphate 1-phosphotransferase, EC 2.7.1.11) was purified to a specific activity of 107 U/mg (2078-fold) from aerobic cultures of Escherichia coli K-12. The enzyme has an isoelectric point (pI) of 5.1, a native molecular weight of 67 000 +/- 3000 and a subunit weight of 34 000 +/- 400. A number of divalent metal ions can substitute for Mg2+ in the enzyme reaction in decreasing order Mn2+ > Mg2+ > Co2+ > Ca2+. In the presence of excess Mg2+, nucleotides do not affect the Km for fructose 6-phosphate with a value of 0.042 mM. The order of efficiency for nucleotides to act as phosphoryl donors is ATP > ITP > GTP > UTP > CTP. This remains unchanged in the presence of excess Mn2+, but V is increased 2.4-fold with ATP. A 2 : 1 ratio of Mn2+/nucleotide 5'-triphosphate produced an equivalent dissociation constant of 1.1 mM for all nucleotides, which was markedly decreased at a high Mn2+ level. The rate of enzyme catalysis was found to be dependent on the concentration of MnATP2-. Mn2+ at non-limiting values does affect the binding of fructose 6-phosphate to the enzyme.

Transitional steady-state investigations during aerobic-anaerobic transition of glucose utilization by Escherichia coli K-12.

Transitional steady-state investigations during changes in oxygen tension under aerobic and during aerobic-anaerobic transition conditions were carried out with the aim of finding an indicator system which separates the equilibrium from the non-equilibrium state. Of the parameters used i.e. biomass formation, CO2 production, Q02, NADH oxidase, succinate dehydrogenase, phosphofructokinase, glyceraldehyde-3 phosphate dehydrogenase, 6-phosphogluconate dehydrogenase and 2-oxoglutarate dehydrogenase, only the three enzymes requiring NADH or NADP for their function fulfilled the requirements. Biomass production and CO2 formation were useful only during the aerobic-anaerobic transition period. In each case the response was immediate and the indicator systems demonstrated that a new steady state of oxygen was always obtained after 11 h which, at the specific growth rate used, was equivalent to at least two volume replacements of the growth vessel.

Bioenergetic aspects of aerobic glucose metabolism of Escherichia coli K-12 under varying specific growth rates and glucose concentrations.

An attempt was made to find a bioenergetical explanation for the differential effect of specific growth rate and glucose concentration on glucose metabolism of Escherichia coli K-12 with the help of 2,4-dinitrophenol (DNP). The effect of DNP on biomass occurred only at high glucose concentrations. The presence of this uncoupler strongly stimulated glucose uptake rates and oxygen uptake rates, but repressed severly Yg values. Increase in glucose concentration, however, sharply decreased QO2. The amount of oxygen required for maintenance was not affected by DNP, but Yomax values were much lower in the presence of DNP. The results are discussed and it is suggested that aerobic fermentation is caused by a severe reduction of site 1 of the respiratory chain region, whereas biomass formation is affected by repression of the terminal cytochrome a2. In comparing the effect of glucose on biomass formation at similar Qglucose levels aerobic and anaerobic fermentation, repression occurred in both cases at glucose concentrations of 0.3% and above. Although the analyses of 15 enzymes established the metabolic differences, the repression of growth was common to both fermentation types.

Purification, properties and immunological relationship of L (+)-lactate dehydrogenase from Lactobacillus casei.

The fructose-1,6-bisphosphate-activated L-lactate dehydrogenase (EC 1.1.1.27) from Lactobacillus casei ATCC 393 has been purified to homogenity by including affinity chromatography (cibacronblue-Sephadex-G-200) and preparative polyacrylamide gel electrophoresis into the purification procedures. The enzyme has an Mr of 132000-135000 with a subunit Mr of 34000. The pH optimum was found to be 5.4 insodium acetate buffer. Tris/maleate and citrate/phosphate buffers inhibited enzyme activity at this pH. The enzyme was completely inactivated by a temperature increase from 60 degrees C to 70 degrees C. Pyruvate saturation curves were sigmoidal in the absence of fructose 1,6-bisphosphate. In the presence of 20 muM fructose 1,6-bisphosphate a Km of 1.0 mM for pyruvate was obtained, whereas fructose 1,6-bisphosphate had no effect on the Km of 0.01 mM for NADH. The use of pyruvate analogues revealed two types of pyruvate binding sites, a catalytic and an effector site. The enzyme from L. casei appears to be subject to strict metabolic control, since ADP, ATP, dihydroxyacetone phosphate and 6-phosphogluconate are strong inhibitors. Immunodiffusion experiments with a rabbit antiserum to L. casei lactate dehydrogenase revealed that L. casei ATCC 393 L (+)-lactate dehydrogenase is probably not immunologically related to group D and group N streptococci. Of 24 lactic acid bacterial strains tested only 5 strains did cross-react: L. casei ATCC 393 = L. casei var. rhamnosus ATCC 7469 - L. casei var. alactosus NCDO 680 greater than L. casei UQM 95 greater than L. plantarum ATCC 14917.