Anaerobic bio-hydrogen production from ethanol fermentation: the role of pH

Hydrogen was produced by an ethanol-acetate fermentation at pH of 5.0 +/- 0.2 and HRT of 3 days. The yield of hydrogen was 100-200 ml g Glu(-1) with a hydrogen content of 25-40%. This fluctuation in the hydrogen yield was attributed to the formation of propionate and the activity of hydrogen utilizing methanogens. The change in the operational pH for the inhibition of this methanogenic activity induced a change in the main fermentation pathway. In this study, the main products were butyrate, ethanol and propionate, in the pH ranges 4.0-4.5, 4.5-5.0 and 5.0-6.0, respectively. However, the activity of all the microorganisms was inhibited below pH 4.0. Therefore, pH 4.0 was regarded as the operational limit for the anaerobic bio-hydrogen production process. These results indicate that the pH plays an important role in determining the type of anaerobic fermentation pathway in anaerobic bio-hydrogen processes.     

The effect of pH,temperature and sucrose concentration on high productivity continuous ethanol fermentation using Zymomonas mobilis

Summary A flocculent strain of Zymomonas mobilis was used for ethanol production from sucrose. Using a fermentor with cell recycle (internal and external settler) high sugar conversion and ethanol productivity were obtained. At a dilution rate of 0.5 h^-1 (giving 96% sugar conversion) the ethanol productivity, yield and concentrations respectively were 20 g/l/h, 0.45 g/g and 40 g/l using a medium containing 100 g/l sucrose. At a sucrose concentration of 150 g/l, the ethanol concentration reached 60 g/l. The ethanol yield was 80% theoretical due to levan and fructo-oligomer formation. No sorbitol was detected. This fermentation was conducted at a range of conditions from 30 to 36°C and from pH 4.0 to 5.5.     

Conditions for forming ethanol during bioconversion of cellulose-containing raw material

Several natural associations composed by thermophilic anaerobic bacteria capable of utilizing various cellulose materials at 60 +/- 2 degrees C and pH 6.0-7.0 were isolated from the sludge of Kamchatka geothermal springs. The rate of ethanol production (up to 1.7 g/l per day) and the concentration of ethanol in the medium (up to 1.2%), as well as the fermentation period (10-15 days) were determined under anaerobic conditions in the presence of cellulose, coniferous sawdust, newsprint, or paper pulp as a carbon source. Microorganisms were found that inhibited the production of ethanol. The initial pH value was found to influence both the ethanol production rate and ethanol/acetate ratio. A pH decrease from 7.0 to 5.0 led to 6.7-fold increased the ethanol production and caused a 23.8-fold increase in the ethanol/acetate ratio.     

Performance characteristics of a two-stage dark fermentative system producing hydrogen and methane continuously

The performance of a mesophilic two-stage system generating hydrogen and methane continuously from sucrose (10-30 g/L) was investigated. A hydrogen-generating CSTR followed by an upflow anaerobic filter were both inoculated with anaerobically digested sewage sludge, and ORP, pH, gas output, %H(2), %CH(4) and %CO(2) monitored. pH was controlled with NaOH, KOH or Ca(OH)(2). Using NaOH as alkali with 10 g/L sucrose, yields of 1.62 +/- 0.2 mol H(2)/mol hexose added and 323 mL CH(4)/gCOD added to the hydrogen and methane reactors respectively were achieved. The overall chemical oxygen demand (COD) reduction was 92.6% with 0.90 +/- 0.1 g/L sodium and 316 +/- 40 mg/L residual acetate in the methane reactor. Operation at 20 g/L sucrose and NaOH as alkali led to impaired volatile fatty acid (VFA) degradation in the methane reactor with 2.23 +/- 0.2 g/L sodium, 1,885 mg/L residual acetate, a hydrogen yield of 1.47 +/- 0.1 mol/mol hexose added, a methane yield of 294 mL/gCOD added and an overall COD reduction of 83%. Using Ca(OH)(2) as alkali with 20 g/L sucrose gave a hydrogen yield of 1.29 +/- 0.3 mol/mol hexose added, a methane yield of 337 mL/gCOD added and improved the overall COD reduction to 91% with residual acetate concentrations of 522 +/- 87 mg/L. Operation at 30 g/L sucrose with Ca(OH)(2) gave poorer overall COD reduction (68%), a hydrogen yield of 1.47 +/- 0.2 mol/mol hexose added, a methane yield of 138 mL/gCOD added and residual acetate 7,343 +/- 715 mg/L. It was shown that sodium toxicity and overloading are important issues for successful anaerobic digestion of effluent from biohydrogen reactors in high rate systems.     

Influence of substrate concentration on the stability and yield of continuous biohydrogen production

The effect of substrate concentration (sucrose) on the stability and yield of a continuous fermentative process producing hydrogen was studied. High substrate concentrations are attractive from an energy standpoint as they would minimise the energy required for heating. The reactor was a CSTR; temperature was maintained at 35 degrees C; pH was controlled between 5.2 and 5.3, and the hydraulic retention time (HRT) was 12 h. Online measurements were taken for ORP, pH, temperature, %CO2, gas output and %H2, and data logged using a MatLAB data acquisition toolbox. Steady-state operation was obtained at 10, 20 and 40 g/L of sucrose in the influent, but a subsequent step change to 50 g/L was unsustainable. The hydrogen content ranged between 50% and 60%. The yield of hydrogen decreased as the substrate concentration increased from 1.7 +/- 0.2 mol/mol hexose added at 10 g/L, to 0.8 +/- 0.1 mol/mol at 50 g/L. Sparging with nitrogen improved the hydrogen yield by at least 35% at 40 g/L and at least 33% at 50 g/L sucrose. Sparging also enabled steady-state operation at 50 g/L sucrose. Addition of an extra 4 g/L of n-butyric acid to the reactor operating at 40 g/L sucrose increased the butyrate concentration from 9,830 to 18,900 mg/L, immediately stopping gas production and initiating the production of propionate, whilst the addition of 2 g/L taking the butyrate concentration to 12,200 mg/L did not do so. It was shown that operation at 50 g/L sucrose in a CSTR in butyrate fermentation is possible.     

Medium components for shoot cultures of chlorophyll-deficient mutants of petunia inflata

Selected medium components were tested for 30 day growth promotion of shoot tips of Petunia inflata wild type, a cytoplasmic and a nuclear inherited chlorophyll-deficient mutant. Experiments were conducted independently with iron, sucrose, thiamine-HCl, indole-3-acetic acid (IAA), Kinetin (K), 6-benzylaminopurine (BA), coconut milk (CM), casein hydrolysate (CH), and plant extract (PE) an aqueous leaf extract, added to modified Murashige and Skoog (MS) salts and vitamins medium, and pH between 4.0 and 7.0 was also compared. The optimum concentrations of all test components were used to formulate revised MS media especially designed for in vitro shoot growth of chlorophyll-deficient petunia mutants. The optimum medium for the nuclear albino was: MS salts+1.5 mg/l thiamine-HCl+100 mg/l myo-inositol+3.5% sucrose+1% PE+5.0 mg/l IAA+0.3 mg/l K at pH 6.0; for the wild type: MS salts+0.6 mg/l thiamine-HCl+100 mg/l myo-inositol+4% sucrose+1.0 mg/l IAA+0.3 mg/l K at pH 5.0 and for the cytoplasmic albino: MS salts+0.4 mg/l thiamine-HCl+100 mg/l myo-inositol+4% sucrose+20% CM+3% PE+1.0 mg/l K at pH 5.0. On the revised MS media a 3-, 4- and 5- fold increase in 30 day plant fresh weight occurred for the nuclear, wild type and cytoplasmic chlorophyll-deficient plants, respectively.     

Optimization for growth of Rhodocyclus gelatinosus in seafood processing effluents

Tuna condensate was a better substrate than shrimp-blanching water or effluent from a frozen-seafood plant for growing Rhodocyclus gelatinosus under anaerobic conditions in the light. One strain out of four examined, R7, gave the highest biomass (4.0 g/l), cell yield (0.32 g cell/g COD), and COD removal (78%) in 1:10 (v/v) diluted tuna condensate. Shrimp-blanching water added to the tuna condensate further increased growth rate, biomass and COD removal. Optimal growth was at pH 7.0 and 3000 Lux light intensity. Acetate, pyruvate, glucose, glutamate, propionate or malate added to the tuna condensate did not increase cell yield, carotenoid or bacteriochlorophyll content or biomass protein. A maximum cell mass of 5.6 g/l (containing 50% protein) and 86% COD removal were obtained after 5 days' incubation under optimal conditions.     

芳香杯伞生物学特性及驯化栽培

以采自于河北省平泉市的一株野生食用菌Clitocybe fragrans的菌丝体为材料,对其营养及环境特性进行研究。检测了不同碳源、氮源、C/N、无机盐在固体培养条件下对芳香杯伞菌丝生长的影响,单因素及正交试验结果表明,实验范围内,芳香杯伞最适碳源为蔗糖、最适氮源为酵母浸粉、最适C/N为40:1、最适无机盐为硫酸镁。正交试验筛选适宜培养基配方为：蔗糖17.3 g,酵母浸粉1.8 g,磷酸二氢钾3 g,无水硫酸镁1.5 g,琼脂20 g,水1 L。对菌丝生长所需的温度、pH及光照条件进行研究,结果显示,适宜菌丝生长的温度范围为19–25℃,pH值范围为5–5.5,光照条件为黑暗。对获得的菌种进行了驯化栽培研究,结果表明,适宜的母种扩繁培养基为：粪草培养料100 g (煮汁),马铃薯200 g (煮汁),葡萄糖20 g,磷酸二氢钾3 g,蛋白胨3 g,无水硫酸镁1.5 g,琼脂20 g,水1 L;原种培养基为：高粱粒98%,葡萄糖1%,石膏1%;栽培培养基质为：粪草培养料98%,石膏1%,葡萄糖1%,含水量55%。栽培袋接菌后35–40 d满袋,8–10 d后现原基,7–8 d原基分化成子...     

Purification and characterisation of a fructosyltransferase from Rhodotorula sp

The present work was devoted to investigations concerning the purification and characterisation of the fructooligosaccharide (FOS)-producing extracellular enzyme of Rhodotorula sp. LEB-V10. FOS are functional food ingredients showing prebiotic properties, meaning that it could stimulate selectively the growth and/or activity of probiotic bacteria in the gut. The purification of the enzyme was carried out according to the following sequential procedure: cell separation by centrifugation, recovering by ethanol precipitation and purification by anion exchange chromatography. The molecular weight was estimated to be 170 kDa by preparative gel filtration and 77 kDa by sodium dodecyl sulphate-polyacrylamide gel electrophoresis, signifying that the native enzyme exists as a dimer. With sucrose as substrate, the data failed to fit the Michaelis-Menten behaviour, rather showing a sigmoid shape similar to that of the allosteric enzymes (cooperative behaviour), requiring high sucrose concentrations to obtain high reaction rates. The enzyme showed both fructofuranosidase (FA) and fructosyl-transferase (FTA) activities. The optimum pH and temperature for FA activity were found to be around 4.0 and 72-75 degrees C, respectively, while FTA showed optimum activity at pH 4.5 and 65-70 degrees C. Both activities were very stable at temperatures below 66 degrees C, while for FA, the enzyme was more stable at pH 4.0 and for FTA at pH 5.0.     

Effects of pH on feeding responses in the apple maggot fly,Rhagoletis pomonella (Diptera: Tephritidae)

Phagostimulatory effects of pH values of sucrose on Rhagoletis pomonella adults were studied in the laboratory. Flies were standardized for age, diet and food deprivation. Two presentation schemes were employed. The first varied pH value (3.0-10.0) with sucrose concentration kept constant at 40%. The second varied both sucrose concentration (8%, 24% and 40%) and pH value (5.0-8.0). Fly feeding propensity was evaluated by observation of fly acceptance or rejection of sucrose and duration of feeding. When tested on red wooden spheres treated with 40% sucrose, fly feeding acceptance was significantly greater when pH ranged from 5.0 to 8.0, and duration of feeding was significantly longer at pH 6.0-7.0. At pH /=8.0, feeding propensity was significantly reduced. Decrease in sucrose concentration significantly increased fly sensitivity to pH. Males were more responsive to varying pH than females. The sucrose pH shown to stimulate maximal feeding response was 6.4. Such information is relevant to formulation improvement of a coating mixture of sucrose and insecticide applied to red spheres as part of apple maggot fly control programs.     

The effect of pH and temperature manipulation on metabolite composition during acidogenesis in a hybrid anaerobic digester

Summary A synthetic medium containing 9 g/l sucrose was hydrolyzed in a novel hybrid reactor. A minimum hydraulic retention time (HRT) of 9.9 h, with a gas production rate of 1.07 m³/m³·d, was obtained without continuous neutralization. A viable anaerobic cell count of 10⁹ organisms/ml was obtained in the reactor fluid. The results showed that both pH and temperature significantly influenced the type and concentration of the various metabolites formed. These include ethanol, formic, acetic, propionic and butyric acids as primary metabolites and caproic acid as secondary metabolite. From the results obtained, it is suggested that to obtain the energetically most favourable products, a substrate pH of 6.5 and a temperature of 35°C must be used in anaerobic acidogenic digesters.     

Production of beta-fructofuranosidase with transfructosylating activity for fructooligosaccharides synthesis by Aspergillus japonicus NTU-1249.

Microbial beta-fructofuranosidases with transfructosylating activity can catalyze the transfructosylation of sucrose and synthesize fructooligosaccharides. Aspergillus japonicus NTU-1249 isolated from natural habitat was found to produce a significant amount of beta-fructofuranosidase with high transfructosylating activity and to have the potential for industrial production of fructooligosaccharides. In order to improve it's enzyme productivity, the medium composition and the cultivation conditions for A. japonicus NTU-1249 were studied. A. japonicus NTU-1249 can produce 83.5 units of transfructosylating activity per ml broth when cultivated in a shaking flask at 28 degrees C for 72 hours with a modified medium containing 80 g/l sucrose, 15 g/l soybean flour, 5 g/l yeast extract and 5 g/l NaCl at an initial pH of 6.0. The enzyme productivity was also optimized by submerged cultivation in a 5-litre jar fermentor with aeration at 1.5 vvm and agitation at 500 rpm. Under these operating conditions, the productivity of transfructosylating activity increased to 185.6 U/ml. Furthermore, the transfructosylating activity was improved to 256.1 U/ml in 1,000-litre pilot-scale fermentor. Enzymatic synthesis of fructooligosaccharides by beta-fructofuranosidase from A. japonicus NTU-1249 was performed in batch type by adding 5.6 units of transfructosylating activity per gram of sucrose to a 50% (w/v) sucrose solution at pH 5.0 and 50 degrees C. The yield of fructooligosaccharides was about 60% after reaction for 24 hours, and the syrup produced contained 29.8% (w/v) fructooligosaccharides, 15.2% (w/v) glucose and 5.0% (w/v) sucrose.     

Kinetics of improved extracellular beta-d-fructofuranosidase fructohydrolase production by a derepressed Saccharomyces cerevisiae

AIMS: beta-d-fructofuranosidase fructohydrolase (FFH, EC 3.2.1.26) is an enzyme which hydrolyses the alpha-1,4 glycosidic bonds of sucrose and releases monosaccharides. The present study deals with the kinetics of improved extracellular FFH production by Saccharomyces cerevisiae in batch culture. MATERIALS AND RESULTS: Strains of S. cerevisiae can show increased FFH activity when grown on chemically defined medium. In the present study, wild-culture S. cerevisiae GCB-IV was mutated by treatment with ethyl methane sulfonate (EMS). Among six yeast mutants, EMS-II was found to be the highest FFH-producing strain (51.46 +/- 2.4 U ml(-1)). Maximum FFH production (78.46 +/- 3.2 U ml(-1)) was obtained 48 h after incubation by this 2-deoxy-d-glucose (2dg)-resistant mutant (76.20 mg ml(-1) protein). The optimal concentration of sucrose, incubation period and initial pH were 30.0 g l(-1), 28 degrees C and 6.5, respectively. The mutant EMS-II showed improvement in FFH production when 5.0 g l(-1) urea was added as a sole nitrogen source into SAPY medium. Values for Q(p) (1.802 +/- 0.2 U ml(-1) h(-1)) and Y(p/s) (3.460 +/- 1.1 U g(-1)) of EMS-II were significantly improved over the other yeast strains. CONCLUSION: The E(a) value (40.28 +/- 3.5 kJ mol(-1)) of EMS-II was significant (P 相似文献   

Early postexercise muscle glycogen recovery is enhanced with a carbohydrate-protein supplement.

In the present study, we tested the hypothesis that a carbohydrate-protein (CHO-Pro) supplement would be more effective in the replenishment of muscle glycogen after exercise compared with a carbohydrate supplement of equal carbohydrate content (LCHO) or caloric equivalency (HCHO). After 2.5 +/- 0.1 h of intense cycling to deplete the muscle glycogen stores, subjects (n = 7) received, using a rank-ordered design, a CHO-Pro (80 g CHO, 28 g Pro, 6 g fat), LCHO (80 g CHO, 6 g fat), or HCHO (108 g CHO, 6 g fat) supplement immediately after exercise (10 min) and 2 h postexercise. Before exercise and during 4 h of recovery, muscle glycogen of the vastus lateralis was determined periodically by nuclear magnetic resonance spectroscopy. Exercise significantly reduced the muscle glycogen stores (final concentrations: 40.9 +/- 5.9 mmol/l CHO-Pro, 41.9 +/- 5.7 mmol/l HCHO, 40.7 +/- 5.0 mmol/l LCHO). After 240 min of recovery, muscle glycogen was significantly greater for the CHO-Pro treatment (88.8 +/- 4.4 mmol/l) when compared with the LCHO (70.0 +/- 4.0 mmol/l; P = 0.004) and HCHO (75.5 +/- 2.8 mmol/l; P = 0.013) treatments. Glycogen storage did not differ significantly between the LCHO and HCHO treatments. There were no significant differences in the plasma insulin responses among treatments, although plasma glucose was significantly lower during the CHO-Pro treatment. These results suggest that a CHO-Pro supplement is more effective for the rapid replenishment of muscle glycogen after exercise than a CHO supplement of equal CHO or caloric content.     

Oxygen binding and acid base status of the blood from the freshwater turtle, Phrynops hilarii

Oxygenation studies with the whole blood of Phrynops hilarii show a P50 of 38 torr at extracellular pH (pHe) of 7.4 which corresponds to an intracellular pH (pHi) of 7.05 at 25 degrees C. The blood CO2 Bohr effect was -0.56 when related to pHi. pHi is related to pHe by the following equation: pHi = 0.75.pHe + 1.54 (r = 0.99); pHi = 0.72. pHe + 1.72 (r = 0.96) at 10 and 25 degrees C respectively. Blood pHe, for 25 degrees C, was 7.519 +/- 0.254 (n = 6). Blood gas partial pressures were: pCO2 = 25.8 +/- 3.8 torr (n = 6); pO2 = 61.7 +/- 21.2 torr (n = 6). The major red cell phosphates, in mmole/l erythrocytes, n = 6, were: ATP (3.66 +/- 0.86); GTP (0.53 +/- 0.28); 2.3-DPG (0.32 +/- 0.12) and inorganic phosphates (2.00 +/- 0.35). The plasma inorganic ion composition, n = 6, was, in mEq/l: K+ (3.04 +/- 0.40); Na+ (148.4 +/- 12.6); Ca2+ (4.75 +/- 1.32); Cl- (106.6 +/- 5.0). Additional blood parameters of interest (n = 6) were: lactate (2.07 +/- 1.72 mM in plasma); erythrocytes/mm3 (416 X 10(3) +/- 4.6 X 10(3)); leucocytes/mm3 (44636 +/- 2618); haematocrit (%) (14.5 +/- 3.6); haemoglobin, g/dl (3.2 +/- 0.5); plasma protein g/dl (4.4 +/- 0.4); osmolarity (293 +/- 10 mOsm/l). The non-bicarbonate buffer value was -22.6 mmol/kg H2O/pH. For a constant CO2 content, delta pHe/delta t = 0.0141 +/- 0.002 (n = 18) and delta pHi/delta t = 0.0157 +/- 0.003 (n = 18).     

Dilute acid pretreatment, enzymatic saccharification, and fermentation of rice hulls to ethanol

Rice hulls, a complex lignocellulosic material with high lignin (15.38 +/- 0.2%) and ash (18.71 +/- 0.01%) content, contain 35.62 +/- 0.12% cellulose and 11.96 +/- 0.73% hemicellulose and has the potential to serve as a low-cost feedstock for production of ethanol. Dilute H2SO4 pretreatments at varied temperature (120-190 degrees C) and enzymatic saccharification (45 degrees C, pH 5.0) were evaluated for conversion of rice hull cellulose and hemicellulose to monomeric sugars. The maximum yield of monomeric sugars from rice hulls (15%, w/v) by dilute H2SO4 (1.0%, v/v) pretreatment and enzymatic saccharification (45 degrees C, pH 5.0, 72 h) using cellulase, beta-glucosidase, xylanase, esterase, and Tween 20 was 287 +/- 3 mg/g (60% yield based on total carbohydrate content). Under this condition, no furfural and hydroxymethyl furfural were produced. The yield of ethanol per L by the mixed sugar utilizing recombinant Escherichia colistrain FBR 5 from rice hull hydrolyzate containing 43.6 +/- 3.0 g fermentable sugars (glucose, 18.2 +/- 1.4 g; xylose, 21.4 +/- 1.1 g; arabinose, 2.4 +/- 0.3 g; galactose, 1.6 +/- 0.2 g) was 18.7 +/- 0.6 g (0.43 +/- 0.02 g/g sugars obtained; 0.13 +/- 0.01 g/g rice hulls) at pH 6.5 and 35 degrees C. Detoxification of the acid- and enzyme-treated rice hull hydrolyzate by overliming (pH 10.5, 90 degrees C, 30 min) reduced the time required for maximum ethanol production (17 +/- 0.2 g from 42.0 +/- 0.7 g sugars per L) by the E. coli strain from 64 to 39 h in the case of separate hydrolysis and fermentation and increased the maximum ethanol yield (per L) from 7.1 +/- 2.3 g in 140 h to 9.1 +/- 0.7 g in 112 h in the case of simultaneous saccharification and fermentation.     

Characterization of a Saccharomyces cerevisiae mutant with enhanced production of beta-D-fructofuranosidase

The present study focused on the improvement of Saccharomyces cerevisiae through random mutagenesis for enhanced production of beta-D-fructofuranosidase (FFase) using sucrose salt media. Sixty strains of S. cerevisiae were isolated from different fruits and soil samples and screened for FFase production. Enzyme productivity of different yeast isolates ranged from 0.03 to 1.10 U/ml. The isolate with the highest activity was subjected to ultraviolet (UV) radiation and mutagenesis using N-methyl N-nitro N-nitroso guanidine (MNNG). One mutant produced FFase at a level of 17.8+/-0.9 U/ml. The MNNG-treated isolate was exposed to ethyl methane sulphonate (EMS), and a mutant with an enzyme activity of 25.56+/-1.4 U/ml was obtained. Further exposure to UV radiation and chemicals yielded a mutant exhibiting an activity of 34.12+/-1.8 U/ml. After optimization of incubation time (48 h), sucrose concentration (5.0 g/L), initial pH (6.0) and inoculum size (2.0% v/v), enzyme production reached 45.65+/-4.6 U/ml with a noticeable greater than 40-fold increase compared to the wild-type culture. On the basis of kinetic variables, notably Q(p) (0.723+/-0.2U/g/h), Y(p/s) (2.036+/-0.05 U/g) and q(p) (0.091+/-0.02 U/g yeast cells/h), the mutant S. cerevisiae UME-2 was found to be a hyperproducer of FFase (LSD 0.054, p0.05).     

Purification and kinetic characterization of a fructosyltransferase from Aspergillus aculeatus

A fructosyltransferase present in Pectinex Ultra SP-L, a commercial enzyme preparation from Aspergillus aculeatus, was purified to 107-fold and further characterised. The enzyme was a dimeric glycoprotein (20% (w/w) carbohydrate content) with a molecular mass of around 135 kDa for the dimer. Optimal activity/stability was found in the pH range 5.0-7.0 and at 60 degrees C. It was stable or slightly activated (upto 1.4-fold) in the presence of reducing agents, such as dithiothreitol and 2-mercaptoethanol, and detergents, such as sodium dodecylsulphate and Tween 80. The enzyme was able to transfer fructosyl groups from sucrose as donor producing the corresponding series of fructooligosaccharides: 1-kestose, nystose and fructosylnystose. Using sucrose as substrate, the k(cat) and K(m) values for transfructosylating activity were 1.62+/-0.09 x 10(4)s(-1) and 0.53+/-0.05 M, whereas for hydrolytic activity the corresponding values were 775+/-25s(-1) and 27+/-3 mM. At elevated sucrose concentrations, the fructosyltransferase from A. aculeatus showed a high transferase/hydrolase ratio that confers it a great potential for the industrial production of prebiotic fructooligosaccharides.     

Fat metabolism and acute resistance exercise in trained men.

The purpose of this study was to investigate the effect of acute resistance exercise (RE) on lipolysis within adipose tissue and subsequent substrate oxidation to better understand how RE may contribute to improvements in body composition. Lipolysis and blood flow were measured in abdominal subcutaneous adipose tissue via microdialysis before, during, and for 5 h following whole body RE as well as on a nonexercise control day (C) in eight young (24 +/- 0.7 yr), active (>3 RE session/wk for at least 2 yr) male participants. Fat oxidation was measured immediately before and after RE via indirect calorimetry for 45 min. Dialysate glycerol concentration (an index of lipolysis) was higher during (RE: 200.4 +/- 38.6 vs. C: 112.4 +/- 13.1 micromol/l, 78% difference; P = 0.02) and immediately following RE (RE: 184 +/- 41 vs. C: 105 + 14.6 micromol/l, 75% difference; P = 0.03) compared with the same time period on the C day. Energy expenditure was elevated in the 45 min after RE compared with the same time period on the C day (RE: 104.4 +/- 6.0 vs. C: 94.5 +/- 4.0 kcal/h, 10.5% difference; P = 0.03). Respiratory exchange ratio was lower (RE: 0.71 +/- 0.004 vs. C: 0.85 +/- .03, 16.5% difference; P = 0.004) and fat oxidation was higher (RE: 10.2 +/- 0.8 vs. C: 5.0 +/- 1.0 g/h, 105% difference; P = 0.004) following RE compared with the same time period on the C day. Therefore, the mechanism behind RE contributing to improved body composition is in part due to enhanced abdominal subcutaneous adipose tissue lipolysis and improved whole body fat oxidation and energy expenditure in response to RE.     

Analysis and control of proteolysis of a fusion protein in Pichia pastoris fed-batch processes

A fusion protein composed of a cellulose-binding module (CBM) from Neocallimastix patriciarum cellulase 6A and lipase B from Candida antarctica (CALB), was produced by Pichia pastoris Mut(+) in high-cell density bioreactor cultures. The production was induced by switching from growth on glycerol to growth on methanol. The lipase activity in the culture supernatant increased at an almost constant rate up to a value corresponding to 1.3 g x l(-1) of CBM-CALB. However, only about 40% of the product was of full-length according to Western blot analysis. This loss was due to a cleavage of the protein in the linker between the CBM and the CALB moieties. The cleavage was catalyzed by serine proteases in the culture supernatant. The CALB-moiety was subjected to further slow degradation by cell-associated proteolysis. Different strategies were used to reduce the proteolysis. Previous efforts to shorten the linker region resulted in a stable protein but with ten times reduced product concentration in bioreactor cultures (Gustavsson et al. 2001, Protein Eng. 14, 711-715). Addition of rich medium for protease substrate competition had no effect on the proteolysis of CBM-CALB. The kinetics for the proteolytic reactions, with and without presence of cells were shown to be influenced by pH. The fastest reaction, cleavage in the linker, was substantially reduced at pH values below 5.0. Decreasing the pH from 5.0 to 4.0 in bioreactor cultures resulted in an increase of the fraction of full-length product from 40 to 90%. Further improvement was achieved by decreasing the temperature from 30 to 22 degrees C during the methanol feed phase. By combining the optimal pH and the low temperature almost all product (1.5 g x l(-1)) was obtained as full-length protein with a considerably higher purity in the culture supernatant compared with the original cultivation.