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Acid Loading (acid + loading)
Selected AbstractsEffects of Sulfuric Acid Loading and Residence Time on the Composition of Sugarcane Bagasse Hydrolysate and Its Use as a Source of Xylose for Xylitol BioproductionBIOTECHNOLOGY PROGRESS, Issue 5 2005Silvio S. Silva A 22 full factorial design was employed to evaluate the effects of sulfuric acid loading and residence time on the composition of sugarcane bagasse hydrolysate obtained in a 250-L reactor. The acid loading and the residence time were varied from 70 to 130 mg acid per gram of dry bagasse and from 10 to 30 min, respectively, while the temperature (121 °C) and the bagasse loading (10%) were kept constant. Both the sulfuric acid loading and the residence time influenced the concentrations of xylose and inhibitors in the hydrolysate. The highest xylose concentration (22.71 g/L) was achieved when using an acid loading of 130 mg/g and a residence time of 30 min. These conditions also led to increased concentrations of inhibiting byproducts in the hydrolysate. All of the hydrolysates were vacuum-concentrated to increase the xylose concentration, detoxified by pH alteration and adsorption into activated charcoal, and used for xylitol bioproduction in a stirred tank reactor. Neither the least (70 mg/g, 10 min) nor the most severe (130 mg/g, 30 min) hydrolysis conditions led to the best xylitol production (37.5 g/L), productivity (0.85 g/L h), and yield (0.78 g/g). [source] Inorganic sulphate extraction from SO2 -impacted AndosolsEUROPEAN JOURNAL OF SOIL SCIENCE, Issue 1 2005T. Delfosse Summary Sulphate sorption on to the surface of short-range ordered minerals and precipitation of Al-hydroxy sulphate contribute to the acid neutralizing capacity of soils. The correct measurement of total inorganic sulphate is thus essential in soils that are accumulating SO42, anions. We extracted SO42, by various solutions, namely 0.005 m Ca(NO3)2, 0.016 m KH2PO4, 0.5 m NH4F and 0.2 m acidic NH4 -oxalate (pH 3), from Vitric and Eutric Andosols exposed to prolonged deposition of acid and SO2 from an active volcano (Masaya, Nicaragua). We attributed sulphate extractable by KH2PO4 (20,3030 mg kg,1) to anion-exchangeable SO42,, which was much smaller than NH4F- and oxalate-extractable SO42, (400,9680 and 410,10 480 mg kg,1, respectively). Our results suggest the occurrence of a sparingly soluble Al-hydroxy-mineral phase extractable by both NH4F and oxalate. The formation of Al-hydroxy minerals would result from the combination of enhanced weathering caused by strong acid loading and simultaneous occurrence of large SO42, concentrations in soil solution. Oxalate extracted slightly more inorganic SO42, than did NH4F, this additional amount of SO42, correlating strongly with oxalate-extractable Si and Fe contents. Preferential occlusion of SO42, by short-range ordered minerals, especially ferrihydrite, explains this behaviour. If we exclude the contribution of occluded sulphate then oxalate and NH4F mobilize similar amounts of SO42, and are believed to mobilize all of the inorganic SO42, pool. [source] Cell shrinkage evoked by Ca2+ -free solution in rat alveolar type II cells: Ca2+ regulation of Na+,H+ exchangeEXPERIMENTAL PHYSIOLOGY, Issue 2 2005Hitoshi Murao The effects of intracellular Ca2+ concentration, [Ca2+]i, on the volume of rat alveolar type II cells (AT-II cells) were examined. Perfusion with a Ca2+ -free solution induced shrinkage of the AT-II cell volume in the absence or presence of amiloride (1 ,m, an inhibitor of Na+ channels); however, it did not in the presence of 5-(N -methyl- N -isobutyl)-amiloride (MIA, an inhibitor of Na+,H+ exchange). MIA decreased the volume of AT-II cells. Inhibitors of Cl,,HCO3, exchange, 4,4,-diisothiocyanostilbene-2,2,-disulfonic acid (DIDS) and 4-acetamido-4,-isothiocyanatostilbene-2,2,-disulfonic acid (SITS) also decreased the volume of AT-II cells. This indicates that the cell shrinkage induced by a Ca2+ -free solution is caused by a decrease in NaCl influx via Na+,H+ exchange and Cl,,HCO3, exchange. Addition of ionomycin (1 ,m), in contrast, induced cell swelling when AT-II cells were pretreated with quinine and amiloride. This swelling of the AT-II cells is not detected in the presence of MIA. Intracellular pH (pHi) measurements demonstrated that the Ca2+ -free solution or MIA decreases pHi, and that ionomycin increases it. Ionomycin stimulated the pHi recovery after an acid loading (NH4+ pulse method), which was not noted in MIA-treated AT-II cells. Ionomycin increased [Ca2+]i in fura-2-loaded AT-II cells. In conclusion, the Na+,H+ exchange activities of AT-II cells, which maintain the volume and pHi, are regulated by [Ca2+]i. [source] Xylitol bioproduction from wheat straw: hemicellulose hydrolysis and hydrolyzate fermentationJOURNAL OF THE SCIENCE OF FOOD AND AGRICULTURE, Issue 9 2006Larissa Canilha Abstract A 22 central composite design with five center points was performed to estimate the effects of temperature (120, 130 and 140 °C) and acid loading (100, 150 and 200 mg g,1) on the yield of monomeric xylose recovery from wheat straw hemicellulose (YS/RM). Under the best hydrolysis condition (140 °C and 200 mg g,1), a YS/RM of 0.26 g g,1 was achieved. After vacuum concentration and detoxification by pH alteration and active charcoal adsorption, the hydrolyzate was used as source of xylose for xylitol bioproduction in a stirred tank reactor. A xylitol production of 30.8 g L,1 was achieved after 54 h,1 of fermentation, resulting in a productivity (QP) of 0.57 g L,1 h,1 and bioconversion yield (YP/S) of 0.88 g g,1. The maximum specific rates of xylose consumption and xylitol production were 0.19 and 0.15 g g,1 h,1, respectively. Copyright © 2006 Society of Chemical Industry [source] Effects of Sulfuric Acid Loading and Residence Time on the Composition of Sugarcane Bagasse Hydrolysate and Its Use as a Source of Xylose for Xylitol BioproductionBIOTECHNOLOGY PROGRESS, Issue 5 2005Silvio S. Silva A 22 full factorial design was employed to evaluate the effects of sulfuric acid loading and residence time on the composition of sugarcane bagasse hydrolysate obtained in a 250-L reactor. The acid loading and the residence time were varied from 70 to 130 mg acid per gram of dry bagasse and from 10 to 30 min, respectively, while the temperature (121 °C) and the bagasse loading (10%) were kept constant. Both the sulfuric acid loading and the residence time influenced the concentrations of xylose and inhibitors in the hydrolysate. The highest xylose concentration (22.71 g/L) was achieved when using an acid loading of 130 mg/g and a residence time of 30 min. These conditions also led to increased concentrations of inhibiting byproducts in the hydrolysate. All of the hydrolysates were vacuum-concentrated to increase the xylose concentration, detoxified by pH alteration and adsorption into activated charcoal, and used for xylitol bioproduction in a stirred tank reactor. Neither the least (70 mg/g, 10 min) nor the most severe (130 mg/g, 30 min) hydrolysis conditions led to the best xylitol production (37.5 g/L), productivity (0.85 g/L h), and yield (0.78 g/g). [source] | ||||||||||