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Multicomponent Cellulase Production by Cellulomonas biazotea NCIM-2550 and Its Applications for Cellulosic Biohydrogen Production

机译:重氮纤维单胞菌NCIM-2550生产多组分纤维素酶及其在纤维素生物制氢中的应用

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Among four cellulolytic microorganisms examined, Cellulomonas biazotea NCIM-2550 can grow on various cellulosic substrates and produce reducing sugar. The activity of cellu-lases (endoglucanase, exoglucanase, and cellobiase), xylanase, amylase, and lignin class of enzymes produced by C. biazotea was mainly present extracellularly and the enzyme production was dependent on cellulosic substrates (carboxymethyl cellulose [CMC], sugarcane bagasse [SCB], and xylan) used for growth. Effects of physicochemical conditions on cellulolytic enzyme production were systematically investigated. Using MnCl2 as a metal additive significantly induces the cellulase enzyme system, resulting in more reducing sugar production. The efficiency of fermentative Conversion of the hydrolyzed SCB and xylan into clean H2 energy was examined with seven H2-producing pure bacterial isolates. Only Clostridium-butyricum CGS5 exhibited efficient H2 production performance with the hydrolysate of SCB and xylan. The cumulative H2 production and H2 yield from using bagasse hydrolysate (initial reducing sugar concentration = 1.545 g/L) were approximately 72.61 mL/L and 2.13 mmol H2/g reducing sugar (or 1.91 mmol H2/g cellulose), respectively. Using xylan hydrolysate (initial reducing sugar concentration = 0.345 g/L) as substrate could also attain a cumulative H2 production and H2 yield of 87.02 mL/L and 5.03 mmol H2/g reducing sugar (or 4.01 mmol H2/g cellulose), respectively.
机译:在所检查的四种纤维素分解微生物中,重氮纤维素纤维菌NCIM-2550可以在各种纤维素底物上生长并产生还原糖。重氮梭菌产生的纤维素酶(内切葡聚糖酶,外切葡聚糖酶和纤维二糖酶),木聚糖酶,淀粉酶和木质素类酶的活性主要存在于细胞外,并且酶的产生取决于纤维素底物(羧甲基纤维素[CMC],甘蔗)蔗渣[SCB]和木聚糖)用于生长。系统地研究了理化条件对纤维素分解酶产生的影响。使用MnCl2作为金属添加剂可显着诱导纤维素酶系统,从而导致更多的糖生产减少。用七个产氢的纯细菌分离株检测了水解后的SCB和木聚糖发酵转化为纯净氢气的效率。只有丁酸梭菌CGS5在SCB和木聚糖的水解产物中表现出有效的H2生产性能。使用甘蔗渣水解物(初始还原糖浓度= 1.545 g / L)产生的累积H2产量和H2产量分别约为72.61 mL / L和2.13 mmol H2 / g还原糖(或1.91 mmol H2 / g纤维素)。使用木聚糖水解产物(初始还原糖浓度= 0.345 g / L)作为底物,分别可以分别产生87.02 mL / L和5.03 mmol H2 / g还原糖(或4.01 mmol H2 / g纤维素)的累积H2产量和H2产量。 。

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