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Sequential hydrogen and methane coproduction from sugary wastewater treatment by 'CSTR_(Hyd)-UASB_(Met)' system

机译:“CSTR_(HYD)-UASB_(MET)”系统序列氢和甲烷泛段处理含糖废水处理

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Potentiality of sequential hydrogen bioproduction from sugary wastewater treatment was investigated using continuous stirred tank reactor (CSTR) for various substrate COD concentrations and HRTs. At optimum substrate concentration of 6 g COD/L, hydrogen could be efficiently produced from CSTR with the highest production rate of 3.00 (±0.04) L/L reactor d at HRT of 6 h. The up flow anaerobic sludge bed (UASB) reactor was used for continuous methane bioproduction from the effluents of hydrogen bioproduction. At optimal HRT 12 h, methane could be produced with a production rate of 2.27 (±0.08) L/L reactor d and the COD removal efficiency reached up to the maximum 82.3%.
机译:使用连续搅拌釜反应器(CSTR)对各种衬底COD浓度和HRT进行序列废水处理的序列氢生物制备的潜力。在最佳底物浓度为6g COD / L中,氢气可以从CSTR有效地产生3.00(±0.04)L / L反应器D的最高生产率为6小时。向上流动厌氧污泥床(UASB)反应器用于从氢生物生产的流出物中连续甲烷生物生产。在最佳HRT 12h时,可以产生2.27(±0.08)L / L反应器D的生产速率生产甲烷,COD去除效率达到最大值82.3%。

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