首页> 外文期刊>Journal of Biotechnology >Separate production of hydrogen and methane from cassava wastewater with added cassava residue under a thermophilic temperature in relation to digestibility
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Separate production of hydrogen and methane from cassava wastewater with added cassava residue under a thermophilic temperature in relation to digestibility

机译:将Cassava废水中的氢气和甲烷分离,在嗜热温度下添加了木薯残留物,与消化率相关

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摘要

In this research, the separate production of hydrogen (H-2) and methane (CH4) from cassava wastewater with added cassava residue was investigated using a two-stage upflow anaerobic sludge blanket (UASB) system under thermophilic temperature (55 degrees C) in a continuous mode of operation and steady state condition. The two-stage UASB system was operated under an optimum chemical oxygen demand (COD) loading rate of 10.29 kg/m(3)d (based on the total volume of both bioreactors) of the cassava wastewater with different concentrations of added cassava residue. The recycle ratio of the effluent from the second bioreactor to the feed flow rate was fixed at 1:1 (v/v). In addition, the solution pH in the first bioreactor was controlled at 5.5, while that in the second bioreactor was not controlled. Under the optimum cassava residue concentration of 1200 mg/L, the produced gas from the first bioreactor contained 42.3% H-2, 55% carbon dioxide (CO2) and 2.70% CH4, while that from the second bioreactor contained 70.5% CH4, 28% CO2 and 1.5% H-2. Apart from a high H-2 and CH4 production performance (45.2 and 150% improvement, respectively, as compared to the system without added cassava residue) under the optimum cassava residue concentration (1200 mg/L) and the controlled COD loading rate (10.29 kg/m(3)d) of the cassava wastewater, the degradation performance of cellulose and hemicellulose were 41% and 22%, respectively, for the first bioreactor and 23% and 11%, respectively, for the second bioreactor. The digestibility of the cassava residue at thermophilic operation was higher than that at mesophilic temperature.
机译:在本研究中,使用两级上流厌氧厌氧污泥毯(UASB)系统在嗜热温度(55摄氏度)中,研究了来自Cassava废水的氢气(H-2)和甲烷(CH4)的氢气(H-2)和甲烷(CH 4),连续的操作模式和稳态条件。两阶段UASB系统在10.29kg / m(3)d(基于所述木薯废水的含有不同浓度的木薯残留物的Cassava废水的最佳化学需氧量(COD)加载速率下操作。从第二生物反应器到进料流速的流出物的再循环比固定在1:1(v / v)。另外,在5.5处控制第一生物反应器中的溶液pH,而不控制第二生物反应器中的溶液pH。在最佳的木薯残留浓度为1200mg / L的下,来自第一生物反应器的产生的气体含有42.3%H-2,55%二氧化碳(CO 2)和2.70%CH 4,而来自第二生物反应器含有70.5%CH4,28 %CO2和1.5%H-2。除了高温H-2和CH4生产性能(45.2和150%的改善),在最佳的木薯残基浓度(1200mg / L)和受控鳕鱼加载速率下Cassava废水的Kg / m(3)d),纤维素和半纤维素的降解性能分别为第二生物反应器分别为41%和22%,分别用于第二生物反应器,分别为23%和11%。在嗜热操作下的木薯残留物的消化率高于中抚化温度。

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