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作 者:赵玉中[1,2] 师晓爽[1] 戴萌[1] 付善飞 许晓晖[1] 郭荣波[1]
机构地区:[1]山东省沼气工业化生产与利用工程实验室,中国科学院青岛生物能源与过程研究所,山东青岛266101 [2]中国科学院大学,北京100049
出 处:《可再生能源》2016年第4期621-627,共7页Renewable Energy Resources
基 金:国家自然科学基金项目(31101918,21307143,41276143);国家科技支撑计划课题(2013BAD22B03);中国科学院重点部署项目(KGCX2-EW-317);山东省重点研发计划(2015GSF115037)
摘 要:以模拟的城镇生活垃圾为底物,在发酵试验起始阶段向反应体系通入不同浓度氧气(0,5,10,20 m L O2/g VS),探究微氧处理对两相发酵联产氢气甲烷的影响。研究表明,通入5 m L O2/g VS的试验组获得了最高的氢气产量(72.23 m L/g VS),较未处理组提高了45.51%;虽然通入5 m L O2/g VS的试验组也获得了最高的甲烷产量(380.35 m L/g VS),但相比其他试验组并无明显提高。从整体来看,通入5 m L O2/g VS的试验组获得了最高的VS降解率(75.66%)和最高的能量回收率(72.76%),较未处理组分别提高了5.70%和5.33%。试验表明,适量的微氧处理(5 m L O2/g VS)可以提高城镇生活垃圾两相发酵联产氢气甲烷的产能效果。In order to investigate the effect of micro-aeration on the co-production of hydrogen and methane from domestic organic waste, different concentrations of oxygen(0,5,10,20 m L O2/g VS) were supplied at the initial stage of the two-phase fermentation. Results showed that the maximum hydrogen yield(72.23 m L/g VS)was obtained at the oxygen load of 5 m L/g VS, which was 45.51% higher than that of sample without micro-aeration. Though the maximum methane yield(380.35 m L/g VS) was also obtained at the oxygen load of 5 m L/g VS, it had no significant difference with other groups. Overall, the highest VS degradation rate(75.66%) and energy recovery rate(72.76%) were simultaneously obtained at the oxygen load of 5 m L/g VS, which were5.70% and 5.33% higher than those of sample without oxygen, respectively. Micro-aeration(5 m L O2/g VS) at the initial stage of the two-phase fermentation was an effective approach to improve the performance of the co-production of hydrogen and methane by the two-phase fermentation.
分 类 号:TK6[动力工程及工程热物理—生物能] S216.4[农业科学—农业机械化工程]
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