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作 者:饶坤[1] 谭小红[1] 黄安娜 严永红[1] 朱建林[1]
机构地区:[1]宁波大学建筑工程与环境学院,浙江宁波315211 [2]宁波开诚生态技术有限公司,浙江宁波315177
出 处:《中国给水排水》2014年第21期23-26,共4页China Water & Wastewater
基 金:"十二五"国家科技支撑计划项目(2012BAC25B05)
摘 要:利用两个容积为200L的反应器进行了餐厨垃圾废水半连续式二级串联中温[(35±2)℃]UASB厌氧处理试验,研究了第二级反应器的HRT对处理效果的影响。结果表明,在第一级UASB反应器对COD的去除率为85%、产气量为281.5—330.0L/d的基础上,第二级UASB反应器对COD的去除率仍可达15.5%~65%,产气量为35.8~102.7L/d,使得对COD的总去除率达到96%;第二级反应器的HRT=20d时,去除效果最稳定,而当HRT=15d时日产气量最高;第一级+UASB出水VFA/碱度值保持在0.29左右,第二级UASB出水VFA/碱度值在0.33~0.45之间,说明反应器具有较强的抗酸化缓冲能力。Anaerobic digestion of food wastewater was performed by employing two semi-continuous two-stage UASB reactors with effective volume of 200 L each under mesophilic condition (35 ± 2 ) ℃, and the influence of hydraulic retention time (HRT) of the second-stage reactor on the treatment efficien- cy was investigated. The results indicated that the COD removal efficiency and the biogas production of the first-stage UASB reactor were 85% and 281.5 to 330.0 L/d respectively, and those of the second- stage UASB reactor were 15.5% to 65% and 35.8 to 102.7 L/d respectively, making the total COD re- moval efficiency increased to nearly 96%. The system operated with the most stability while HRT of the second-stage reactor was 20 d, and the highest daily biogas production was achieved at HRT = 15 d. The VFA/basicity ratio of the effluent from the first-stage UASB reactor remained at around 0. 29, and that of the effluent from the second-stage UASB reactor maintained between 0.33 and 0.45, implying that the two-stage UASB system has a strong buffering capacity to resist acidification.
分 类 号:X703[环境科学与工程—环境工程]
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