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作 者:张杰[1,2] 张艳辉[1] 李冬[1] 梁瑜海[1] 关宏伟[1] 赵世勋
机构地区:[1]水质科学与水环境恢复工程北京市重点实验室(北京工业大学),北京100124 [2]城市水资源与水环境国家重点实验室(哈尔滨工业大学),哈尔滨150090
出 处:《哈尔滨工业大学学报》2017年第2期1-5,共5页Journal of Harbin Institute of Technology
基 金:北京市长城学者项目;北京市市委组织部青年拔尖团队项目(2014000026833TD02)
摘 要:为探究不同厌氧运行方式对亚硝化恢复的影响,在常温(20±2)℃下,采用两组两级连续搅拌反应器(CSTR)1#和2#,实验分为S1、S2和S3三个阶段.在S1阶段1#采用厌氧/厌氧运行(两级DO均为0~0.1 mg/L),2#采用厌氧/好氧运行(两级DO分别为0~0.1和0.6~0.8 mg/L);在S2阶段1#转变为好氧/好氧运行(两级DO分别为0.2~0.4和0.6~0.8 mg/L),2#保持厌氧/好氧不变(两级DO分别为0~0.1和0.6~0.8 mg/L);在S3阶段,研究恢复后亚硝化的稳定性,此时1#、2#两级DO均为1.0~1.2 mg/L.分别对此过程中亚硝化的恢复时间以及恢复后稳定性进行比较.结果表明,1#的恢复时间比2#缩短了12 d,但当溶解氧增加到1.0~1.2 mg/L时,2#恢复后的亚硝化更稳定.先厌氧/厌氧(两级DO均为0~0.1 mg/L)后好氧/好氧运行(两级DO分别为0.2~0.4和0.6~0.8 mg/L),有利于亚硝化的快速恢复,恢复后转变为厌氧/好氧运行(两级DO分别为0~0.1和0.6~0.8 mg/L)有助于亚硝化的长期稳定运行.To investigate different effects of anaerobic modes on recovery of partial nitrification( PN),two-stage continuous stirred-tank reactors( CSTR) 1# and 2# were used at room temperature( 20±2) ℃. The experiment had three stages( S1,S2 and S3).During S1,1# was maintained anaerobic/anaerobic( DO: 0-0.1,0-0.1 mg/L),2# was maintained anaerobic/oxic( DO: 0-0.1,0.6-0.8 mg/L). During S2,1# was maintained oxic/oxic( DO: 0.2-0.4,0.6-0.8 mg/L),2#was continually maintained anaerobic/oxic( DO: 0-0.1,0.6-0.8 mg/L). To investigate stability of PN after recovery,S3 was carried out. During S3,1# and 2# was maintained oxic/oxic( DO: 1.0-1.2,1.0-1.2 mg/L) The following paremeters( time of recovery of PN and stability of PN) were investigated. It demonstrated that the recovery time of 1# was shorter than that of 2# by 12 d. However,PN in 2# was more stable when DO increased to 1.0-1.2 mg/L. Efficient PN could be recovered by the mode of first anaerobic/anaerobic( DO: 0- 0. 1,0- 0. 1 mg/L) then oxic/oxic( DO: 0. 2- 0. 4,0. 6-0.8 mg/L). Afterwards,stable PN could be maintained by anaerobic/oxic( DO: 0-0.1,0.6-0.8 mg/L).
关 键 词:生活污水 亚硝化 连续搅拌反应器 厌氧/厌氧 好氧/好氧 厌氧/好氧
分 类 号:X703.1[环境科学与工程—环境工程]
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