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移动床生物膜反应器处理实际煤气化废水中的硝化抑制和恢复。

Inhibition and recovery of nitrification in treating real coal gasification wastewater with moving bed biofilm reactor.

机构信息

State Key Laboratory of Urban Water Resources and Environment, Harbin Institute of Technology, Harbin 150090, China.

出版信息

J Environ Sci (China). 2011;23(4):568-74. doi: 10.1016/s1001-0742(10)60449-4.

Abstract

Moving bed biofilm reactor (MBBR) was used to treat real coal gasification wastewater. Nitrification of the MBBR was inhibited almost completely during start-up period. Sudden increase of influent total NH3 concentration was the main factor inducing nitrification inhibition. Increasing DO concentration in the bulk liquid (from 2 to 3 mg/L) had little effect on nitrification recovery. Nitrification of the MBBR recovered partially by the addition of nitrifying sludge into the reactor and almost ceased within 5 days. Nitrification ratio of the MBBR achieved 65% within 12 days by increasing dilute ratio of the influent wastewater with tap water. The ratio of nitrification decreased to 25% when influent COD concentration increased from 650 to 1000 mg/L after nitrification recovery and recovered 70% for another 4 days.

摘要

移动床生物膜反应器(MBBR)用于处理实际的煤气化废水。在启动期间,MBBR 的硝化作用几乎完全受到抑制。进水总 NH3 浓度的突然增加是导致硝化抑制的主要因素。增加主体液体中的 DO 浓度(从 2 增加到 3mg/L)对硝化恢复几乎没有影响。通过向反应器中添加硝化污泥,MBBR 的硝化作用部分恢复,但在 5 天内几乎停止。通过用自来水增加进水的稀释比,硝化恢复后,MBBR 的硝化率在 12 天内达到 65%。当进水 COD 浓度从 650mg/L 增加到 1000mg/L 时,硝化比下降到 25%,硝化恢复 70%,又持续了 4 天。

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