首页> 外文会议>2011 International Symposium on Water Resource and Environmental Protection >Micro-aerobic granulation for actual coking wastewater treatment in an expanded granular sludge bed (EGSB) reactor: Intermittent oxygenation
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Micro-aerobic granulation for actual coking wastewater treatment in an expanded granular sludge bed (EGSB) reactor: Intermittent oxygenation

机译:微氧制粒法用于膨胀式颗粒污泥床(EGSB)反应器中实际焦化废水处理:间歇性充氧

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To accomplish rapidly the micro-aerobic granulation process of digestion sludge for the treatment of actual coking wastewater and meanwhile achieve high COD, the EGSB reactor was employed with two operation stages. Stage I: Granular sludge was formed from digestion sludge using brewery wastewater as substrate in the anaerobic way (meanwhile adding little granules, which were 1/7 of the total biomass). Stage II: Granular sludge was acclimatized with the actual coking wastewater through intermittent micro-oxygenation way of 800–20000ml·min−1 18–12 times at 20–60min intervals, 1h each time. The experimental results showed that the granular sludge could quickly form in 10d in the EGSB reactor seeded with digestion sludge and little loose granules. It took only about 6 months for the successful micro-aerobic acclimating of the granular sludge by the actual coking wastewater. With 631–1220mg·L−1 influent COD concentration, 1.0L·h−1 influent flow, 12h HRT, 20000ml.min−1 air flow and 3g·L−1 NaHCO3 supplement, the micro-aerobic EGSB reactor could have 75% high COD removal efficiency. The actual coking wastewater was not restrain the granules at the primary stage (at least for more than 1 month), but at 4 months, the SMA reduced 62.9% compared with the parallel, before treating CWW. The supplement of some oxygen and NaHCO3 was very important. Directly using the actual coking wastewater and through an intermittent oxygenation way was an effective acclimation approach.
机译:为了快速完成消化污泥的微好氧制粒工艺,以处理实际的焦化废水,同时达到较高的COD,采用了EGSB反应器的两个操作阶段。第一阶段:以啤酒废水为底物,以厌氧方式由消化污泥形成颗粒污泥(同时添加少量颗粒,占总生物量的1/7)。第二阶段:颗粒状污泥通过800–20000ml·min −1 的间歇微加氧方式,以20–60min的间隔,每次1h的方式适应实际的焦化废水。实验结果表明,在装有消化污泥和少量疏松颗粒的EGSB反应器中,污泥可在10天内迅速形成。实际的焦化废水仅用了大约6个月就成功地使颗粒污泥进行了微好氧驯化。进水COD浓度为631–1220mg·L -1 ,进水流量为1.0L·h -1 ,HRT为12h,20000ml.min -1 空气流量和3g·L −1 NaHCO 3 补充剂可以使微好氧EGSB反应器的COD去除率达到75%。实际的焦化废水在初始阶段(至少持续1个月以上)并没有限制颗粒,但是在处理CWW之前的4个月中,SMA降低了62.9%。补充一些氧气和NaHCO 3 非常重要。直接使用实际的焦化废水并通过间歇性的氧化方法是一种有效的适应方法。

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