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PROCESS CONTROL AND DESIGN CONSIDERATIONS FOR METHANOL-INDUCED DENITRIFICATION IN A SEQUENCING BATCH REACTOR

机译:间歇式反应器中甲醇诱导的脱硝过程控制与设计注意事项

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The primary goal of this research was to determine the effect of methanol-induced denitrification on volatile suspended solids production, settleability, and oxidation-reduction potential in a full-scale sequencing batch reactor. Batch tests were also conducted to determine the influence of mixing and acclimatization on the denitrification of wastewater with methanol. The observed sludge production in the full-scale sequencing batch reactor with methanol addition was 0.21 kg volatile suspended solids l~(-1) methanol, versus the calculated stoichiometric sludge production of 0.17 kg volatile suspended solids l~(-1) methanol. The settleability in the full-scale sequencing batch reactor, measured by the sludge volume index, increases linearly with increasing denitrification rate. The total change in the oxidation-reduction potential magnitude during a sequencing batch reactor cycle increased linearly with increasing denitrification rate. A minimum of 55% increase in the denitrification rate was observed in a batch reactor with methanol addition and a sludge acclimatized to methanol addition, compared to a batch reactor with methanol addition and a non-acclimatized sludge. The non-acclimatized batch reactor had a negligible denitrification rate without methanol addition. However, significant denitrification rates were observed in the acclimatized batch reactors without methanol addition, potentially caused by microbial storage or an increased population of denitrifiers that scavenge any available carbon. A completely mixed batch reactor, with sludge acclimatized to methanol addition during the anoxic cycle, had an increase in the denitrification rate ranging from 660%, without methanol addition, to 200%, with a methanol dosage of 12.7 mg l~(-1), compared to the unmixed batch reactor with an acclimatized sludge. Therefore, mixing appears to be critical to the denitrification process, to realize the best kinetic performance.
机译:这项研究的主要目的是确定甲醇诱导的反硝化对全规模测序间歇反应器中挥发性悬浮固体产生,沉降性和氧化还原电位的影响。还进行了分批测试,以确定混合和驯化对废水与甲醇反硝化的影响。在加入甲醇的全规模测序间歇反应器中观察到的污泥产量为0.21 kg挥发性悬浮固体l〜(-1)甲醇,而计算出的化学计量污泥产量为0.17 kg挥发性悬浮固体l〜(-1)甲醇。通过污泥体积指数测得的全规模测序间歇反应器中的沉降性随反硝化速率的增加而线性增加。在顺序批反应器循环中,氧化还原电位的总变化随反硝化速率的增加而线性增加。与添加甲醇和未驯化的污泥的间歇反应器相比,在添加甲醇和使污泥适应甲醇的间歇反应器中,反硝化率至少增加了55%。未经驯化的间歇式反应器在不添加甲醇的情况下反硝化率可忽略不计。然而,在不添加甲醇的适应的间歇式反应器中观察到明显的反硝化速率,这可能是由于微生物存储或清除任何可用碳的反硝化剂种群增加所致。一个完全混合的间歇式反应器,其中的污泥在缺氧循环中能适应甲醇的添加,其反硝化率的增加范围从660%(不添加甲醇)到200%(甲醇用量为12.7 mg l〜(-1))。 ,与具有适应性污泥的未混合间歇式反应器相比。因此,混合对于实现最佳的动力学性能似乎对于脱氮过程至关重要。

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