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Effect of ozonation on activated sludge from pulp and paper industry

机译:臭氧化对制浆造纸业活性污泥的影响

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Aerobic biological treatment with activated sludge is the predominant process all over the worldnfor treatment of pulp and paper industry wastewater. 50–70% of the biodegradable organicnmaterial is oxidized to CO2 and the rest is converted to bacterial biomass, typically termed asnexcess sludge or waste activated sludge (WAS). Handling and disposal of WAS in general and innparticular from the pulp and paper industry face different processing difficulties, regulatorynstringency due to organochlorine contamination and reluctance of people for reuse. With annobjective of reducing the net disposable biomass, ozonation of WAS from a pulp and paper millnand from a laboratory scale batch activated sludge process operated with the wastewater andnbacterial seed of the same pulp and paper mill have been carried out. With the mill sludge havingnpredominant filamentous organisms 18% MLSS was reduced at an ozone dosage of 55mg O3/gndry MLSS solid (DS) resulting in 2.5 times COD increase. With the laboratory sludge which is wellnstructured and flocculating, only 6% MLSS was reduced at an ozone dosage of 55mg O3/g DS.nOzonation mineralizes 26% and 20% AOX compounds embedded in the secondary sludge in thenmill and laboratory sludge respectively at an ozone dosage of 55mg O3/g DS. During ozonation,nabsorbed/adsorbed lignin on biomass was released which resulted in increased colournconcentration. Ozonation can be a potential oxidative pretreatment process for reducing the WASnand paving the way for cost effective overall treatment of WAS.
机译:用活性污泥进行好氧生物处理是世界范围内处理制浆造纸工业废水的主要方法。 50-70%的可生物降解有机材料被氧化为CO2,其余的则转化为细菌生物质,通常称为厌氧污泥或废物活性污泥(WAS)。制浆和造纸行业中,特别是制浆业普遍和特别是WAS的处理和处置面临着不同的加工困难,由于有机氯污染导致的监管严格性以及人们不愿重复使用。为了减少净的一次性生物量,已经进行了纸浆和造纸厂的WAS的臭氧化,以及用同一纸浆和造纸厂的废水和细菌种子操作的实验室规模的间歇活性污泥法的臭氧化。在工厂污泥中主要存在丝状生物的情况下,臭氧剂量为55mg O3 / gndry MLSS固体(DS)时,MLSS减少了18%,导致COD增加了2.5倍。实验室污泥经过良好结构化和絮凝后,在臭氧剂量为55mg O3 / g DS的情况下,仅6%的MLSS减少了.nOzonation会在臭氧中将26%和20%的AOX化合物矿化,然后分别埋藏在二级污泥中。剂量为55mg O3 / g DS。在臭氧化过程中,生物质上吸附的/吸附的木质素被释放出来,导致色度浓度增加。臭氧化可能是减少WASn的潜在氧化预处理工艺,并为经济有效的WAS整体处理铺平了道路。

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