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首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Recovery of phosphorus and nitrogen from alkaline hydrolysis supernatant of excess sludge by magnesium ammonium phosphate
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Recovery of phosphorus and nitrogen from alkaline hydrolysis supernatant of excess sludge by magnesium ammonium phosphate

机译:磷酸镁铵从过量污泥碱解上清液中回收磷和氮

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摘要

Magnesium ammonium phosphate (MAP) method was used to recover orthophosphate (PO_4~(3-)-P) and ammonium nitrogen (NH_4~+-N) from the alkaline hydrolysis supernatant of excess sludge. To reduce alkali consumption and decrease the pH of the supernatant, two-stage alkaline hydrolysis process (TSAHP) was designed. The results showed that the release efficiencies of PO_4~(3-)-P and NH_4~+-N were 41.96% and 7.78%, respectively, and the pH of the supernatant was below 10.5 under the running conditions with initial pH of 13, volume ratio (sludge dosage/water dosage) of 1.75 in second-stage alkaline hydrolysis reactor, 20 g/L of sludge concentration in first-stage alkaline hydrolysis reactor. The order of parameters influencing MAP reaction was analyzed and the optimized conditions of MAP reaction were predicted through the response surface methodology. The recovery rates of PO_4~(3-)-P and NH_4~+-N were 46.88% and 16.54%, respectively under the optimized conditions of Mg/P of 1.8, pH 9.7 and reaction time of 15 min.
机译:采用磷酸镁铵(MAP)法从剩余污泥的碱水解上清液中回收正磷酸盐(PO_4〜(3-)-P)和铵态氮(NH_4〜+ -N)。为了减少碱消耗并降低上清液的pH,设计了两阶段碱水解工艺(TSAHP)。结果表明:在初始pH值为13的条件下,PO_4〜(3-)-P和NH_4〜+ -N的释放效率分别为41.96%和7.78%,上清液的pH值低于10.5。第二阶段碱性水解反应器中的污泥体积比(污泥剂量/水剂量)为1.75,第一阶段碱性水解反应器中的污泥浓度为20 g / L。分析了影响MAP反应的参数顺序,并通过响应面法预测了MAP反应的最佳条件。在优化的Mg / P为1.8,pH为9.7和反应时间为15分钟的条件下,PO_4〜(3-)-P和NH_4〜+ -N的回收率分别为46.88%和16.54%。

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