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Development of Biological Livestock Wastewater Treatment System Combined with Physical Pretreatment and Chemical Posttreatment

机译:物理预处理与化学后处理相结合的生物畜禽污水处理系统的开发

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Lab-scale livestock wastewater treatment process was operated. Treatment process was composed of anaerobic reactor, aerobic reactor, anoxic reactor, settler, and microorganisms activation reactor. We divided this system into Systems 1–5 according to various conditions. In Systems 4 and 5, ammonia stripping was performed as pretreatment. And flocculation was performed as posttreatment. Average influent concentrations of COD, BOD, TKN, and TP were 21,894, 11,533, 2255, and 415 mg/L, respectively, and COD/N and BOD/N ratios in influent were 9.9 and 5.3, respectively. When ammonia stripping was performed as pretreatment, effluent BOD concentration was 44.4 mg/L and removal efficiency was 99.62%. TN removal efficiencies in Systems 4 and 5 were 84.1 and 95.2%, respectively, and effluent TN concentrations were 305.9 and 78.4 mg/L, respectively, which was because of with/without pH control. In operation period of Systems 4 and 5, average SNR and SDNR were 18.6 and 17.4 g N/kg MLSS/d, respectively, which was rate as much as endogenous denitrification rate because of long SRT due to low F/M ratio. In Systems 3, 4, and 5, optimal doses of flocculation agent were 350, 100, and 100 mgFe/L. This difference was caused by alkalinities of Systems 3, 4, and 5, which were 750, 284, and 162 mg/L as CaCO_3.
机译:实验室规模的牲畜废水处理工艺得以运行。处理过程由厌氧反应器,好氧反应器,缺氧反应器,沉降器和微生物活化反应器组成。我们根据各种条件将此系统分为系统1-5。在系统4和5中,氨汽提是作为预处理进行的。并进行絮凝作为后处理。 COD,BOD,TKN和TP的平均进水浓度分别为21,894、11,533、2255和415 mg / L,进水的COD / N和BOD / N之比分别为9.9和5.3。当进行氨汽提作为预处理时,出水BOD浓度为44.4 mg / L,去除效率为99.62%。系统4和5中TN的去除效率分别为84.1%和95.2%,出水TN浓度分别为305.9和78.4 mg / L,这是因为有/无pH控制。在系统4和5的运行期间,平均SNR和SDNR分别为18.6 g N / kg MLSS / d,这与内源反硝化率相当,这是由于低的F / M比导致SRT较长。在系统3、4和5中,絮凝剂的最佳剂量为350、100和100 mgFe / L。这种差异是由于系统3、4和5的碱度(CaCO_3为750、284和162 mg / L)引起的。

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