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Post-treatment of effluents from anaerobic digesters by the Anammox process

机译:通过厌氧消化工艺对厌氧消化池的废水进行后处理

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The application of the Anammox process was studied under two different approaches for the post-treatment of anaerobic digester supernatants: two independent units, the combined SHARON-Anammox system, performed in a chemostate and a SBR, respectively, and, a single unit system composed by an air pulsing SBR to carry out the CANON process. The technology based on the combination of the SHARON-Anammox process was used to treat the effluent of an anaerobic digester from a fish canning industry. The presence of organic matter in the influent caused fluctuations in the efficiency of the SHARON unit and an optimal nitrite to ammonium ratio was not achieved in this system to feed the Anammox reactor. Nevertheless an overall percentage of nitrogen removal of 40-80% was obtained when the Anammox reactor operated at nitrite limited conditions. In those periods when the effluent from the SHARON unit contained a NO2--N/NH4+-N molar ratio higher than 1.3 the Anammox process lost its stability due to nitrite accumulation. The effluent from an anaerobic digester placed at a WWTP was treated by a CANON system operated at room temperature (20-24 degrees C). This system was developed from a nitrifying air pulsing reactor working at limiting dissolved oxygen conditions which was inoculated with Anammox biomass. A quick start-up of the system was observed and the reactor reached a nitrogen removal rate of 0.25 g N/(Ld) 40 days after inoculation. The maximum nitrogen removal rate reached 0.5 g N/(Ld). These results indicate the feasibility of the treatment of effluents from psychrophilic anaerobic digesters using the Anammox process.
机译:在两种不同的厌氧消化池上清液后处理方法中,研究了厌氧氨氧化工艺的应用:两个独立的单元,分别在化学部分和SBR中进行的SHARON-厌氧氨氧化系统组合,以及一个由单个单元组成的单系统通过空气脉冲SBR进行CANON处理。基于SHARON-Anammox工艺组合的技术用于处理鱼罐头行业厌氧消化池的废水。进水中有机物的存在引起SHARON装置效率的波动,并且在向Anammox反应器供料的该系统中未实现最佳的亚硝酸盐与铵之比。但是,当Anammox反应器在亚硝酸盐受限条件下运行时,脱氮总百分比为40-80%。在SHARON单元的出水中NO2--N / NH4 + -N摩尔比高于1.3的那些时期,Anammox工艺由于亚硝酸盐的积累而失去了稳定性。来自放置在污水处理厂的厌氧消化池的流出物通过在室温(20-24摄氏度)下运行的CANON系统进行处理。该系统是由硝化空气脉冲反应器开发的,该反应器在限制了溶解氧的条件下工作,并用Anammox生物质进行了接种。观察到系统快速启动,接种后40天,反应器的脱氮率达到0.25 g N /(Ld)。最大脱氮率达到0.5 g N /(Ld)。这些结果表明使用厌氧氨氧化工艺处理嗜酸性厌氧消化池废水的可行性。

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