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Process design for nitrogen removal using nitrifying biofilm and denitrifying suspended growth in a biofilm airlift suspension reactor

机译:在生物膜气提悬浮反应器中使用硝化生物膜和反硝化悬浮物脱氮的工艺设计

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Operation of a Biofilm Airlift Suspension (BAS) reactor was possible with nitrifying biofilm growth and heterotrophic suspended growth, simultaneously converting ammonium and acetate. Control of the location of heterotrophic growth, either in suspension or in layers over the nitrifying biofilms, was established by manipulation of the hydraulic retention time. Two process configurations (based on the BAS reactor) are identified, for nitrogen removal from wastewater by integration of nitrification in biofilms and denitrification in suspension. The first set-up consists of a conventional nitrifying BAS reactor, coupled with a suspended biomass reactor (without biomass retention). The second process configuration is a single BAS reactor which is sequentially aerated and non-aerated, by cyclically recirculating the offgas. Process design schemes for these configurations are presented and the design aspects are evaluated. Three limiting processes are identified: gas-liquid oxygen transfer, the hydraulic capacity of the settler and the minimal time needed for oxygen depletion of the gas phase during offgas recirculation. It was found that the two-reactor configuration is mainly suitable for pre-treatment of concentrated ammonia containing wastewaters. The one-reactor configuration can be applied to obtain low nitrogen concentrations in the effluent.
机译:生物膜空运悬浮(BAS)反应器的运行可以使生物膜硝化和异养悬浮生长,同时转化铵和乙酸盐。通过控制水力停留时间,可以控制硝化生物膜悬浮或成层的异养生长的位置。确定了两种工艺配置(基于BAS反应器),用于通过将生物膜中的硝化作用与悬浮液中的反硝化作用结合来从废水中去除氮。第一个装置由一个常规的硝化BAS反应器和一个悬浮的生物质反应器(无生物质保留)组成。第二种工艺配置是单个BAS反应器,该反应器通过循环再循环废气依次进行充气和不充气。提出了针对这些配置的过程设计方案,并对设计方面进行了评估。确定了三个限制过程:气液氧转移,沉降器的水力容量以及废气再循环期间气相耗氧所需的最短时间。发现两反应器配置主要适用于浓氨水的预处理。可以采用单反应器配置以获得流出物中的低氮浓度。

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