Green M, Denekamp N, Lahav O, Tarre S
Faculty of Agricultural Engineering, Technion-Israel Institute of Technology, Haifa.
Water Sci Technol. 2002;46(1-2):215-22.
The production of gaseous nitrogen compounds, particularly the greenhouse gas nitrous oxide, was investigated in a novel process for ammonium removal from wastewater. The process is based on the adsorption of ammonium on zeolite followed by bioregeneration. The zeolite serves the dual purpose of an ion exchanger and a physical carrier for nitrifying bacteria which bio-regenerate the ammonium saturated mineral. An analysis of the nitrifying population composition in the reactor fed with simulated secondary effluent (NH4+ = 50 mg/l) revealed that about half of the bacteria in the biofilm were common ammonium oxidizers Nitrosococcus mobilis and Nitrosomonas, while the other half were nitrite oxidizers. The amount of nitrogen losses, under different conditions, and the identification of the emitted gases (N2 or N2O) were investigated in two sets of experiments: (I) batch experiments using biomass originating from the ion exchange reactor with and without the addition of nitrite, and (II) continuous experiments using the ion exchange reactor with zeolite as the biomass carrier. In the batch experiments, nitrite and oxygen concentrations were determined as the major parameters responsible for the formation of gaseous nitrogen gas during ammonia oxidation by autotrophic bacteria. Continuous experiments showed that the major parameter significantly affecting nitrogen losses was the amount of ammonium adsorbed by the zeolite during the ion exchange phase. The amount of ammonium adsorbed determines the ammonium concentration during the initial period of bioregeneration, which in turn directly influences oxygen demand and the resulting concentrations of oxygen and nitrite. It was concluded that the formation of nitrogen gas compounds in the ion exchange/bioregeneration process can be eliminated by adjusting the operational regime to have a shorter adsorption phase resulting in smaller amounts of ammonium adsorbed per cycle.
在一种从废水中去除铵的新工艺中,对气态氮化合物(特别是温室气体一氧化二氮)的产生进行了研究。该工艺基于铵在沸石上的吸附,随后进行生物再生。沸石兼具离子交换剂和硝化细菌物理载体的双重作用,硝化细菌对铵饱和的矿物进行生物再生。对以模拟二级出水(NH4+ = 50 mg/l)为进水的反应器中的硝化菌群组成进行分析后发现,生物膜中约一半的细菌是常见的铵氧化菌,如运动亚硝化球菌和亚硝化单胞菌,而另一半是亚硝酸盐氧化菌。在两组实验中研究了不同条件下的氮损失量以及排放气体(N2或N2O)的鉴定:(I)使用来自离子交换反应器的生物质进行的批次实验,添加和不添加亚硝酸盐;(II)使用以沸石为生物质载体的离子交换反应器进行的连续实验。在批次实验中,确定亚硝酸盐和氧气浓度是自养细菌氨氧化过程中气态氮气形成的主要参数。连续实验表明,显著影响氮损失的主要参数是离子交换阶段沸石吸附的铵量。吸附的铵量决定了生物再生初期的铵浓度,进而直接影响需氧量以及由此产生的氧气和亚硝酸盐浓度。得出的结论是,通过调整操作方式以缩短吸附阶段,从而使每个循环吸附的铵量减少,可以消除离子交换/生物再生过程中氮气化合物的形成。