Sakuma Takeyuki, Jinsiriwanit Siriwat, Hattori Toshihiro, Deshusses Marc A
Department of Chemical and Environmental Engineering, University of California, Riverside, CA 92521, USA.
Water Res. 2008 Nov;42(17):4507-13. doi: 10.1016/j.watres.2008.07.036. Epub 2008 Aug 7.
The removal of gaseous ammonia in a system consisting of a biotrickling filter, a denitrification reactor and a polishing bioreactor for the trickling liquid was investigated. The system allowed sustained treatment of ammonia while preventing biological inhibition by accumulating nitrate and nitrite and avoiding generation of contaminated water. All bioreactors were packed with cattle bone composite ceramics, a porous support with a large interfacial area. Excellent removal of ammonia gas was obtained. The critical loading ranged from 60 to 120 gm(-3)h(-1) depending on the conditions, and loadings below 56 gm(-3)h(-1) resulted in essentially complete removal of ammonia. In addition, concentrations of ammonia, nitrite, nitrate and COD in the recycle liquid of the inlet and outlet of each reactor were measured to determine the fate of nitrogen in the reactor, close nitrogen balances and calculate nitrogen to COD ratios. Ammonia absorption and nitrification occurred in the biotrickling filter; nitrate and nitrite were biologically removed in the denitrification reactor and excess dissolved COD and ammonia were treated in the polishing bioreactor. Overall, ammonia gas was very successfully removed in the bioreactor system and steady state operation with respect to nitrogen species was achieved.
研究了在一个由生物滴滤池、反硝化反应器和用于滴滤液的抛光生物反应器组成的系统中去除气态氨的情况。该系统能够持续处理氨,同时通过积累硝酸盐和亚硝酸盐防止生物抑制,并避免产生受污染的水。所有生物反应器都填充有牛骨复合陶瓷,这是一种具有大界面面积的多孔载体。获得了优异的氨气去除效果。根据条件不同,临界负荷范围为60至120 g m⁻³ h⁻¹,负荷低于56 g m⁻³ h⁻¹时可实现氨的基本完全去除。此外,测量每个反应器进出口循环液中氨、亚硝酸盐、硝酸盐和化学需氧量(COD)的浓度,以确定反应器中氮的去向、接近氮平衡并计算氮与COD的比率。氨的吸收和硝化在生物滴滤池中发生;硝酸盐和亚硝酸盐在反硝化反应器中被生物去除,过量的溶解COD和氨在抛光生物反应器中得到处理。总体而言,生物反应器系统中氨气去除非常成功,并且在氮物种方面实现了稳态运行。