Baquerizo Guillermo, Maestre Juan P, Machado Vinicius C, Gamisans Xavier, Gabriel David
Department of Mining Engineering and Natural Resources, Universitat Politècnica de Catalunya, Bases de Manresa 61-73, Manresa, Spain.
Water Res. 2009 May;43(8):2293-301. doi: 10.1016/j.watres.2009.02.031. Epub 2009 Feb 28.
A comprehensive study of long-term ammonia removal in a biofilter packed with coconut fiber is presented under both steady-state and transient conditions. Low and high ammonia loads were applied to the reactor by varying the inlet ammonia concentration from 90 to 260 ppm(v) and gas contact times ranging from 20 to 36 s. Gas samples and leachate measurements were periodically analyzed and used for characterizing biofilter performance in terms of removal efficiency (RE) and elimination capacity (EC). Also, N fractions in the leachate were quantified to both identify the experimental rates of nitritation and nitratation and to determine the N leachate distribution. Results showed stratification in the biofilter activity and, thus, most of the NH(3) removal was performed in the lower part of the reactor. An average EC of 0.5 kg N-NH(3)m(-3)d(-1) was obtained for the whole reactor with a maximum local average EC of 1.7 kg N-NH(3)m(-3)d(-1). Leachate analyses showed that a ratio of 1:1 of ammonium and nitrate ions in the leachate was obtained throughout steady-state operation at low ammonia loads with similar values for nitritation and nitratation rates. Low nitratation rates during high ammonia load periods occurred because large amounts of ammonium and nitrite accumulated in the packed bed, thus causing inhibition episodes on nitrite-oxidizing bacteria due to free ammonia accumulation. Mass balances showed that 50% of the ammonia fed to the reactor was oxidized to either nitrite or nitrate and the rest was recovered as ammonium indicating that sorption processes play a fundamental role in the treatment of ammonia by biofiltration.
本文介绍了在稳态和瞬态条件下,对填充椰子纤维的生物滤池中氨的长期去除情况进行的综合研究。通过将进口氨浓度从90 ppm(v) 变化到260 ppm(v) 以及气体接触时间从20秒变化到36秒,向反应器施加低氨负荷和高氨负荷。定期分析气体样品和渗滤液测量结果,并用于根据去除效率(RE)和去除能力(EC)来表征生物滤池性能。此外,对渗滤液中的氮组分进行定量,以确定亚硝化和硝化的实验速率,并确定氮渗滤液分布。结果表明生物滤池活性存在分层现象,因此,大部分氨的去除在反应器下部进行。整个反应器的平均EC为0.5 kg N-NH₃m⁻³d⁻¹,最大局部平均EC为1.7 kg N-NH₃m⁻³d⁻¹。渗滤液分析表明,在低氨负荷的稳态运行过程中,渗滤液中铵离子和硝酸根离子的比例为1:1,亚硝化和硝化速率的值相似。在高氨负荷期间,硝化速率较低,这是因为大量铵和亚硝酸盐在填充床中积累,从而由于游离氨的积累对亚硝酸盐氧化细菌造成抑制。质量平衡表明,进入反应器的氨中有50%被氧化为亚硝酸盐或硝酸盐,其余以铵的形式回收,这表明吸附过程在生物过滤处理氨中起基本作用。