Brown Jess C, Snoeyink Vernon L, Raskin Lutgarde, Lin Richard
Department of Civil and Environmental Engineering, University of Illinois at Urbana-Champaign, Urbana, IL 61801, USA.
Water Res. 2003 Jan;37(1):206-14. doi: 10.1016/s0043-1354(02)00243-9.
Flow rate, electron donor addition, and biomass control were evaluated in order to optimize perchlorate (ClO4-) removal from drinking water using biologically active carbon (BAC) filtration. Influent dissolved oxygen (DO) was lowered from ambient conditions to approximately 2.5 mg/L for all experiments using a nitrogen sparge. When influent nitrate concentration was 0-2.0 mg/L, 1.6-2.8 mg/L as carbon of acetate or ethanol was required to achieve and sustain the complete removal of 50 microg/L perchlorate in a BAC filter. Most or all of the exogenous acetate and ethanol was removed during biofiltration. When a 72-h electron donor feed failure was simulated, a maximum perchlorate breakthrough of 18 microg/L was observed and, once electron donor was reapplied, 9 days were required to reestablish complete perchlorate removal. During a 24-h electron donor feed failure simulation, the maximum effluent perchlorate concentration detected was 6.7 microg/L. Within 24 h of reactivating the electron donor, the filter regained its capacity to consistently remove 50 microg/L perchlorate to below detection. Although biomass growth diminished the filter's ability to consistently remove perchlorate, a cleaning procedure immediately restored stable, complete perchlorate removal. This cleaning procedure was required approximately every 50 days (4800 bed volumes) when influent DO concentration was 2.5 mg/L. Empty-bed contact time (EBCT) experiments showed that 80% perchlorate removal was achieved using a 5-min EBCT, and complete perchlorate removal was observed for an EBCT of 9 min. It was also demonstrated that BAC filtration consistently removed perchlorate to below detection for influent perchlorate concentrations ranging from 10 to 300 microg/L, influent sulfate concentrations between 0 and 220 mg/L, influent pH values of 6.5-9.0, and operating temperatures of 5-22 degrees C.
为了优化使用生物活性炭(BAC)过滤从饮用水中去除高氯酸盐(ClO4-)的效果,对流速、电子供体添加量和生物量控制进行了评估。在所有实验中,通过氮气鼓泡将进水溶解氧(DO)从环境条件降低至约2.5mg/L。当进水硝酸盐浓度为0-2.0mg/L时,需要1.6-2.8mg/L(以碳计)的乙酸盐或乙醇才能在BAC过滤器中实现并维持50μg/L高氯酸盐的完全去除。生物过滤过程中大部分或全部外源乙酸盐和乙醇被去除。当模拟72小时电子供体进料中断时,观察到高氯酸盐的最大穿透量为18μg/L,一旦重新添加电子供体,需要9天才能重新建立高氯酸盐的完全去除。在模拟24小时电子供体进料中断期间,检测到的最大出水高氯酸盐浓度为6.7μg/L。在重新激活电子供体后的24小时内,过滤器恢复了将50μg/L高氯酸盐持续去除至检测限以下的能力。尽管生物量的增长降低了过滤器持续去除高氯酸盐的能力,但通过清洗程序可立即恢复稳定、完全的高氯酸盐去除效果。当进水DO浓度为2.5mg/L时,大约每50天(4800床体积)需要进行一次此清洗程序。空床接触时间(EBCT)实验表明,使用5分钟的EBCT可实现80%的高氯酸盐去除率,当EBCT为9分钟时可观察到高氯酸盐的完全去除。还证明,对于进水高氯酸盐浓度为10-300μg/L、进水硫酸盐浓度为0-220mg/L、进水pH值为6.5-9.0以及操作温度为5-22℃的情况,BAC过滤可将高氯酸盐持续去除至检测限以下。