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The sensitivity of fixed-bed biological perchlorate removal to changes in operating conditions and water quality characteristics

机译:固定床生物去除高氯酸盐对操作条件和水质特征变化的敏感性

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Flow rate, electron donor addition, and biomass control were evaluated in order to optimize perchlorate (ClO_4~-) removal from drinking water using biologically active carbon (BAC) filtration. Influent dissolved oxygen (DO) was lowered from ambient conditions to approximately 2.5mg/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 50μg/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 18μg/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 6.7μg/L. Within 24 h of reactivating the electron donor, the filter regained its capacity to consistently remove 50μg/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 300μg/L, influent sulfate concentrations between 0 and 220 mg/L, influent pH values of 6.5-9.0, and operating temperatures of 5-22℃.
机译: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(ClO_4-)的效率,对流速,电子供体的添加和生物质控制进行了评估。对于所有使用氮气喷射的实验,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0-2.0 mg / L时,需要乙酸盐或乙醇碳1.6-2.8 mg / L才能达到并维持BAC过滤器中50μg/ L高氯酸盐的完全去除。在生物过滤过程中,大部分或全部外源乙酸盐和乙醇被去除。当模拟72小时电子给体进料失败时,观察到最大高氯酸盐突破量为18μg/ L,一旦重新应用电子给体,则需要9天才能完全清除高氯酸盐。在24小时电子给体进料故障模拟中,检测到的最大流出高氯酸盐浓度为6.7μg/ L。在重新激活电子供体的24小时内,过滤器恢复了其始终如一地去除50μg/ L高氯酸盐的能力,使其低于检测值。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,但清洁程序立即恢复了稳定,完全的高氯酸盐去除。当进水DO浓度为2.5 mg / L时,大约每50天(4800床体积)需要执行一次清洁程序。空床接触时间(EBCT)实验表明,使用5分钟的EBCT可达到80%的高氯酸盐去除率,而对于9分钟的EBCT,可观察到完全去除高氯酸盐。还证明了BAC过滤始终去除高氯酸盐,直到进水浓度在10至300μg/ L,进水硫酸盐浓度在0至220 mg / L之间,进水pH值在6.5-9.0之间,工作温度为5到检测以下。 22℃。

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