School of Sustainable Engineering and Built Environment, Ira A. Fulton Schools of Engineering, Arizona State University, 501 E. Tyler Mall, ECG 252, Tempe, AZ 85287-5306, USA.
Water Res. 2013 Mar 15;47(4):1596-603. doi: 10.1016/j.watres.2012.12.021. Epub 2012 Dec 26.
Granular activated carbon (GAC) can remove trace organic pollutants and natural organic matter (NOM) from industrial and municipal waters. This paper evaluates an iron nanocatalyst approach, based on Fenton-like oxidation reactions, to regenerate spent GAC within a packed bed configuration after saturation by organic compounds. Specifically, we focus on regenerating GAC packed beds equilibrated with varying influent concentrations of phenol, a model organic compound. Iron nanocatalysts were synthesized using ferric chloride, a chemical already used as a coagulant at municipal WTPs, and reacted with hydrogen peroxide (H(2)O(2)) for the purpose of in-situ regeneration. Up to 95% of phenol adsorption capacity was regenerated for GAC equilibrated with 1000 mg/L of phenol. Using this technique, at least four adsorption-regeneration cycles can be performed sequentially for the same batch of GAC with fresh iron nanocatalysts while achieving a regeneration efficiency of 90 ± 5% between each loading. Moreover, the iron nanocatalyst can be recovered and reused multiple times. Lower initial adsorbate concentrations (10-500 mg/L) resulted in a slightly lower saturated adsorbent-phase concentration of phenol and lower regeneration efficiencies (72 ± 5%). Additionally, this catalytic in-situ regeneration was applied to GAC saturated by NOM. A slightly lower regeneration efficiency (60%) was observed for the Suwannee River NOM adsorption capacity of GAC. The next step is validation in a pilot-scale test that applies this regeneration technique to a GAC adsorber employed in NOM removal.
颗粒状活性炭(GAC)可以去除工业和市政用水中的痕量有机污染物和天然有机物(NOM)。本文评估了一种基于芬顿类氧化反应的铁纳米催化剂方法,用于在有机化合物饱和后,在填充床配置中再生已饱和的 GAC。具体来说,我们专注于再生用不同浓度的苯酚平衡的 GAC 填充床,苯酚是一种模型有机化合物。铁纳米催化剂是使用氯化铁合成的,氯化铁已经作为市政水处理厂的混凝剂使用,并用过氧化氢(H(2)O(2))进行反应,目的是进行原位再生。对于用 1000mg/L 苯酚平衡的 GAC,可再生高达 95%的苯酚吸附容量。使用该技术,至少可以连续进行四次吸附-再生循环,对于同一批 GAC,使用新鲜的铁纳米催化剂,每次加载之间可实现 90±5%的再生效率。此外,铁纳米催化剂可以多次回收和重复使用。较低的初始吸附质浓度(10-500mg/L)导致苯酚的饱和吸附相浓度略低,再生效率略低(72±5%)。此外,这种催化原位再生应用于被 NOM 饱和的 GAC。对于 GAC 对苏万尼河 NOM 的吸附容量,观察到略低的再生效率(60%)。下一步是在中试规模试验中验证,该试验将这种再生技术应用于用于去除 NOM 的 GAC 吸附剂。