Van Nooten Thomas, Diels Ludo, Bastiaens Leen
Flemish Institute for Technological Research (VITO), Separation and Conversion Technologies, Boeretang 200, 2400 Mol, Belgium.
Environ Sci Technol. 2008 Dec 1;42(23):8890-5. doi: 10.1021/es801704t.
This study describes a laboratory-scale multifunctional permeable reactive barrier (multibarrier) for the removal of ammonium (NH4+: 313 +/- 51 mg N L(-1)), adsorbable organic halogens (AOX: 0.71 +/- 0.25 mg Cl L(-1)), chemical oxygen demand (COD: 389 +/- 36 mg L(-1)), and toxicity from leachate originating from a 40-year-old Belgian landfill. The complexity of the contamination required a sequential setup combining different reactive materials and removal processes. All target contaminants could be removed to levels below the regulatory discharge limits. Ammonium was efficiently removed in a first microbial nitrification compartment, which was equipped with diffusive oxygen emitters to ensure a sufficient oxygen supply. Ammonium was mainly oxidized to nitrite and to a lesser extent to nitrate, with an average mass recovery of 96%. Remaining ammonium concentrations could be further removed by ion exchange in a second compartment filled with clinoptilolite, exhibiting a total ammonium removal capacity of 46.7 mg N per g of clinoptilolite. Athird microbial denitrification compartment fed with sodium butyrate as a carbon source, was used to remove nitrate and nitrite formed in the first compartment. Maximum nitrification and denitrification rates at 12 degrees C indicated that hydraulic retention times of approximately 62 h and approximately 32 h were required in the columns to remove 400 mg N L(-1) by nitrification and denitrification, respectively. Leachate toxicity decreased to background levelstogetherwiththe removal of ammonium and its oxidation products. AOX and COD were efficiently removed by sorption in an additional compartment filled with granular activated carbon.
本研究描述了一种实验室规模的多功能渗透反应屏障(多屏障),用于去除来自一个有40年历史的比利时垃圾填埋场渗滤液中的铵(NH4+:313±51 mg N L(-1))、可吸附有机卤素(AOX:0.71±0.25 mg Cl L(-1))、化学需氧量(COD:389±36 mg L(-1))和毒性。污染物的复杂性要求采用一种结合不同反应材料和去除过程的顺序设置。所有目标污染物均可去除至低于监管排放限值的水平。铵在第一个微生物硝化隔室中被有效去除,该隔室配备了扩散式氧气发射器以确保充足的氧气供应。铵主要被氧化为亚硝酸盐,较少程度地氧化为硝酸盐,平均质量回收率为96%。剩余的铵浓度可在第二个填充斜发沸石的隔室中通过离子交换进一步去除,斜发沸石的总铵去除容量为每克46.7 mg N。第三个以丁酸钠作为碳源的微生物反硝化隔室用于去除在第一个隔室中形成的硝酸盐和亚硝酸盐。12℃时的最大硝化和反硝化速率表明,柱中通过硝化和反硝化分别去除400 mg N L(-1)所需的水力停留时间约为62 h和约32 h。随着铵及其氧化产物的去除,渗滤液毒性降至背景水平。AOX和COD在另一个填充颗粒活性炭的隔室中通过吸附被有效去除。