硫酸盐自由基高级氧化工艺 (SR-AOP) 同步去除垃圾渗滤液中难降解有机污染物和氨。

Sulfate radical-advanced oxidation process (SR-AOP) for simultaneous removal of refractory organic contaminants and ammonia in landfill leachate.

机构信息

Department of Earth and Environmental Studies, Montclair State University, Mallory Hall 252, 1 Normal Ave, Montclair, NJ 07043, USA.

出版信息

Water Res. 2011 Nov 15;45(18):6189-94. doi: 10.1016/j.watres.2011.09.015. Epub 2011 Sep 21.

Abstract

Typically, a mature landfill leachate contains high levels of non-biodegradable organics and ammonia nitrogen. Simultaneous removal of the both persistent leachate pollutants is a significant challenge. This paper reports the first scientific study to apply a sulfate radical (SO(4)(·-)) - based advanced oxidation process (SR-AOP) to treat a mature leachate, with an emphasis of concurrent removal of refractory organics and ammonia. In this study, all the experiments were run in a batch reactor with temperature control. In the thermal persulfate oxidation (TPO) process, persulfate (S(2)O(8)(2-)) was activated by heat to produce powerful oxidants, SO(4)(·-) (E(o) = 2.6 V). Three factors affecting the removal efficiencies of chemical oxygen demand (COD) and ammonia nitrogen were investigated, including initial solution pH (3-8.3), temperature (27-50 °C), and chemical dose (S(2)O(8)(2-):12COD(0) = 0.25-2.0). Typically, acidic pH (3-4), higher temperature, and higher dose favored the removal of COD and ammonia. At S(2)O(8)(2-):12COD(0) = 2 and 50 °C, the COD removal rates were 79% and 91% at pH 8.3 (no pH adjustment) and 4, respectively; and the ammonia nitrogen removal reached 100% at pH 8.3 or 4. SR-AOP appears to be more advantageous over hydroxyl radical (OH∙)-based advanced oxidation processes (HR-AOPs) because OH∙ almost does not oxidize ammonia. Furthermore, compared with Fenton treatment of the same batch leachate sample, the TPO could achieve a higher COD removal at an identical chemical dose. For example, COD removal was 40% at H(2)O(2):2.125COD(0) = 2 during Fenton treatment (pH 3), but 91% at S(2)O(8)(2-):12COD(0) = 2 during TPO (pH 4). These findings demonstrate that SR-AOP is a promising landfill leachate treatment method.

摘要

通常情况下,成熟的垃圾渗滤液中含有大量不可生物降解的有机物和氨氮。同时去除这两种持久性渗滤液污染物是一项重大挑战。本文报道了首例应用硫酸根自由基(SO(4)(·-))基高级氧化工艺(SR-AOP)处理成熟渗滤液的科学研究,重点是同时去除难降解有机物和氨氮。在这项研究中,所有实验均在带有温度控制的批式反应器中进行。在热过硫酸盐氧化(TPO)过程中,过硫酸盐(S(2)O(8)(2-))通过加热激活产生强氧化剂 SO(4)(·-)(E(o) = 2.6 V)。研究了三个影响化学需氧量(COD)和氨氮去除效率的因素,包括初始溶液 pH 值(3-8.3)、温度(27-50°C)和化学剂量(S(2)O(8)(2-):12COD(0) = 0.25-2.0)。通常情况下,酸性 pH 值(3-4)、较高的温度和较高的剂量有利于 COD 和氨氮的去除。在 S(2)O(8)(2-):12COD(0) = 2 和 50°C 时,pH 值为 8.3(无需 pH 调节)和 4 时的 COD 去除率分别为 79%和 91%;在 pH 值为 8.3 或 4 时,氨氮去除率达到 100%。与基于羟基自由基(OH∙)的高级氧化工艺(HR-AOPs)相比,SR-AOP 似乎更具优势,因为 OH∙几乎不氧化氨氮。此外,与相同批次渗滤液样品的芬顿处理相比,TPO 可以在相同的化学剂量下实现更高的 COD 去除率。例如,在芬顿处理(pH 3)时,H(2)O(2):2.125COD(0) = 2 时 COD 去除率为 40%,但在 TPO(pH 4)时 S(2)O(8)(2-):12COD(0) = 2 时 COD 去除率为 91%。这些发现表明,SR-AOP 是一种很有前途的垃圾渗滤液处理方法。

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