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强化 Fenton 氧化法在制浆造纸废水处理中的应用。

Application of intensified Fenton oxidation to the treatment of sawmill wastewater.

机构信息

Ingenieria Quimica, Universidad Autonoma de Madrid, Crta. Colmenar km 15, 28049 Madrid, Spain.

Ingenieria Quimica, Universidad Autonoma de Madrid, Crta. Colmenar km 15, 28049 Madrid, Spain.

出版信息

Chemosphere. 2014 Aug;109:34-41. doi: 10.1016/j.chemosphere.2014.02.062. Epub 2014 Apr 5.

Abstract

The application of the Fenton process for the treatment of sawmill wastewater has been investigated. The sawmill wastewater was characterized by a moderate COD load (≈3gL(-1)), high ecotoxicity (≈ 40 toxicity units) and almost negligible BOD/COD ratio (5×10(-3)) due to the presence of different fungicides such as propiconazole and 3-iodo-2-propynyl butyl carbamate, being the wastewater classified as non-biodegradable. The effect of the key Fenton variables (temperature (50-120°C), catalyst concentration (25-100 mg L(-1) Fe(3+)), H2O2 dose (1 and 2 times the stoichiometric dose) and the mode of H2O2 addition) on COD reduction and mineralization was investigated in order to fulfill the allowable local limits for industrial wastewater discharge and achieve an efficient consumption of H2O2 in short reaction times (1h). Increasing the temperature clearly improved the oxidation rate and mineralization degree, achieving 60% COD reduction and 50% mineralization at 120°C after 1h with the stoichiometric H2O2 dose and 25 mg L(-1) Fe(3+). The distribution of H2O2 in multiple additions throughout the reaction time was clearly beneficial avoiding competitive scavenging reactions and thus, achieving higher efficiencies of H2O2 consumption (XCOD ≈ 80%). The main by-products were non-toxic short-chain organic acids (acetic, oxalic and formic). Thus, the application of the Fenton process allowed reaching the local limits for industrial wastewater discharge into local sewer system at a relatively low cost.

摘要

芬顿工艺在处理锯木厂废水中的应用已得到研究。由于存在不同的杀菌剂,如丙环唑和 3-碘-2-丙炔基丁基氨基甲酸酯,该锯木厂废水具有中等 COD 负荷(约 3g/L)、高生态毒性(约 40 毒性单位)和几乎可以忽略不计的 BOD/COD 比(5×10(-3)),废水被归类为不可生物降解。为了满足当地工业废水排放的允许限值,并在短反应时间内(1h)实现 H2O2 的有效消耗,研究了关键 Fenton 变量(温度(50-120°C)、催化剂浓度(25-100mg/LFe(3+))、H2O2 剂量(化学计量剂量的 1 和 2 倍)和 H2O2 添加方式)对 COD 去除和矿化的影响。提高温度明显提高了氧化速率和矿化程度,在 1h 内用化学计量 H2O2 剂量和 25mg/LFe(3+)达到 60%的 COD 去除率和 50%的矿化率。在整个反应时间内多次添加 H2O2 的分布显然是有益的,避免了竞争清除反应,从而实现了更高的 H2O2 消耗效率(XCOD ≈ 80%)。主要的副产物是无毒的短链有机酸(乙酸、草酸和甲酸)。因此,芬顿工艺的应用使得在相对较低的成本下达到了排入当地污水系统的工业废水当地排放标准。

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