Characteristics of TOC Treatment for Industrial Wastewater Treatment -Characteristics of Industrial Wastewater TOC Treatment Status and TOC Treatment by Ozone and Advanced Oxidation Process-

Kyeongjin Kim, Jeong-Pyo Jeon, I. Yeom
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Abstract

Objectives:As the organic pollutant indicator is changed from CODMn to TOC and the demand for TOC treatment of industrial wastewater increasing, the current situation of TOC treatment of wastewater discharge facilities of each industrial category is analyzed, and it is intended to consider the possibility of residual TOC treatment by ozone and advanced oxidation process.Methods:To review the TOC treatment situations of wastewater discharge facilities of each industrial category, the field survey data (46 sites) by Environment Ministry and Korea Environment Corporation were analyzed according to inflow TOC concentrations, direct/indirect discharge type, and main treatment process of wastewater treatment facilities. To review the characteristics of TOC treatment by ozone and advanced oxidation processes, previous studies and the results of field pilot tests conducted by ozone companies were comprehensively analyzed.Results and Discussion:The TOC treatment level varies depending on the inflow TOC concentrations to each industrial wastewater treatment facility, direct/indirect discharge type depending on the location of the wastewater treatment facilities, and the main treatment process of the wastewater treatment facility. In particular, the TOC removal rate differed by more than 20% depending on the presence or absence of biological treatment. The wastewater treatment facilities that require additional treatment of residual TOC were divided as follows (1) when the facility has biological treatment as main process, increasing unexpected inflow TOC load in treatment facilities or the condition of the biological treatment become worsen. (2) when the facility has phy-chemical treatment as main process, increasing unexpected inflow TOC load. (3) extending the replacement cycle of activated carbon to save maintenance cost. The advance oxidation process decomposes easily by OH radicals through the radical substitution of unsaturated hydrocarbons and aromatic compounds, so the removal rate of TOC by the O3+H2O2 advanced oxidation pilot test was 14.7~93.5%, higher than that of ozone oxidation. The specific ozone consumption per TOC removal amount (O3/ΔTOC) by O3+H2O2 advanced oxidation is 8.5~22.5mgO3/mgTOC, which is 1/5 of that of ozone oxidation only. In addition, comparing ozone demand by CODMn and TOC removal, ozone demand of O3+H2O2 advanced oxidation to remove TOC is 2.7 to 4.3 times compared to that by O3 oxidation to remove CODMn.Conclusion:In order to reduce residual TOC from industrial wastewater effluent, it is necessary to secure stability of the existing main treatment process in preparation for load fluctuations, and the technologies research on complex advanced oxidation processes, hybrid advanced oxidation processes, and pretreatment technology to reduce ozone demand is needed for economical field application.
工业废水TOC处理的特点-工业废水TOC处理现状及臭氧和深度氧化法处理TOC的特点
目的:随着有机污染物指标由CODMn改为TOC,以及对工业废水TOC处理需求的增加,分析了各工业类别废水排放设施的TOC处理现状,旨在考虑臭氧和深度氧化工艺处理残留TOC的可能性。方法:根据进水TOC浓度、直接/间接排放类型和污水处理设施的主要处理工艺,对环境部和韩国环境公司的现场调查数据(46个地点)进行分析,以回顾各工业类别污水排放设施的TOC处理情况。为了综述臭氧和高级氧化工艺处理TOC的特点,综合分析了以往的研究和臭氧公司进行的现场中试结果。结果与讨论:TOC处理水平因每个工业废水处理设施的进水TOC浓度、废水处理设施位置的直接/间接排放类型以及污水处理设施的主要处理工艺而异。特别地,TOC去除率相差超过20%,这取决于生物处理的存在或不存在。需要对残余TOC进行额外处理的废水处理设施分为以下几类:(1)当该设施以生物处理为主要工艺时,处理设施中的意外流入TOC负荷增加或生物处理条件恶化。(2) 当设施以物理化学处理为主要工艺时,增加了意外流入的TOC负荷。(3) 延长活性炭的更换周期以节省维护成本。高级氧化过程通过不饱和烃和芳香族化合物的自由基取代,容易被OH自由基分解,因此O3+H2O2高级氧化中试对TOC的去除率为14.7~93.5%,高于臭氧氧化。O3+H2O2深度氧化的单位TOC去除量臭氧消耗量(O3/ΔTOC)为8.5~22.5mgO3/mgTOC,仅为臭氧氧化的1/5。此外,比较CODMn和TOC去除的臭氧需求量,O3+H2O2深度氧化去除TOC的臭氧需求是O3氧化去除CODMn的2.7至4.3倍,需要对复杂高级氧化工艺、混合高级氧化工艺和预处理技术进行技术研究,以降低臭氧需求,实现经济的现场应用。
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