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Thermal oxidation treatment system of heat desorption gas extracted from soil contaminated with persistent organic pollutants

机译:热解吸气体热氧化处理系统从持久性有机污染物污染的土壤中提取

摘要

The present invention relates to a treatment system for removing persistent organic pollutants contained in soil discharged by treating persistent organic pollutants (dioxin) and steam as harmless gases through a thermal oxidation system, and condensation step (S10), oil Separation step (S20), heating step (S30), cooling step (S40), collecting step (S50), dust collecting step (S60), of cooling the gas by the latent heat of evaporated water by spraying water into the inside of the rapid cooling device, The white smoke reduction step (S70) proceeds sequentially to remove dioxin contained in the contaminated soil, convert it into a harmless gas, and discharge it, but in the condensation step (S10), the dioxin and moisture thermally desorbed from the soil are condensed in the form of extracted steam. When flowing into the condenser, the condensate is separated into gas, water, and condensed water containing oil, and discharged to a heating device and an oil-water separator, respectively.In the oil separation step (S20), the water from which the oil content of the condensed water stored in the oil-water separator is removed is an active adsorption tower. After discharged to the water treatment facility, the oil containing the dioxin component separated by the condenser is stored in an oil storage unit, and in the heating step (S30), gaseous dioxins volatilized and extracted from the soil and supplied from the oil storage unit Dioxins are removed by complete decomposition through a thermal oxidation process in which the oil component containing dioxin is sprayed into the heating device as fine particles, and caustic soda is used in the Wet Scrubber in which the collecting step (S50) is performed. Sodium hydroxide (caustic soda) required for neutralization through the tank is automatically injected according to the pH, and dioxin absorbs hydrogen chloride (HCL) gas generated after thermal oxidation and neutralizes it.In the dust collection step (S60), water is supplied to the upper water tank. A continuous water film type eczema electrostatic precipitator that flows evenly to the dust collecting electrode by the water film forming nozzle as the level rises and cools down by the dust collector, which is a continuous water film type eczema electrostatic precipitator. The dust is removed, and in the white smoke reduction step (S70), the high-temperature and high-humidity exhaust gas is transferred through the heat exchanger 2 using a white smoke reduction device. The wastewater additionally generated in the cooling step (S40), the dust collecting step (S60), and the white smoke reduction step (S70) is discharged to the outside by mitigating the white smoke phenomenon caused by the discharge of water vapor by mixing and discharging after heat exchange with outside air. It is recovered through (S42) and fed back to the heating step (S30) to completely remove dioxins that may be weakly contained in wastewater. A thermal oxidation treatment system for thermal desorption gas is proposed. Therefore, in the present invention, residual pollutants (dioxin) and water vapor extracted through thermal desorption are thermally oxidized at high temperature by heating, and through a rapid cooling process, collection and adsorption and wet electrostatic precipitating processes are performed, all residual dioxin and process by-products are removed. It works. In addition, by applying a rapid cooling device, the residence time in the temperature range in which dioxin is recombined is minimized, and even if a very small amount is recombined, there is an advantage that it can be completely removed through a wet electrostatic precipitator. In addition, the process gas finally discharged to the outside is heat-exchanged using a white smoke reduction device and then finally discharged, and energy efficiency is improved by applying a heat exchange device and a cooling water generating device in the cooling process of thermal oxidizing gas.
机译:本发明涉及通过通过热氧化系统治疗持久性有机污染物(二恶英)和蒸汽作为无害气体,通过热氧化系统处理持续有机污染物(DiOxin)和蒸汽,以及冷凝步骤(S10),油分离步骤(S20),加热步骤(S30),冷却步骤(S40),收集步骤(S50),通过将水喷射到快速冷却装置的内部,通过蒸发水的潜热来冷却气体的灰尘收集步骤(S60)。减少烟雾降低步骤(S70)顺序地进行以除去污染的土壤中含有的二恶英,将其转化为无害的气体,并放电,但在冷凝步骤(S10)中,从土壤中热解吸的二恶英和水分凝结提取的蒸汽的形式。当流入冷凝器时,冷凝物分别分离成气体,水和冷凝水,并分别排出到加热装置和油水分离器。在油分离步骤(S20)中,来自哪个水除去储存在油水分离器中的冷凝水的油含量是活性吸附塔。在排出到水处理设施之后,将含有冷凝器分离的二恶英组分的油储存在储油单元中,并在加热步骤(S30)中,气态二恶英从土壤中挥发并从储油单元中供应通过通过热氧化方法完全分解除去二恶英,其中将含有二恶英的油组分喷射到加热装置中作为细颗粒,并且在湿式洗涤器中使用苛性钠,其中进行收集步骤(S50)。通过罐中和所需的氢氧化钠(苛性钠)根据pH自动注射,并且Dioxin吸收热氧化后产生的氯化氢(HCl)气体并中和它。在灰尘收集步骤(S60)中,供应水。上水箱。连续水膜型湿疹静电除尘器通过水膜形成喷嘴均匀地流到集尘电极,随着水平的升高并通过集尘器冷却,其是连续的水膜式湿疹静电除尘器。除去灰尘,并且在白色烟雾降低步骤(S70)中,使用白色烟雾减少装置通过热交换器2传递高温和高湿度排气。在冷却步骤(S40)中另外产生的废水,灰尘收集步骤(S60)和白色烟雾还原步骤(S70)通过减轻通过混合和通过混合排出水蒸气引起的白色烟雾现象排出到外部与外部空气热交换后放电。它通过(S42)回收(S42)并反馈回加热步骤(S30)以完全除去可以弱含有废水中的二恶英。提出了一种热解吸气体的热氧化处理系统。因此,在本发明中,通过热解吸萃取的残余污染物(二恶英)和水蒸气通过加热在高温下热氧化,并通过快速冷却过程,收集和吸附和湿静电沉淀过程,所有残留的二恶英和处理副产品被删除。有用。另外,通过施加快速冷却装置,最小化二恶英重组的温度范围内的停留时间,并且即使重组非常少量,也可以通过湿式静电除尘器完全除去它。另外,使用白色烟雾减少装置热交换最终排出到外部的处理气体,然后通过在热氧化的冷却过程中施加热交换装置和冷却水发生装置来改善能量效率。气体。

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