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Dioxins/Furans Distribution in the Unit Processes of Heat Exchangers and Bag Filters of Waste Incinerator System

机译:DIOXINS / FURANS分布在换热器系统的换热器和袋式过滤器的装置过程中

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Despite various studies, PCDDs/DFs behavior in MSWIs has been not well estimated because of complicated factors (operating conditions of incinerator, waste composition and flue gas treatment facilities). In this research, characteristic of dioxins behavior was investigated at unit processes after the boiler of MSWIs incinerator. In order to know PCDDs/DFs behavior, it is necessary to analyze experimental conditions of treatment facilities (temperature, flue gas flow rate, etc.) and incinerator operating conditions(furnace temperature, waste feeding rate, combustion gas flow rate, etc.) as well as the concentration of other air pollutants(SOx, NOx, CO, etc.) during PCDDs/DFs sampling period. The facilities were composed of Boiler for recovering heat, Cooling tower for decreasing temperature and Bag Filter for filtering Fly Ash, removing PCDDs/DFs and Acid Gas by injecting Activated Carbon + Ca(OH)_2. Flue gas was sampled at Boiler outlet, Bag Filter inlet and outlet coincidently. Ash samples were collected at Boiler, Cooling Tower, Bag Filter Hopper, respectively. The facilities were divided into two sections (Boiler + Cooling Tower, Bag Filter). Boiler and Cooling tower section showed a very similar behavior regardless of temperature variations. In contrast, PCDDs/DFs level through Bag Filter relatively increased specially in high-Chlorinated PCDDs/DFs. The result indicated that Low Chlorinated dioxins were removed in greater amount than High-Chlorinated dioxins at Bag filter section. Through Mass Balance Calculations extended over the Unit Processes, the release of PCDDs/DFs fro the incinerator had been also evaluated in terms of the total emission rate. Dioxins mass flux was calculated from concentrations measured in three solid residues of processes as well as in flue gases. In conclusion, the PCDDs/DFs concentration decreased consistently through Boiler + Cooling Tower +B/F in flue gases and increased in ashes, respectively. It would be considered that there exist some kinds of mechanism to increase PCDDs/DFs concentrations when flue gas passes both Cooling Tower and Bag Filter because of condensation and adsorption on the Fly Ash surface and memory effect.
机译:尽管各种研究,Mswis中的PCDDS / DFS行为由于复杂因素(焚烧炉,废物组成和烟气处理设施的运行条件)并未估计。在本研究中,在Mswis焚烧炉锅炉锅炉之后在单位过程中研究了二恶英行为的特征。为了了解PCDDS / DFS行为,有必要分析治疗设施的实验条件(温度,烟气流量等)和焚烧炉操作条件(炉温,废料率,燃烧气体流速等)以及在PCDDS / DFS采样期间的其他空气污染物(SOX,NOX,CO等)的浓度。该设施由锅炉组成,用于回收热量,冷却塔用于减少温度和袋式过滤器,用于过滤粉煤灰,通过注射活性炭+ Ca(OH)_2来除去PCDDS / DFS和酸气。在锅炉出口时采样烟气,袋式过滤器入口和出口。在锅炉,冷却塔,袋式过滤器料斗时收集灰样品。该设施分为两部分(锅炉+冷却塔,袋式过滤器)。锅炉和冷却塔部分显示出非常相似的行为,无论温度变化如何。相比之下,通过袋式滤波器的PCDDS / DFS级别在高氯化PCDDS / DF中相对增加。结果表明,在袋式过滤器部分的高氯化二恶英中除去低氯化二恶英。通过质量平衡计算在单元流程上扩展,PCDDS / DFS的释放来自焚烧炉的总排放率也在总排放率方面进行评估。二恶英质谱由在三种固体残留的方法以及烟道气中测量的浓度计算。总之,PCDDS / DFS浓度通过锅炉+冷却塔+ B / F一致地降低,分别在灰烬中增加。当烟气通过粉煤灰表面和记忆效果上的冷凝和吸附时,存在一些有些机制来增加PCDDS / DFS浓度的机制,以增加PCDDS / DFS浓度。

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