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Treatment of VOC Mixture in a Trickling-bed Air Biofilter Integrated with Cyclic Adsorption/Desorption Beds

机译:用循环吸附/解吸床一体化滴床空气生物过滤器的VOC混合物

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Biofiltration has emerged as a reliable and cost-effective technology for the control of volatile organic compounds (VOCs) emissions. However, fluctuations in concentration and variation in the waste air composition is commonly encountered in the chemical industry, which challenges the application of biofiltration technology. An integrated technology by coupling cyclic adsorption/desorption beds with a trickling-bed air biofilter was proposed and studied for contaminated air with single solute in our previous studies. The integrated system was found to be able to reduce concentration fluctuation and maintain long-term high removal efficiency. However, many industrial air emissions contain mixtures of VOCs that possess various physical and chemical properties affecting their biological treatment. Therefore, this study expands the application of the integrated technology to VOC mixture. Toluene, styrene, methyl ethyl ketone (MEK), and methyl isobutyl ketone (MIBK) were selected as the target VOCs in the mixture. The content for the four VOCs in the mixture is based on point source air emission in EPA 2003 toxic release report for chemical industries with the ratio of 0.448: 0.260: 0.234: 0.058 for toluene: styrene: MEK: MIBK, respectively. To compare the performance of the integrated system, the air stream was divided equally into two sub-air streams. One steam passed the 2-bed cyclic adsorption/desorption unit followed by Biofilter "A", and the other stream passed directly through the control system- a stand alone biofilter (Biofilter "B"). Square wave influent concentrations were employed on the integrated and control systems as fluctuating conditions. Backwashing once a week with duration of one hour was employed as the biomass control for both systems. Biofilter "A" maintained long-term 99% removal efficiency due to the effective dampening effect of the 2-bed cyclic adsorption/desorption unit. However, performance for Biofilter "B"fluctuated in removal performance according to the fluctuations in the feed.
机译:生物过滤已成为一个可靠和成本有效的技术挥发性有机化合物(VOC)的排放量的控制。然而,在废气成分的浓度和变化的波动在化工行业,其中生物过滤挑战技术的应用是经常遇到的。集成的技术,通过耦合用涓涓层空气循环生物滤池吸附/解吸床,提出并研究了在我们以往的研究单溶质污染的空气。集成的系统被认为是能够降低浓度波动和长期保持高去除效率。然而,许多工业废气排放含有具有影响其生物处理各种物理和化学性质VOC的混合物。因此,本研究扩展了集成技术,VOC混合物中的应用。甲苯,苯乙烯,甲基乙基酮(MEK),和甲基异丁基酮(MIBK)被选定为在混合物中的挥发性有机化合物的目标。分别MIBK,:用于在所述混合物中的四个的VOC含量是基于点源排放的空气在2003 EPA用于化学工业具有0.448的比有毒释放报告:对甲苯0.058::0.260:0.234苯乙烯:MEK。为了比较的集成系统的性能,气流等分成两个子气流。一个蒸汽通过了2床循环吸附/解吸单元随后生物滤池“A”,而另一个流直接通过控制系统 - 独立生物滤池(生物滤池“B”)通过。方波进水浓度对所用集成和控制系统波动的条件。每周一次用一小时时间反洗被用作用于两个系统生物量控制。生物滤池“A”长期保持99%的去除效率,由于2-床循环吸附/解吸单元的有效阻尼效果。然而,对于生物滤池“B”性能在去除性能根据原料中的波动波动。

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