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Performance evaluation of hybrid reactor for bio filtration of n-hexane–styrene mixture

机译:混合反应器生物过滤正己烷-苯乙烯混合物的性能评估

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摘要

Bio filtration of n-hexane and styrene mixture is always a difficult and challenging process due to the hydrophobicity and recalcitrant nature of the components. In this research study, a novel nano composite based adsorber was employed as the pre-treatment stage before biofilter to treat the VOC mixture. The hybrid reactor yielded better results compared to the stand alone biofilter. The concentration range employed in this study was 0.5-2.0 g m(-3) for n-hexane and 0.25-1.0 g m(-3) for styrene. Higher removal efficiencies were achieved at lower inlet concentrations at maximum EBRT of 90 s. Styrene removal efficiencies were found to be better than n-hexane removal efficiencies. The comparison between hybrid model and conventional biofilter proved the superior performance of the hybrid model. The carbon dioxide production was found to be proportional to the degradation rate represented in terms of elimination capacity. The correlation was proposed and actual yield coefficient was found to be lesser than the theoretical value. Biomass growth was studied across the height of the biofilter and found to be appreciable in the lower sections.
机译:由于组分的疏水性和难降解性,正己烷和苯乙烯混合物的生物过滤始终是一个困难而富挑战性的过程。在这项研究中,一种新型的基于纳米复合材料的吸附剂被用作生物滤池处理VOC混合物之前的预处理阶段。与独立式生物滤池相比,混合反应器产生了更好的结果。在这项研究中使用的浓度范围为正己烷为0.5-2.0 g m(-3),苯乙烯为0.25-1.0 g m(-3)。在最大EBRT为90 s的情况下,在较低的入口浓度下实现了更高的去除效率。发现苯乙烯的去除效率优于正己烷的去除效率。混合模型与常规生物滤池的比较证明了混合模型的优越性能。发现二氧化碳产生与以消除能力表示的降解速率成比例。提出了相关性,发现实际屈服系数小于理论值。研究了生物滤池整个高度的生物量增长,并在下部发现了可观的增长。

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