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SIFT-MS analysis of the removal of dimethyl sulphide, n-hexane and toluene from waste air by a two phase partitioning bioreactor

机译:通过两相分配生物反应器从废气中去除二甲硫,正己烷和甲苯的SIFT-MS分析

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Dimethyl sulphide (DMS), n-hexane and toluene removal from a waste air was carried out by a two phase partitioning bioreactor (TPPR) containing a 25/75 vol/vol silicone oil/water emulsion inoculated with activated sludge under continuous feeding conditions. The performance of the reactor was determined using two different measuring techniques, GC-FID and SIFT-MS in order to determine the feasibility of the SIFT-MS as analytical technique. The linearity between both measurement techniques indicated that SIFT-MS can be used as a suitable alternative to determine the bioreactor performance. When feeding the TPPR only with hexane, elimination capacities (EC) of 139, 164 and 242 g m(-3) h(-1) are reached for an inlet load (IL) of 350 g m(-3) h(-1) at respectively 30, 60 and 120 s empty bed residence time (EBRT). If a mixture of DMS, hexane and toluene is fed to the bioreactor at an EBRT of 60 s EC of respectively 45, 45 and 75 g m(-3) h(-1) are reached for the different compound at an IL of 100 g m(-3) h(-1). This indicates that a TPPR can be applied to treat a mixture of hydrophobic and hydrophilic compounds. Excessive growth of biomass in a TPPR can lead to deteriorated aeration and a decrease in performance. By using pulse injections, the net retention time of the compounds could be determined online, which is related to the aeration and air distribution within the reactor. A low net retention time indicates bad aeration and air distribution, resulting in a low reactor performance. Therefore the net retention time can be used as a parameter indicating when biomass needs to be purged or when the aqueous medium needs to be refreshed. (C) 2016 Elsevier B.V. All rights reserved.
机译:通过两相分配生物反应器(TPPR)从二氧化硫(DMS),正己烷和甲苯中去除废气,该反应器包含在连续进料条件下接种了活性污泥的25/75体积/体积硅油/水乳液。为了确定SIFT-MS作为分析技术的可行性,使用两种不同的测量技术(GC-FID和SIFT-MS)确定了反应器的性能。两种测量技术之间的线性表明,SIFT-MS可用作确定生物反应器性能的合适替代方法。当仅使用己烷进料TPPR时,进口负荷(IL)为350 gm(-3)h(-1)时,消除能力(EC)为139、164和242 gm(-3)h(-1)空床停留时间分别为30、60和120 s(EBRT)。如果将DMS,己烷和甲苯的混合物以60 s的EBRT进料到生物反应器中,则不同化合物在IL为100 gm时分别达到45、45和75 gm(-3)h(-1)。 (-3)h(-1)。这表明TPPR可用于处理疏水和亲水化合物的混合物。 TPPR中生物量的过度生长会导致曝气恶化和性能下降。通过使用脉冲注入,可以在线确定化合物的净保留时间,这与反应器内的通气和空气分布有关。净保留时间短表明曝气和空气分配不良,导致反应堆性能低下。因此,净保留时间可以用作指示何时需要清除生物质或何时需要更新水性介质的参数。 (C)2016 Elsevier B.V.保留所有权利。

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