摘要：设计了一种气升式两相分配膜生物反应器,用于工业有机废气的净化处理,解决常见有机废气净化装置存在净化效率低、适用范围小以及尾气排放达不到较高标准要求等问题。采用多导流筒、低高径比和圆升气管的方形内循环式结构,进行装置的总体设计,并进行装置试运行,结果表明该装置简便易行,效率高,处理有机废气浓度广、无二次污染。

摘要：燃煤源汞是造成大气汞污染的重要原因。利用活性炭进行吸附脱汞是目前重点研究的汞污染控制技术。在通过管路将活性炭送入烟道的过程中,必须保证活性炭的量严格按照要求进行分配。文中通过理论分析与CFD数值模拟,考察了二叉树型管路、多叉树型管路和线型管路在活性炭均匀分配上的效果,并讨论了其应用的条件。研究认为,线型管路无论对连续相还是离散相都难以做到均匀分配;多叉树型管路(典型的如三叉树、四叉树)可以做到均匀分配,并且有一定的灵活性,最适宜在实际工业中应用;二叉树型管路只有在确保管路对称性的情况下才能得到较好的均分活性炭效果,且灵活性较差。此外研究还发现,活性炭颗粒在流场中的运动较为复杂,受包括时间在内的诸多参数影响,且管路非对称性对颗粒分布的影响大于其对流场分布的影响。如对均分的要求较为严格,须加装颗粒浓度实时监测装置与控制装置。

摘要：Toluene degradation performances were studied in a 10 L Two-Phase Partitioning Bioreactor(TPPB).The liquid phase consisted of a mixture of water and PDMS 50(Poly Di Methyl Siloxane,*** oil,viscosity of 46 m Pa·s) in the volume ratio of 75%/25%.Two series of experiments were carried out:in the first,the reactor was sequentially supplied with toluene whereas in the second,toluene was continuously *** sludge from the wastewater treatment plant of Beaurade(Rennes,France) was used at an initial concentration of 0.5 dry mass g·(mixture L)^(-1).The elimination capacity(EC) was investigated as well as the change in biomass concentration over *** biodegradation was very ef ficient(removal ef ficiency,RE=100%) for toluene flows ranging from 0.2 to 1.2 ml·h^(-1),corresponding to elimination capacities of up to 104 g·m^(-3)·h^(-1).For a toluene flow of 1.2 ml·h^(-1),the biomass concentration measured at the end of the experiment was 4.7 dry mass g·(mixture L)^(-1).The oxygen concentration in the liquid phase was clearly not a limiting factor in these operating *** on these results,an extrapolation leading to the design of a large-scale pilot TPPB can now be considered to study toluene degradation performances in industrial conditions.