Lee D H, Lau A K, Pinder K L
Department of Chemical and Bio-Resource Engineering, University of British Columbia, Vancouver, Canada.
J Air Waste Manag Assoc. 2001 Jan;51(1):78-85. doi: 10.1080/10473289.2001.10464255.
Step tracer tests were carried out on lab-scale biofilters to determine the residence time distributions (RTDs) of gases passing through two types of biofilters: a standard biofilter with vertical gas flow and a modified biofilter with horizontal gas flow. Results were used to define the flow patterns in the reactors. "Non-ideal flow" indicates that the flow reactors did not behave like either type of ideal reactor: the perfectly stirred reactor [often called a "continuously stirred tank reactor" (CSTR)] or the plug-flow reactor. The horizontal biofilter with back-mixing was able to accommodate a shorter residence time without the usual requirement of greater biofilter surface area for increased biofiltration efficiency. Experimental results indicated that the first bed of the modified biofilter behaved like two CSTRs in series, while the second bed may be represented by two or three CSTRs in series. Because of the flow baffles used in the horizontal biofilter system, its performance was more similar to completely mixed systems, and hence, it could not be modeled as a plug-flow reactor. For the standard biofilter, the number of CSTRs was found to be between 2 and 9 depending on the airflow rate. In terms of NH3 removal efficiency and elimination capacity, the standard biofilter was not as good as the modified system; moreover, the second bed of the modified biofilter exhibited greater removal efficiency than the first bed. The elimination rate increased as biofilter load increased. An opposite trend was exhibited with respect to removal efficiency.
在实验室规模的生物滤池中进行了阶跃示踪剂试验,以确定通过两种类型生物滤池的气体的停留时间分布(RTD):一种是垂直气流的标准生物滤池,另一种是水平气流的改良生物滤池。结果用于确定反应器中的流动模式。“非理想流动”表明流动反应器的行为不像任何一种理想反应器:全混流反应器[通常称为“连续搅拌槽式反应器”(CSTR)]或平推流反应器。具有返混的水平生物滤池能够容纳更短的停留时间,而无需通常为提高生物过滤效率而增加生物滤池表面积的要求。实验结果表明,改良生物滤池的第一床表现得像两个串联的CSTR,而第二床可以用两个或三个串联的CSTR来表示。由于水平生物滤池系统中使用了导流板,其性能更类似于完全混合系统,因此,不能将其建模为平推流反应器。对于标准生物滤池,根据气流速率,发现CSTR的数量在2到9之间。在NH₃去除效率和去除容量方面,标准生物滤池不如改良系统;此外,改良生物滤池的第二床表现出比第一床更高的去除效率。去除速率随着生物滤池负荷的增加而增加。去除效率则呈现相反的趋势。