Biotrickling filters
As shown in Figure 4.3, in many respects these represent an
intermediate tech-nology between biofilters and bioscrubbers, sharing certain
features of each. Once again, an engineered vessel holds a quantity of filter
medium, but in this case, it is an inert material, often clinker or slag. Being
highly resistant to compaction, this also provides a large number of void
spaces between particles and a high surface area relative to the overall volume
of the filter. The microbes form an attached growth biofilm on the surfaces of
the medium. The odourous air is again forced through the filter, while water
simultaneously recirculates through it, trickling down from the top, hence the
name. Thus a counter-current flow is established between the rising gas and the
falling water, as shown in the diagram, which improves the efficiency of
dissolution. The biofilm communities feed on substances in the solution passing
over them, biodegrading the constituents of the smell.
Process monitoring can be
achieved relatively simply by directly sampling the water recirculating within
the filter vessel. Process control is similarly straight-forward, since
appropriate additions to the circulating liquid can be made, as required, to
ensure an optimum internal environment for bacterial action. Though the
efficiency of the biotrickling filter is broadly similar to the previous
method, it can deal with higher concentrations of contaminant and has a
significantly smaller foot-print than a biofilter of the same throughput
capacity. However, as with almost all aspects of environmental biotechnology,
these advantages are obtained by means of additional engineering, the corollary
of which is, inevitably, higher capital and running costs.
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