Article ID Journal Published Year Pages File Type
150370 Chemical Engineering Journal 2012 8 Pages PDF
Abstract

A novel mesoscale helical baffled design of oscillatory baffled reactor (OBR) has been constructed and characterised in the net flow laminar regime net flow Reynolds numbers (Ren) (net flow Reynolds numbers Ren ≤ 10). A high degree of plug flow can be achieved in this design of OBR. In conventional OBR designs, plug flow is generated by the formation of well-mixed volumes in series due to toroidal vortex formation generated by the interaction of the baffle geometry with an oscillatory motion superimposed upon the net flow. The helical baffled design represents a significant development in oscillatory baffled reactors, as this system can provide plug flow behaviour over a wider range of oscillatory Reynolds number (Reo), (50–800). This is due to the combined effect of the swirling flow and vortex production. The oscillation amplitude was demonstrated to have a strong effect on the flow behaviour. The results revealed that the helical baffled design exhibited plug flow at high oscillation amplitudes (xo ≥ 2 mm or Strouhal number (Str), Str ≤ 0.2).The highest number of equivalent tanks-in-series was obtained at Reo = 400–700.

► Helical baffled design exhibited plug flow at high oscillation amplitudes (xo ≥ 2 mm or Strouhal number Str ≤ 0.2). ► Fluid mixing inside the helical baffled design exhibited little improvement as the number of tanks was below 5 and only reached a maximum of 10–15 at Reo = 100–150. ► Plug flow performance was observed at a wide range of Reo (Reo = 50–800 at Str < 0.2, and 50 ≤ Reo ≤ 300 at Str = 0.2).

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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