posted on 2019-12-16, 14:06authored byChirag
M. Khalde, Vikram Ramanan, Jitendra S. Sangwai, Vivek V. Ranade
Significant efforts have been and are being spent on
developing
intensified tubular reactors for continuous manufacturing of fine
and specialty chemicals. In this work, we have proposed a new design
of a passive mixer cum reactor for process intensification and development
of continuous processes. The mixer/reactor consists of threaded inserts
with cone-shaped ends, placed concentrically in the tube such that
fluid flows through the annular region between the inserts and the
tube. The proposed design is easy to fabricate and maintain, and overcomes
the limitations of scale up/scale down compared to most of the commercial
passive mixers. The spliting and recombination of flow around inserts,
the swirling effect generated by threads, the change in the swirl
direction due to a change in the direction of the screw threads, and
the pinching effect/expansion at the cone–cone shaped ends
realize desired enhancements in mixing and heat transfer. A detailed
computational study has been carried out on the mixer cum reactor
to characterize flow, mixing, and heat transfer at different operating
conditions using a verified and validated CFD model. Various designs
and configurations of threaded inserts were considered: 5-channel,
7-channel, 9-channel, smooth surface (no threading), and smooth surface-extended
rear end inserts. The flow, mixing, and heat transfer were characterized
over the Reynolds number range of 100 to 1600. The structure of the
generated swirling flow, effect of pinching/expansion, direction reversal
of flow, tracer fraction, temperature, and pathlines were investigated
systematically to gain new insights. Threaded inserts could achieve
excellent mixing (>99% of mixing intensity) and heat transfer (7
times
with smooth inserts and 20 times without inserts). The presented results
will provide a sound basis for selecting appropriate threaded inserts
for intensifying mixing and heat transfer in tubular reactors. The
work also provides a useful starting point for further work on multiphase
flows in a tubular reactor with threaded inserts.