Design and Efficiency Aspects of Rotary Dryers
by Greg Palmer, B.E. Ph.D. and Tony Howes*, B.E. Ph.D.
Palmer Technologies Pty Ltd, Brisbane, Australia
* Department of Chemical Engineering, University of Queensland, St. Lucia 4072 Australia.
Abstract
The drying of products like sand, aggregates, fertilizers and food products is an important step
in industrial processes. With an increasing focus on reducing greenhouse gas emissions and
energy demand the design of drying units has become critical. In the past rotary dryers have
been in some cases thermally very inefficient primarily due to poor design. Fluid bed dryers on
the other hand are thermally very efficient due to the interment contact of the gas stream with
individual particles and a better understanding of the design principles. Thus, the science of
fluid bed dryer design means these units are relatively easy to design even though thermal
energy demand between each type of unit is approximately the same. The problem is that the
same level of engineering knowledge has not been available for rotary dryers and as
consequence these drying units are generally over designed and thermally inefficient.
This paper discusses the difference between a rotary dryer and a fluid bed dryer used to dry
slag1. It is important to understand the difference between the two pieces of equipment and the
design aspects required in the rotary dryers. One of the difficulties with the design of rotary
dryers is determining the amount of material falling through the gas stream at any moment in
time.
Due to the complexity in calculating the percentage hold up in the gas stream and the
percentage hold up in the lifter various lifter designs have been tried over the years on a trail
and error basis, many with poor results. Because of complexity of estimating some parameters
most rotary dryers are over designed and as a consequence the final product can be over dried
and heated wasting thermal energy and higher than necessary equipment costs.
Work carried out by Palmer Technologies and The University of Queensland has been aimed at
understand the aspects of drying in a rotary dryer. This work enabled computer models to be
developed and validated against numerous industrial dryers in the sand and cement industries.
The results from drying slag using a fluid bed dryer and a rotary dryer are first compared
followed by the design criteria for rotary dryers are discussed in this paper.