Thesis-2000-Cave.pdf (84.44 MB)
Download fileGypsum calcination in a fluidised bed reactor
thesis
posted on 2010-10-22, 10:27 authored by Sion CaveGypsum (calcium sulphate dihydrate) is of great industrial importance with over 95,000
ktonnes being used in the world per annum. The greatest use of gypsum is in the
production of plaster (calcium sulphate hemihydrate) for use as an interior finisher. Plaster
is produced by the calcination (thermal decomposition) of gypsum. The most popular
design is a continuous calciner where gypsum is fed continuously and is directly heated by
hot air.
There are a number of different phenomena occurring within a calciner, including heat
transfer, mass transfer, particle and gas mixing, elutriation and the dehydration reaction
itself. All these processes interact with each other. Although a lot of research has been
carried out in these areas already, the literature has been found to contain significant
discrepancies. This study contains experimental work which has been carried out in order
to better understand the physical processes occurring within a gypsum calciner.
The rate of dehydration of gypsum (35-67μm in diameter) has been studied in a fluidised
bed reactor. Experiments were carried out at bed temperatures of 100 to 170°C. The
fluidising gas was air with water vapour pressures of 0.001 to 0.30 atm. The dehydrations
were under differential conditions. The results show that the dehydration under these
conditions can be successfully modelled using the two dimensional Avrami-Er'ovev
expression.
A study of the fluidisation and elutriation properties of gypsum in batch vessels (cylindrical
and conical) has been carried out. The mechanics of elutriation has been investigated and
modelled for various freeboards, superficial gas velocities and air humidities.
Tracer tests have also been carried out on a laboratory scale continuous conical kettle.
Sodium carbonate was used as the inert tracer material. Runs were carried out at different
air and gas flowrates and different bed temperatures. Residence time distributions were
elucidated.
Finally, the above experimental data and component models have been investigated for
their applicability to producing a model of the laboratory scale gypsum calciner.
History
School
- Aeronautical, Automotive, Chemical and Materials Engineering
Department
- Chemical Engineering
Publisher
© Sîon CavePublication date
2000Notes
A Doctoral Thesis. Submitted in partial fulfillment of the requirements for the award of Doctor of Philosophy of Loughborough University.EThOS Persistent ID
uk.bl.ethos.247922Language
- en