Bio leaching is becoming increasingly used for the extraction of gold from
refractory gold ore. It is established that in gold bio leaching two kinds
of mechanism are involved namely indirect bio leaching and direct bio leach
ing. The reaction schemes involved in the different mechanisms and kinetic
rate expressions for different reactions have been reported in the literatu
re.
In the present paper an attempt has been made to develop an approach for si
mulation of a gold bio reactor leach circuit. For this purpose a mathematic
al model for bio leaching has been developed for process design of a gold b
io reactor circuit. The salient features of the model are parameter estimat
ion from experimental data and then scaling up the process for pilot size a
nd industrial size bio reactor operation in continuous mode. Bio reactors c
an be simulated for various combinations of series-parallel modes of operat
ion. Experimental data of the laboratory scale bio reactor collected for di
fferent pulp densities and residence times have been simulated for paramete
r estimation. Experimental data of pilot size bio reactors, collected from
the literature, have been used for vetting of the parameters estimated earl
ier. Analysis of the simulation results indicates the extent of conversion
taking place due to indirect and direct mechanisms. The performance of the
simulation model developed based on literature information has been confirm
ed by some experimental data collected as well as by literature data. (C) 2
001 Elsevier Science Ltd. All rights reserved.