The wastewaters discharged from chemical industries which may contain heavy
metal ions have toxic effect on all the living organisms. Because of this,
disposal of them to the environment is a major threat to both human health
and ecosystem. So the development of new technologies is required to treat
wastewaters as an alternative to traditional physicochemical processes. Bi
osorption, the process of passive cation binding by dead or Living biomass,
represents a potentially cost-effective way of eliminating toxic heavy met
als from industrial waste waters. While the abilities of microorganisms ro
remove metal ions in solution have been extensively studied, fungi have bee
n recognized as a promising class of low-cost adsorbents for removal of hea
vy-metal ions from aqueous waste streams. Algae, fungi and bacteria differ
from each other in their constitution, giving rise to different mechanisms
of metal biosorption. The paper reviews the biosorption capacities of vario
us fungi (free or immobilized or subjected to physical and chemical treatme
nts) and, chitin and chitosan, important fungal cell wall components, in di
fferent reactor systems for heavy metal ions and discusses the fungal bioso
rption mechanisms. To explore the biosorption mechanisms, it is necessary t
o identify the functional groups involved in the biosorption process. As si
ngle toxic metallic species rarely exist in natural and waste waters, any a
pproach that attempts to removal heavy metals from multi-component systems
using fungi would be more realistic. The effects of various combinations of
the metal ions on the biosorption capacity of various fungi are discussed
and the actions of the metal ion combinations synergistic or antagonistic a
re identified. Equilibria and capacity relationships for mono-component sys
tems are well established and quantitatively expressed by various types of
adsorption isotherms. In the case of multi-metal systems, models should be
modified in order to take into account all metals and cover experimental da
ta over a wide range of solution concentrations. The researcher is often pu
zzled as to what are the basic differences or similarities between the isot
herms and what isotherm to select for practical use to predict adsorption c
apacities or to incorporate it in predicting breakthrough of columnar opera
tions. The paper reviews the range of equilibrium sorption models, and diff
usion and sorption models in different reactor systems used by different re
searchers to correlate experimental data for fungal biosorption.