Various attempts have been made to develop biotechnological processes
based on microbiological desulfurization employing aerobic and anaerob
ic bacteria. In order to obtain a biodesulfurization process competiti
ve with the chemical-physical one of hydrodesulfurization (HDS), a bio
technological process has to follow the three main refinery steps: 1)
separation, entailing some pretreatment of crude oil; 2) conversion, i
.e. biocatalytic transformation where the biocatalyst favours a select
ive desulfurization process without destroying useful products; 3) fin
ishing, in which the crude oil is separated from the biocatalyst and t
he byproducts. Biocatalysis may be carried out using whole cells or is
olated enzymes in the free or immobilized form. The use of isolated en
zymes is advantageous since it avoids the formation of undesirable byp
roduct mediated by contaminating enzymes as in the case of the aerobic
biodesulfurization, which is not a selective process. In fact, the ae
robic microorganisms may degrade almost all the compounds which make u
p the heavy oil. However, despite this advantage, extraction and purif
ication of the enzyme is costly and, frequently, enzymes catalyzing ox
idation-reduction reactions require enzyme cofactors which must be reg
enerated after the reaction. For these reasons, metabolic conditions c
an often be designed by using whole cell biotransformations to promote
cofactor regeneration, thus avoiding the problems associated with cof
actor recycling and regeneration. Today, the main limitations for the
industrial application of a biodesulfurization process are associated
with the high cost of the biocatalyst and with the volumetric ratio be
tween the organic phase and the aqueous one. In order to overcome thes
e problems, cell immobilization is one of the most promising approache
s in terms of treatment costs and in finishing step times when compare
d to a continuous stirred tank bioreactor for the biodesulfurization p
rocess. (C) 1997 Elsevier Science B.V.