268
17 Utilization of Microbial Potential for Bioethanol Production from Lignocellulosic Waste
Bacterial/fungi
/enzyme
Biological
delignification
Hydrolysis
Fermentation
Biofuel
Agricultural refuse
Streptomyces, P.
chrysosporium,
LiP
Bacillus sp.,
cellulases,
xylanases,
etc.
S. cerevisiae,
C. shehatae
Bacterial/fungi
/enzyme
Bacterial
and/fungi
Figure 17.2
Overview of bioethanol production from lignocellulosic biomass.
17.2
Processing of Lignocellulosic Biomass to Ethanol
Pretreatment of LCB is the primary step in bioethanol production protocol. It
is considered to be the basic step which largely affects edibility of cellulose and
that unequivocally affects downstream expenses including detoxification, catalyst
stacking, squander treatment requests, and different factors (Figure 17.2). Pretreat-
ment establishes for over 40% of the all-out handling cost. The cellulose in LCB
is secured by lignin and hemicelluloses. Subsequently, it decreases the available
surface area accessible for enzyme-mediated saccharification. Pretreatment is
necessary to change the LCB to naturally visible and minute size. Appropriate
pretreatment might expand the convergence of fermentable sugars post-enzymatic
saccharification in this way increasing the general procedure efficiency. A perfect
pretreatment process is essential to enhance the hydrolysis of LCB [5]. The various
pretreatment methods of LCB include mechanical pretreatment, physico-chemical
pretreatment, chemical pretreatment, and biological pretreatment. Mechanical
pretreatment reduces cellulose crystallinity, is easy to handle, reduces degree of
polymerization, and increases surface area. But unfortunately, it has no high energy
input nor removes any lignin. Summary of commonly used pretreatment methods
are listed in Table 17.1. Physico-chemical pretreatment increases pore volume,
improves enzyme accessibility, removes hemicellulose, and reduces particle size.
But, it contributes to less lignin removal, it has high energy demands, and it
decomposes sugars.
Chemical pretreatment has high reaction rates, it removes hemicellulose more
efficiently, increases surface area, and creates an alteration in lignin structure.
Little lignin removal, requirement of neutralization process, inhibitors formation,
and requirement of disposal of neutralization salts are some of the drawbacks of
chemical pretreatment. To fill up the voids of all these pretreatments of LCB, a new
method of biological pretreatment has come up. It can degrade lignin successfully,
has less formation of inhibitors, has low energy and capital cost demands, no
chemical reagents are required, and it can reduce the polymerization degree of
cellulose and hemicellulose in mild environmental conditions. It just has a few
disadvantages like slow rate of delignification, longer residence timings, and loss of
carbohydrates as they are metabolized by the microbes [3]. Plenty of LCB namely