Ethanol fermentation
Fermentative processes have been described earlier, both in the
general wider metabolic context and specifically in regard to their potential use
in the treatment of biowaste. Fermentation produces a solution of ethanol in
water, which can be further treated to produce fuel-grade ethanol by subsequent
simple distillation, to 95% ethanol, or to the anhydrous form by azeotropic
codistillation using a solvent.
The relative ease with which
liquid fuels can be transported and handled, coupled with their straightforward
delivery to, and inherent controllability of combustion in, engines makes them
of considerable importance. Ethanol is a prime example in this respect, since
it can be used either as a direct replacement for petrol, or as a
co-constituent in a mix. Though at 24 G J/m3, it has a lower calorific value
than petrol (39 G J/m3), in practice any performance discrepancy is largely
offset by its better combustion properties.
There are thriving ethanol
industries in many countries of the world, generally using specifically
energy-farmed biomass in the form of primary crop plants, like corn in the USA
and sugarcane in Brazil. In another example of the importance of local
conditions, the production costs of ethanol and the market price realised by
the final fuel depend on many factors external to the technology itself. Hence
the indigenous economy, employment and transport costs, government policy, taxation
instruments and fiscal incentives all contribute to the overall commercial
viability of the operation.
Brazil, where ethanol/petrol
mixing has been routine since the 1970s is an excellent example. Although the
country’s use of ethanol partial substitution has a relatively long history,
dating back to the 1930s, the real upsurge of acceptance of ‘gasohol’ lay in an
unusual combination of events, partly driven by the energy crisis of the
mid-1970s. Rising oil prices, which increased by over 25% in lessthan two
years, came at the same time as a fall in sugar revenue following a slump in
the world market. The Brazilian sugarcane industry, which had shortly before
invested heavily in an extensive national programme of modernisation, faced
collapse. Against this background, the production of fuel from the newly
available biomass crop became a sound commercial move, simultaneously reducing
the country’s outlay on purchased energy and buoying up one of its major
industries.
In the preceding discussion of biogas, this involved the marrying
together of the goals of biowaste treatment and energy production. In a similar
vein, as was described in an earlier, there have been various attempts, over
the years, to produce ethanol from various forms of waste biomass, using
naturally occurring microbes, isolated enzymes and genetically modified
organisms (GMOs). The appeal to obtaining renewable energy from such a cheap
and readily available source, is obvious.
In many respects, the
situation which exists today with biowaste is very sim-ilar to that which
surrounded Brazil’s sugarcane, principally in that there is an abundant supply
of suitable material available. The earlier technological barri-ers to the
fermentation of cellulose seem to have been successfully overcome. The future
of ethanol-from-biowaste as an established widespread bioindustrial process
will be decided, inevitably, on the long-term outcome of the first few
commercial projects. It remains fairly likely, however, that the fledgling
industry will depend, at least initially, on a sympathetic political agenda and
a support-ive financial context to succeed. While this application potentially
provides a major contribution to addressing two of the largest environmental
issues of our time; energy and waste, it is not the only avenue for integrated
biotechnology in connection with ethanol production.
As has already been
mentioned, specifically grown crops form the feedstock for most industrial
fermentation processes. The distillation which the fermen-tate undergoes to
derive the final fuel-grade alcohol gives rise to relatively large volumes of
potentially polluting byproducts in the form of ‘stillage’. Typically high in
BOD and COD, between six and 16 litres are produced for every litre of ethanol
distilled out. A variety of end-use options have been examined, with varying
degrees of success, but dealing with stillage has generally proved expen-sive.
Recently developments in anaerobic treatments have begun to offer a better
approach and though the research is still at an early stage, it looks as if
this may ultimately result in the double benefit of significantly reduced cost
and additional biomass to energy utilisation. The combination of these
technologies is itself an interesting prospect, but it opens the door for
further possibilities in the future. Of these, perhaps the most appealing would
be a treatment train approach with biowaste fermentation for ethanol
distillation, biogas production from the stillage and a final aerobic
stabilisation phase; an integrated process on a single site. There is, then,
clear scope for the use of sequential, complementary approaches in this manner
to derive maximum energy value from waste biomassin a way which also permits
nutrient and humus recovery. Thus, the simultaneous sustainable management of
biologically active waste and the production of a sig-nificant energy
contribution becomes a realistic possibility, without the need for mass-burn
incineration. In many respects this represents the ultimate triumph of
integration, not least because it works exactly as natures does, by unifying
disparate loops into linked, cohesive cycles.
Clearly, both AD and ethanol
fermentation represent engineered manipulations of natural processes, with the
activities of the relevant microbes optimised and harnessed to achieve the
desired end result. In that context, the role of biotechnol-ogy is obvious.
What part it can play in the direct utilisation of biomass, which generates
energy by a quite different route, is less immediately apparent. One of the
best examples, however, once again relates to biological waste treatment
technologies, in this instance integrated with short rotation coppicing (SRC).
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