BIOMASS
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Production of the biomass (harvesting, transport).
- Preparation of the biomass as a suitable fuel (comminution or gasification).
- Combustion of the fuel so as to provide useful energy (boilers or internal
combustion).
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Shape and size (e.g., dust, pellets, shavings, bales).
- Density and compaction (which affects the calorific value and volatile content
per unit volume. This in turn affects the combustion characteristics, product
handling and storage space required)
- Water content (depends on type of biomass, time of harvest and type of storage.
It affects not only the calorific value but also the combustion
temperature, exhaust and ash characteristics, plus the time and type of
storage).
- Ash content and fusion characteristics (depends on type of biomass and degree
of contamination. It affects the calorific value and its acceptance in certain
types of burner).
Raw
Material.
The complete biomass system consists of the following steps:
For
electricity generation biofuels may be either burnt directly or after conversion
to a gaseous state. Liquid products are mainly used as a transport fuel.
Biomass comprises two main groups:
a.
Dry waste (e.g. straw & forestry residue).
b. Wet waste (e.g. farm slurries resulting from animals, plus green agricultural
crop waste).
Dry
waste can include food crops such as rape and sugar-producing crops. From these,
liquid fuels can be produced to replace diesel or gasoline in automotive engines.
The term also includes energy crops, grown specifically as fuel. Short rotation
coppice (SRC) such as willow and poplar has been identified as showing potential
for energy supply from farm land no longer required for food production. Eucalyptus
and alder also produce reasonable yields. The grasses miscanthus and spartina
appear to have the ability to produce high yields of biomass.
Design of the utilisation plant has to be co-ordinated,
not only with the characteristics of the biomass used, but also with its preparation.
In the case of combustion, this affects the type of burner used, e.g. underfeed
or chain-grate stoker, pulverised or fluidised bed combustion. A homogeneous
fuel will make automation easier. It will reduce the need for maintenance
and manual intervention. Some of the essential characteristics which need
to be determined are:
ENERGY
CONVERSION
Due
to the low energy content per unit volume of biomass, and the consequent transport
costs, energy conversion has to take place near to the point of production.
The principal methods for converting biofuels into
energy are:
a)
Direct combustion.
b) Biological conversion.
c) Advanced thermal conversion.
COMBUSTION:
At
present, plants using direct combustion for steam generation are the only fully
developed biomass systems available for the heat and electricity generation
markets. For generation and for Combined Heat and Power (CHP) they operate in
combination with turbines or motors (screw or reciprocating types) Complete
systems, with normal commercial guarantees, are available from competing vendors
(see attachment “chiklitt”).
In such a process the biomass is simply burnt to recover
energy in the form of heat. Electricity can then be generated, using a conventional
steam cycle. Numerous boiler designs are available, many of which have been
developed specifically for the use of biomass fuels. A plant for the combustion
of wood chippings, straw or “dry” energy crops has the same basic
design as that for coal combustion. More refractory lining is added to allow
the relatively wet fuels to dry on the grate, with extra secondary air to
ensure complete combustion of volatiles. Such plant can handle fuels with
a moisture content as high as 60% by weight. They are available in a wide
range of sizes, from a few hundred kilowatts to many megawatts. The emissions
from these plants is low, with only a vapour plume from the stack following
start-up. At the larger sizes, fluidised bed combustion is possible.
The higher the combustion temperature, the more efficient
the process and the more energy available for electricity generation. At high
temperatures however, fusion of the ash could cause deposition problems in
boilers. In all combustion plant types, cereal straw presents problems as
the ash has a low melting point. This may lead to boiler fouling.
For large power stations, biomass may be burnt together
with coal. Most biomass fuelled plants will be small in size, due to the limitation
imposed by having to transport the fuel over long distances. Consequently,
the overall thermal efficiency will be low – 20-25% in the output range
of 1 – 30 MW (elect). Where the plant size is less than 1 MW (elect)
the efficiency falls to a value making such small scale electricity generation
uneconomic in almost all situations. The exceptions are where the biomass
fuel is obtained free, or where the price of fossil fuel (gas, oil, coal)
is high.
BIOLOGICAL
CONVERSION:
There
is significant development activity in this area, with numerous pilot and demonstration
projects in operation (see attachment “biogas”). Green agricultural
crops and residues, as well as animal slurries and sewage sludge can be subjected
to anaerobic digestion. This is the bacteriological fermentation of organic
material in the absence of oxygen. This can take place in fabricated tanks.
The activity of these “anaerobic” bacteria leads to the formation
of a methane-rich biogas, comprising about 60% methane, with a calorific value
of about 25 Mjoules/ sq.m. After filtering and drying, the gas can be used as
a fuel, either for boilers, gas turbines or conventional spark ignition gas
engines. Most new applications use spark ignition engines for the driving of
alternators.
ADVANCED
THERMAL CONVERSION:
Research
is proceeding on these concepts, with a number of pilot plants in operation.
These processes are fairly early in the development phase. It is too early for
commercial application. There are three techniques available, all requiring
the application of heat.
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Gasification is the thermal oxidation of an organic feedstock, with too little
oxygen to enable complete combustion. This results in the production of a gas
mixture, containing carbon monoxide, hydrogen and methane. All of these have
a fuel value and can be used to fuel internal combustion engines. At the scales
appropriate to biomass, overall thermal efficiency is increased beyond that
for conventional combustion, from the low 20% range to over 40%. This process
has a longer history than the other two below.
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Pyrolysis is the thermal degradation of organic feedstock in the absence of
an oxidising agent to produce a gas, liquid and char remains. By
increasing the heating rate, the proportion of gas and liquid is increased.
The resultant pyrolysis oil can be used as a fuel in internal combustion
engines.
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Liquefaction is a relatively low temperature process. High-pressure hydrogen
is injected into an organic feedstock to liquefy it. This technology is at the
research stage only
Where
biomass is used to fuel generator prime movers, be they internal combustion
engines, steam or gas turbines, the possibility exists of utilising the waste
heat from the prime mover exhaust. Such Combined Heat and Power (CHP) schemes
offer an interesting alternative where heat is required in addition to electricity.
Where air conditioning is required, this heat can be utilised as the energy
input to an absorption chiller. The tendency at the lower power range (<3
mw) is for motors to be more economic as a prime mover than turbines.
GENERATION.
The
economics of the project will be affected by the purchase price of a kilowatt-hour,
and hence the reduction in the cost of power purchased from the public supply.
Whether the public supply will allow parallel operation is of great significance
economically, in particular what price they will pay for kilowatt-hours exported.
Power systems have traditionally been designed to take
power “down” to the consumer. Local, or “embedded”
generation acts in the opposite sense. There is therefore a tendency to raise
the local voltage. This has to be taken into account when calculating the
effect of local generation on other users and on the distribution system as
a whole. Fault level and system capacity have to be considered and a protection
and control scheme agreed with the public supply authority.