7.2.4.4
Emissions from direct biomass combustion
The great variety of both biomass fuel types and boiler
designs, and the large range of plant size (10kW to 50
MW), all make impossible any precise comparison between
procedures, products and plant, when considering not only
technical and economic performance, but also environmental
impact. Table 7.5 gives a general guideline about airborne
emissions.
|
Plant size
|
Flue gas O2 content [Vol. %]
|
CO[ g/m3 }
|
Emission limits
|
|
Dust [mg/m3]
|
OrganicC [mg/m3]
|
NOx [mg/m3]
|
|
15 kW - 100kW
|
13
|
4
|
150
|
-
|
-
|
|
100kW - 5MW
|
11
|
0,25
|
150
|
50
|
500
|
|
5MW - 50MW
|
11
|
0,25
|
50
|
50
|
500
|
7.2.4.5 Fluidised
Beds
For larger plants, a more complex option is fluidised bed
combustion, in which mixing of the fuel and air is assisted
by being blown through a bed of inert dry particles such
as sand. This technique allows either complete combustion
or gasification of the fuel (see below). Commercial developments
are categorised as either bubbling fluidised bed (BFB) combustion
using low air velocities, or circulating fluidised bed (CFB)
combustion in which higher velocities result in some sand
being blown out of the top and recirculated (figure 7.14).
CFB tends to be more expensive, but reduces NOx emissions
due to lower operating temperatures.
Figure
7.14 Fluidised bed boilers Source: ref 7.7
Fluidised
bed combustors are more technically intricate with associated
higher costs of design, construction and operation. As a
general rule, there is a threshold in the region of 8 MWth
above which they begin to gain economic advantage over fixed
bed combustors. On the other hand, fluidised bed has the
following advantages over fixed bed combustion:
· The high thermal inertia of the bed provides conditions
for stable ignition, despite variability of fuel quality.
Hence it is more tolerant of a wider range of fuel characteristics.
· Control of bed temperature allows a range of fuels
with varying ash properties to be burnt while avoiding ash
softening conditions in the bed.
· Relatively low combustion temperatures mean that
NOx emissions are low.
· If limestone is added to the bed material then
in-situ capture of SO2 is possible, though this is not necessary
for biomass fuels since they are low in sulphur.
BFB units are commercially offered up to 100 MWe, and CFB
units up to 400-600 MWe. CFB boilers have proven feasibility
to burn about 70 different fuels alone or in co-combustion
mode. BFB boilers have proved their feasibility for biomass
and waste fuels with similar characteristics especially
in lower capacities, starting from 5 MWth with well-processed
fuel.