BOILER
EMISSIONS -2
When
SCR or catalyst is used for NOx control,it has to be located in an optimum
gas temperature zone in the boiler or HRSG.Typically for most catalysts,
600 to 800 F is a good starting point, though there are catalysts which
can operate efficiently around 450-500 F. CO catalysts can operate at higher
temperatures;a higher gas temperature reduces the size or amount of catalyst
due to the higher efficiency of conversion or activity,however oxidation
concerns and catalyst life have to be considered,while low gas temperatures
may require a larger size and hence resulting in more cost and higher gas
pressure drop across the catalyst. Very low gas temperatures,in the region
of 450 F or below, may be a concern when oxides of sulfur are present in
the flue gas stream. There is a potential for formation of ammonium sulfate
at low gas temperatures(below 450 F typically),when excess ammonia interacts
with sulfur trioxide.These particles when deposited on downstream heating
surfaces can affect heat transfer process,particularly when extended surfaces
are used.
It
is important to evaluate the boiler or HRSG performance at various modes
of operation when a catalyst is used and ensure that the gas temperatures
are within limits set by the catalyst supplier. Charts below give an idea
of the boiler or HRSG performance under different loads. Note the variations
in gas temperatures at different locations.Figure below show the temperature
profiles in a package boiler firing gas at various loads and the bottom
figure shows the temperature profiles in a fired HRSG at various steam
generation rates. Suitable location for the SCR is obtained by splitting
up the HRSG evaporator section or by using a gas bypass system in a package
boiler to ensure a reasonable gas temperature at various loads. For the
example below,it appears that if a SCR is located between the evaporator
and economizer,the gas temperature is reasonable from 100 % to 50 % load,below
which gas bypass system must be operated to raise the gas temperature.By
splitting up the evaporator of the HRSG below into two portions,a suitable
gas temperature range may be arrived at for the SCR.The two evaporators
connect with the same drum and have a common downcomer,riser system.
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