Flue gas loss (q2), leading cause of heat loss in boiler, contributes about 60-70% of the total. It is mainly decided by flue gas temperature and volume. Normally when flue gas temperature increases every 12-15℃, q2 will increase 1%, accordingly, coal consumption will increase 1.2-2.4g/kW·h. Mostly, flue gas temperature in utility boiler is about 120-140℃, some are up to 160℃. Flue gas cooler could furtherly reduce temperature 40-50℃. The energy recovered from flue gas could be used to heat condensate water from low pressure feedwater heater, cycling water of district heating network, or combustion air for boiler.
Flue gas cooler could be connected with low pressure feedwater heater in parallel or series to reduce steam extraction from turbine, thus turbine output is increased. In parallel design, when flue gas cooler is in breakdown, the plant has to shut down. So, connection in series is popular.
Some energy would be lost if flue gas is used to heat condensate water from feedwater heater, because saturated steam with increased pressure would conflict steam extracted from turbine. So, economic profit would be better if flue gas is used to heat cycling water. For CHP unit, it could heat cycling water in winter, and condensate water in summer.
Flue gas cooler could also transfer heat to combustion air. Increased temperature of combustion air means higher boiler efficiency. Flue gas for combustion air heating only is rarely seen in practice. Sometimes, it is combined with condensate water heating. This flexible design could adjust water flow according to season and boiler steam rate to optimize operation.
Flue gas cooler installed before ESP is an economic and easy operation. It could bring benefits like low fuel consumption, higher dust collection efficiency, less ID fan energy consumption, less water consumption in FGD system.
Cooled flue gas at 85~90℃ could enter absorption tower directly. This design could utilize waste heat in flue gas deeply and reduce cooling water of FGD system.
The first stage is placed before dust collector. Flue gas temperature is reduced to 115~125℃ to improve dust collection efficiency. For a hybrid particulate collector, it could extend service life of filter bags.
The second stage is placed before FGD absorption tower to utilize waste heat to the maximum.
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