Coal-fired boiler exhaust gas treatment apparatus and coal-fired boiler exhaust gas treatment method
View Patent ↗An exhaust gas treatment apparatus which includes a denitration device, a dust collector, and a desulfurization device in order, respectively, in a flow path of exhaust gas discharged from a boiler, wherein a heavy-metal component removal device is provided in the exhaust gas flow path between the dust collector and the desulfurization device. This device is provided with: an absorption tower including a nozzle which sprays acidic absorption liquid on the exhaust gas, a tank which stores liquid which has absorbed a heavy metal, and a pump which supplies the nozzle with the liquid in the tank; a neutralizing tank which neutralizes the liquid drawn from the absorption tower; and a separator which separates the neutralized liquid into a solid and a liquid component. Since a small amount of heavy metal can be removed in the absorption tower, re-emission of the heavy metal by the desulfurization device is prevented.
1. A coal-fired boiler exhaust gas treatment apparatus comprising:
(a) a denitration device including a denitration catalyst to remove nitrogen oxide in an, exhaust gas,
(b) a dust collector configured to remove ash dust in the exhaust gas,
(c) a heavy-metal component removal device configured to remove a heavy-metal component in the exhaust gas,
the heavy-metal component removal device comprising;
an absorption tower including a heavy-metal absorption unit configured to spray an acidic absorption liquid having a pH of 1 to 3 for absorbing heavy metal to the ex-haunt gas, a storage unit configured to store a heavy-metal absorption liquid ab-sorbing the heavy metal in the heavy-metal absorption unit, and a circulation unit configured to supply the heavy-metal absorption liquid of the storage unit to the heavy-metal absorption unit; an extraction unit configured to extract the heavy-metal absorption liquid from the absorption tower; a neutralization unit configured to supply a pH adjuster to the heavy-metal absorption liquid extracted by the extraction unit and neutralize the same so that the pH of the heavy-metal ab-sorption liquid in the neutralization unit is 5 to 7; and a solid-liquid separation unit configured to separate a solid component and a liquid component from the heavy-metal absorption liquid neutralized in the neutralization unit,
(d) a desulfurization device configured to remove sulfur oxide in the exhaust gas by an absorption liquid and a denitration device, a dust collector, a heavy-metal component removal device and a desulfurization device are sequentially disposed from an upstream side to a downstream side of exhaust gas flow.
2. The coal-fired boiler, exhaust gas treatment apparatus according to claim 1 , further comprising a waste fluid supply unit configured to supply a part of the liquid component separated by the solid-liquid separation unit to the exhaust gas flow path between the denitration device and the dust collector.
3. A coal-fired boiler exhaust gas treatment method in which nitrogen oxide in an exhaust gas discharged from a boiler using coal as a fuel is removed by a denitration catalyst, and ash dust is removed from the exhaust gas after removing the nitrogen oxide, and then sulfur oxide is removed from the exhaust gas by an absorption liquid after removing the ash dust, the coal-fired boiler exhaust gas treatment method comprising:
spraying an acidic absorption liquid having a pH of 1 to 3 for absorbing heavy metal to the exhaust gas after removing the ash dust and before removing the sulfur oxide;
again using the heavy-metal absorption liquid after spraying for absorbing the heavy metal, and supplying a pH adjuster to a part of the heavy-metal absorption liquid after spraying, thus to neutralize the same so that the pH of the heavy-metal absorption liquid is 5 to 7; and
separating a solid component and a liquid component from the neutralized heavy-metal absorption liquid, thus to remove a heavy-metal component in the exhaust gas.
4. The coal-fired boiler exhaust gas treatment method according to claim 3 , further comprising supplying a part of the separated liquid component to the exhaust gas after removing the nitrogen oxide and before removing the ash dust.