Systems and methods for removing mercury from emissions
The present technology is generally directed to systems and methods for removing mercury from emissions. More specifically, some embodiments are directed to systems and methods for removing mercury from exhaust gas in a flue gas desulfurization system. In one embodiment, a method of removing mercury from exhaust gas in a flue gas desulfurization system includes inletting the gas into a housing and conditioning an additive. In some embodiments, conditioning the additive comprises hydrating powder-activated carbon. The method further includes introducing the conditioned additive into the housing and capturing mercury from the gas.
1. An emissions handling system, comprising:
a housing comprising a contact zone and configured to be in communication with a source of emissions including mercury, the contact zone comprising a dry scrubber;
a first supply line, upstream of the contact zone, fluidically coupled to a source of a first input comprising an additive;
a second supply line, upstream of the contact zone, fluidically coupled to a source of a second input comprising water;
a third supply line fluidically coupled to the first and second supply lines and the housing upstream of the contact zone, wherein the third supply line is configured to provide to the housing the first input and the second input, such that, in operation the first input contacts the source of emissions; and
a baghouse in communication with the outlet of the housing and configured to capture at least a portion of the additive.
2. The system of claim 1 , further comprising an introducer configured to provide the first input, the introducer comprising an atomizer, throat, or nozzle.
3. The system of claim 2 , further comprising a sensor configured to sense at least one of mercury, temperature, dew point, or pressure, wherein the sensor is in communication with the introducer.
4. The system of claim 1 , further comprising:
a first sensor configured to measure mercury;
a second sensor configured to measure temperature; and
a third sensor configured to measure dew point.
5. The system of claim 4 wherein the second sensor is positioned to measure temperature at an outlet of the contact zone and the third sensor is positioned to measure dew point at the outlet of the contact zone.
6. The system of claim 1 wherein the source of the emissions comprises at least one of a coke processing system, a power plant, a trash-to-steam plant, a carbon alloy processing system, a dry sulfur removal system, or a hot ash circulator.
7. The system of claim 1 , wherein the bag house comprises fly ash.
8. The system of claim 1 , wherein the additive comprises powder-activated carbon.
9. The system of claim 1 , wherein the additive comprises a carbon-based material and/or an absorbent.
10. The system of claim 1 , further comprising a fourth supply line fluidically coupled to the housing upstream of the contact zone and configured to provide to the housing a third input comprising lime.
11. The system of claim 1 , further comprising a continuous emissions monitoring system (CEMS) downstream of the baghouse.
12. The system of claim 11 , further comprising an induced draft fan between the CEMS and the baghouse.