Methods for removing contaminants from exhaust gases
View Patent ↗Industrial gas streams such as flue gas streams are treated for nitrogen oxides and other contaminants in dry or semi-dry scrubbers. After the flue gas stream has been contacted with a sorbent, ozone is mixed downstream into the flue gas stream thereby oxidizing the nitrogen oxides and other contaminants. The oxidized contaminants is contacted with sorbent present in the gas stream in the remaining height or volume of the scrubber downstream of ozone injection; and The sorbent is then separated from the flue gas stream leaving the dry or semi-dry scrubber.
1. A method for removing contaminants from a gas stream comprising the steps:
a) feeding the gas stream containing contaminants into a dry or semi-dry scrubber at a location near one end of the dry or semi-dry scrubber;
b) contacting the gas stream containing contaminants with a sorbent;
c) injecting ozone into the dry or semi-dry scrubber downstream of the contact between the gas stream containing contaminants and the sorbent, the ozone being injected at a location that is at least 15% of the total height of the dry or semi-dry scrubber above a lower end of the dry or semi-dry scrubber and higher than the location where the gas stream is fed to the dry or semi-dry scrubber, thereby oxidizing the contaminants in the gas stream;
d) contacting the oxidized contaminants with sorbent in remaining height or volume of the scrubber downstream of ozone injection; and
e) separating the sorbent from the gas stream exiting the dry or semi-dry scrubber.
2. The method as claimed in claim 1 wherein the sorbent is selected from the group consisting of aqueous solution of lime, Ca(OH) 2 , limestone, soda ash; caustic soda, sodium bi carbonate, Natrona, magnesium promoted lime and naturally occurring or synthetically derived carbonates, bicarbonates, hydroxides of alkali or alkaline earth metals and mixtures thereof.
3. The method as claimed in claim 1 wherein the sorbent is more than one sorbent.
4. The method as claimed in claim 1 wherein the gas stream containing contaminants is an exhaust gas.
5. The method as claimed in claim 4 wherein the exhaust gas is from a device selected from the group consisting of a boiler, an engine, a metallurgical furnace, cement kiln, lime sintering kiln and palletizing kiln.
6. The method as claimed in claim 5 wherein the device is powered by a fuel selected from the group consisting of coal, fossil fuel, solid waste, biomass and heavy hydrocarbon feedstock.
7. The method as claimed in claim 1 wherein the contaminants are selected from the group consisting of nitrogen oxides, sulfur oxides, acid gases, particulates, and heavy metals.
8. The method as claimed in claim 1 wherein the dry scrubber is a dry sorbent injector scrubber.
9. The method as claimed in claim 1 wherein the semi-dry scrubber is a spray dryer adsorber scrubber.
10. The method as claimed in claim 1 wherein the contaminants oxidize in the remaining 80% to 85% height or volume of the dry or semi-dry scrubber.
11. The method as claimed in 10 wherein nitrogen oxides are oxidized to their pentavalent form in the remaining 80% to 85% height or volume of the dry or semi-dry scrubber.
12. The method as claimed in claim 1 wherein the ozone is added to the dry or semi-dry scrubber in an amount of greater stoichiometry than the amount of nitrogen oxides present in the gas stream containing contaminants.
13. The method as claimed in claim 12 wherein the ozone is fed in a stoichiometric ratio of 1.5 moles of ozone per mole of nitrogen oxide and 0.5 moles of ozone per mole of nitrogen dioxide in the gas stream containing contaminant.
14. The method as claimed in claim 1 wherein the ozone is injected into the dry or the semi-dry scrubber in a range of about 2% to about 12% by weight ozone in oxygen.
15. The method as claimed in claim 1 wherein the temperature range for the ozone when it is injected into the dry or semi-dry scrubber is from 37.7° C. to 121.1° C.