Use of gas turbine heated fluid for reductant vaporization
US-2017292424-A1 · Oct 12, 2017 · US
US10773252B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10773252-B2 |
| Application number | US-201815937896-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 28, 2018 |
| Priority date | Mar 30, 2017 |
| Publication date | Sep 15, 2020 |
| Grant date | Sep 15, 2020 |
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A catalyst for treating an exhaust gas comprising SO2, NOx and elemental mercury in the presence of a nitrogenous reductant comprises a composition containing oxides of: (i) Molybdenum (Mo) and/or Tungsten (W); (ii) Vanadium (V); (iii) Titanium (Ti), and (iv) an MFI zeolite, wherein the composition comprises, based on the total weight of the composition: (i) 1 to 6 wt % of MoO3 and/or 1 to 10 wt % WO3; and (ii) 0.1 to 3 wt % V2O5, and (iii) 48.5 to 94.5 wt % TiO2; and (iv) 35 to 50 wt % MFI zeolite.
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The invention claimed is: 1. A catalyst for treating an exhaust gas comprising SO 2 , NO x and elemental mercury in the presence of a nitrogenous reductant, the catalyst comprising a composition containing oxides of: (i) Molybdenum (Mo) and/or Tungsten (W); (ii) Vanadium (V); (iii) Titanium (Ti); and (iv) an MFI zeolite, wherein the composition comprises, based on the total weight of the composition: (i) 1 to 6 wt % of M o O3 and/or 1 to l0 wt % WO 3 ; and (ii) 0.1 to 3 wt % V 2 O 5 ; and (iii) 48.5 to 94.5 wt % TiO 2 ; and (iv) 35 to 50 wt % MFI zeolite. 2. The catalyst according to claim 1 , wherein the composition does not comprise phosphorus. 3. The catalyst according to claim 1 , wherein the composition consists of the MFI zeolite and the oxides of Mo, W, V, and Ti. 4. The catalyst according to claim 1 , wherein the catalyst is a plate catalyst. 5. The catalyst according to claim 1 , wherein the MFI zeolite is an H-MFI zeolite. 6. The catalyst according to claim 1 , wherein the MFI zeolite is an H-ZSM-5 zeolite. 7. A method for treating an exhaust gas comprising SO 2 , NO x and elemental mercury, the method comprising: contacting a flow of exhaust gas with the catalyst of claim 1 in the presence of a nitrogenous reducing agent to thereby provide a treated exhaust gas. 8. The method according to claim 7 , wherein the nitrogenous reducing agent is ammonia, hydrazine or an ammonia precursor selected from the group consisting of urea ((NH 2 ) 2 CO), ammonium carbonate, ammonium carbamate, ammonium hydrogen carbonate and ammonium formate. 9. The exhaust system of claim 8 , wherein the combustion source is a furnace or a boiler, of a coal or oil power plant, a cement plant or a waste incinerator. 10. A exhaust system for a combustion source for treating an exhaust gas comprising SO 2 , NO x and elemental mercury, the system comprising a conduit for carrying a flowing exhaust gas, a source of nitrogenous reductant, a catalyst according to claim 1 disposed in a flow path of the exhaust gas and means for metering nitrogenous reductant into a flowing exhaust gas upstream of the catalyst. 11. The exhaust system according to claim 10 , the system further comprising a wet or a dry scrubber for recovering oxidized mercury from the treated exhaust gas.
not in framework positions · CPC title
containing arsenic, antimony, bismuth, vanadium, niobium tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
Tungsten · CPC title
Molybdenum · CPC title
Titanium · CPC title
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