초록 ▼

Two new classes of catalysts for the removal of heavy metal contaminants, especially mercury (Hg) from effluent gases. Both of these classes of catalysts are excellent absorbers of HCl and Cl2 present in effluent gases. This adsorption of oxidizing agents aids in the oxidation of heavy metal contami

Two new classes of catalysts for the removal of heavy metal contaminants, especially mercury (Hg) from effluent gases. Both of these classes of catalysts are excellent absorbers of HCl and Cl2 present in effluent gases. This adsorption of oxidizing agents aids in the oxidation of heavy metal contaminants. The catalysts remove mercury by oxidizing the Hg into mercury (II) moieties. For one class of catalysts, the active component is selected from the group consisting of iridium (Ir) and iridum-platinum (Ir/Pt) alloys. The Ir and Ir/Pt alloy catalysts are especially corrosion resistant. For the other class of catalyst, the active component is partially combusted coal or “Thief” carbon impregnated with Cl2. Untreated Thief carbon catalyst can be self-activating in the presence of effluent gas streams. The Thief carbon catalyst is disposable by means of capture from the effluent gas stream in a particulate collection device (PCD).

대표청구항 ▼

The embodiment of the invention in which an exclusive property or privilege is claimed is defined as follows: 1. A method for preparing a catalyst for the oxidation of mercury in an effluent stream comprising: a. removing partially combusted coal from a coal fired combustion source, wherein the par

The embodiment of the invention in which an exclusive property or privilege is claimed is defined as follows: 1. A method for preparing a catalyst for the oxidation of mercury in an effluent stream comprising: a. removing partially combusted coal from a coal fired combustion source, wherein the partially combusted coal contains between approximately 20 wt. % and 80 wt. % ash and has a surface area of approximately 10 m2/g to 300 m2/g; b. treating the partially combusted coal with a halogen to obtain a catalyst for the oxidation of mercury, wherein the catalyst has a final halogen concentration of about 1 wt. % to 10 wt. %, and wherein the treatment involves contacting the partially combusted coal with a gas phase containing chlorine gas, bromine liquid, bromine vapor or combinations thereof, or treating the partially combusted coal with hydrochloric or hydrobromic acid or combination thereof. 2. The method according to claim 1 wherein the partially combusted coal has a surface area of approximately 220 m2/g. 3. The method according to claim 1 further comprising the step of placing the catalyst for the oxidation of mercury on a stainless steel support.