Process for thermal VOC oxidation
AssigneeW. R. Grace & Co.-Conn.
InventorsCarmo J. Pereira, Rodney J. Schwartz
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Abstract
A method and apparatus for reducing the emissions from a thermal oxidizer for volatile organic compounds (VOC) containing waste gases. The waste gas is treated in a thermal reactor and either before, in or after the thermal reactor the waste gas is contacted with a catalyzed surface device in the gas stream within the thermal oxidizer. The catalyzed surface device has a catalyzed surface which contacts the waste gas and further oxidizes the waste gas.
Claims10
A method for the thermal oxidation of Volatile Organic Components (VOCs) in waste gas from industrial plants, the method comprising (a) providing a thermal oxidizer comprising at least one flow distribution means having at least one catalytically-active surface;
- (b) contacting waste gas with said catalytically-active surface in the oxidizer;
- and (c) oxidizing the VOCs in the waste gas, wherein said at least one catalytic-active surface has a surface area, S, such that when a volumetric flow rate of waste gas passing through the flow distribution means is Q, the ratio of Q/S is at least 0.025 ft/sec and wherein the flow distribution means is at least one device selected from the group consisting of turning vanes, flow mixers, flow straighteners and flow diverter devices.
In a method for the thermal oxidation of Volatile Organic Compounds ("VOCs") in waste gas from industrial plants wherein waste gas is contacted with a thermal oxidizer to oxidize the VOCs in the waste gas, the improvement comprising (a) providing within the thermal oxidizer at least one flow distribution means having at least one catalytically-active surface;
- (b) contacting the waste gas with said catalytically-active surface in the oxidizer;
- and (c) oxidizing the VOCs in the waste gas, wherein said at least one catalytically-active surface has a surface area, S, such that when a volumetric flow rate of waste gas passing through the flow distribution means is Q, the ratio of Q/S is at least 0.025 ft/sec and wherein the flow distribution means is at least one device selected from the group consisting of turning vanes, flow mixers, flow straighteners and flow diverter devices.
Dependencies are inferred from the claim text.