Abstract: A heat exchanger for a regenerative thermal oxidizer is described which includes at least one heat exchange column provided with a multi-layer of packing material including at least one layer of randomly packed and specially shaped and sized particles, each particle being formed of a high temperature stable material and preferably having a cylindrical outer wall and internal reinforcing vanes extending from the cylindrical outer wall to the center of the particle, and at least one layer of structured monolithic media having a plurality of flow passages in the direction of gas flow through the column.

Abstract: A regenerative thermal oxidizer in which contaminated air is first passed through a hot heat-exchange bed and into a communicating high temperature oxidation (combustion) chamber, and then through a relatively cool second heat exchange bed. The apparatus includes a number of internally insulated, ceramic filled heat recovery columns topped by an internally insulated combustion chamber. From the combustion chamber, the air flows vertically downward through another column containing heat exchange media, thereby storing heat in the media for use in a subsequent inlet cycle when the flow control valves reverse. Temperature is sensed within the bed of heat exchange media in order to monitor the temperature profile and control a bypass of hot combustion gases should the temperature exceed a predetermined level.

Abstract: Regenerative thermal oxidizer in which a gas such as contaminated air is first passed through a hot heat-exchange bed and into a communicating high temperature oxidation (combustion) chamber, and then through a relatively cool second heat exchange bed. The apparatus includes a number of internally insulated, ceramic filled heat recovery columns topped by an internally insulated combustion chamber. Process air is fed into the oxidizer through an inlet manifold containing a number of hydraulically or pneumatically operated flow control valves (such as poppet valves). The air is then directed into the heat exchange media which contains "stored" heat from the previous recovery cycle. The process air is heated to near oxidation temperatures. Oxidation is completed as the flow passes through the combustion chamber, where one or more burners are located. The gas is maintained at the operating temperature for an amount of time sufficient for completing destruction of the VOC's.

Abstract: A catalytic regenerative oxidizer (18) comprises a closed casing (24) having upper and lower ends, an input port (20) at the lower end and an output port (22) at the upper end. The casing contains a plurality of stacked layers or beds, including upper (34), lower (32), and central beds (40) of silica gravel or the like. Two catalyst layers (36, 38) are provided in the stack, one between the lower and central gravel beds, and the other between the upper and central gravel beds. A heating element (42) is situated in the central bed, for maintaining at least one of the catalyst layers at an activation temperature in the range of about 500-1000 deg.F. The catalyst layers are formed by a multiplicity of ceramic pellets on which is deposited a catalyst material, such as precious metal. The contaminated gas stream enters the casing through the lower port and passes vertically through the stacked beds and layers.

Abstract: A regenerative bed incinerator 10 is provided with a gas recirculation duct 80 through which a controlled amount of incinerated process exhaust gases 7 are recirculated to the regenerative bed incinerator 10 to again pass through the combustion zone within the bed 14 housed therein so as to improve overall hydrocarbon destruction efficiency without exceeding permissible temperature limits.