The Babcock & Wilcox Company

Mcdermott Technology, Inc.

Other

Wadie F Gohara

Thomas W Strock

Kevin J Rogers

Dennis W Johnson

George B Watson

Randy J Reynolds

Steve Feeney

Robert B Myers

Steven Feeney

Fred C Owens, Ii

John Ronald Cline

William H Hall

Dennis K McDonald

Norman D Nelson

Paul J Williams

Edward J Piaskowski

Melvin E Murphy

Denis W Johnson

David A Forrester

A high velocity absorber has a lower larger diameter tank section for receiving a slurry at a liquid level in the. tank section, an upper smaller diameter absorber section where liquid scrubbing agent is mingled with flue gas from which impurities are to be absorbed, and a low pressure drop inlet assembly having a transition structure between the tank section and the absorber section for closing a gas flow path and a liquid flow path between the tank section and the absorber section. An inlet housing is connected to and communicates with the transition structure for inlet of flue gas into the transition structure between the tank section and the absorber section.

Low pressure drop inlet design to promote good gas flow patterns in high velocity absorbers

A low pressure drop inlet arrangement for an absorber having straight walls has a perforated tray positioned above the gas inlet opening between the walls of the absorber. A ring around the outer edge of the tray lacks perforations, or the perforations are covered. A drip ledge may be positioned on the bottom of the tray around the inner edge of the non-perforated ring. Baffles are positioned over the tray as well. The baffles may extend between the walls of the absorber, or they may only occupy the space over the perforations in the tray and the size of the tray perforations may be varied to control the overall pressure drop. An absorber made in accordance with the invention experiences a low pressure drop at the gas inlet opening.

Low pressure drop inlet for high velocity absorbers with straight tanks

A method and device for using the density control water to continuously flush the oxidation air header and the sparge pipes in a flue gas wet scrubber agitation tank. The density control line is routed to the elevation where the control valve is located. A U-shaped trap is located between the control valve and air sparge header such that the density control water joins the humidified oxidation air. A liquid layer forms on the floor of the header and is moved toward the distant side of the header by the motion of the air passing on top of the liquid layer and by the continuous flow of water. The bottom section of the main header is perforated to allow the flowing water to exit the header into the tank and flush any accumulated solids that might penetrate the header through the air holes. The air holes are located in a section at a minimum of five degrees off the floor and maximum of one hundred eighty degrees off the header bottom and preferably at forty-five degrees. The distant end of the header has an opening located close to the header floor to provide an outlet for the flushed solids and prevents the formation of back waves in the header.

Method and apparatus for air sparged slurry tanks

An improvement in a center inlet type scrubber that retrofit the scrubber with a perforated tray made up of rectangular or partially rectangular sections supported on beam supports in the annulus of the scrubber. The supports can be modified to form turning vanes or additional turning vanes can be employed. One or more perforated trays may be installed in the annulus to help correct the problem.

Retrofit of a center inlet type scrubber with absorption/gas

A device for using the density control water to continuously flush the oxidation air header and the sparge pipes in a flue gas wet scrubber agitation tank. The density control line is routed to the elevation where the control valve is located. A U-shaped trap is located between the control valve and air sparge header such that the density control water joins the humidified oxidation air. A liquid layer forms on the floor of the header and is moved toward the distant side of the header by the motion of the air passing on top of the liquid layer and by the continuous flow of water. The bottom section of the main header is perforated to allow the flowing water to exit the header into the tank and flush any accumulated solids that might penetrate the header through the air holes. The air holes are located in a section at a minimum of five degrees off the floor and maximum of one hundred eighty degrees off the header bottom and preferably at forty-five degrees. The distant end of the header has an opening located close to the header floor to provide an outlet for the flushed solids and prevents the formation of back waves in the header.

Apparatus for air sparged slurry tanks

An air sparger assembly for a flue gas desulfurization wet scrubber agitation tank that eliminates the need for a mixer and reduces the amount of piping required. The air sparge pipes are arranged to be concentric with the agitation tank. A single main header provides air to the air sparge pipes. The discrete location of the air discharge holes in the sparge pipes utilizes the buoyant energy of the oxidation air to mix the slurry in the agitation tank.

Wet scrubber oxidation air sparger arrangement

An apparatus to mix a slurry mixture with an oxidization air within a reaction tank of a wet scrubber spray tower of a flue gas desulfurization system for a furnace. The apparatus improves the contact between forced oxidization air and slurry mixture within the reaction tank.

Apparatus for mixing a tank and improving air/liquid contact in an

A system and method for distributing, injecting, and dispersing a sorbent mixture of sorbent and compressed filtered flue gas into the combustion furnace portion of a boiler furnace. Prior to injection into the combustion furnace, the sorbent mixture is heated with steam and distributed within the combustion furnace through a plurality of injection tubes having their ends arranged in a grid and oriented substantially toward the combustion furnace flue gas flow.

Apparatus for the injection distribution and dispersion of sorbent in a

A system for removing SO.sub.2, NO.sub.2, and other contaminants from flue gases uses hydrogen peroxide (H.sub.2 O.sub.2) as the reagent to convert the oxides of sulfur and some of the oxides of nitrogen (NO, NO.sub.2, etc.) to more stable oxidation states. Acids formed as a result of this conversion, namely sulfuric acid (H.sub.2 SO.sub.4) and nitric acid (HNO.sub.3) can then be neutralized with limestone or, alternatively, the sulfuric and nitric acids can be collected and processed for sale as an industrial product.

Hydrogen peroxide for flue gas desulfurization

A high velocity gas absorber for desulfurization of flue gas has a uniquely formed awning and inlet having an inclined awning extending upwardly from the inlet at an angle between 5 and 20 degrees and having strategically placed triangularly shaped gutters therealong for drawing the liquid flow across the inlet while the inlet bottom plate is inclined downward at an angle of approximately 60 degrees of the inlet horizontal bottom plate into the liquid of the absorber's recirculation tank to reduce splash into the inlet.

Inlet awning for high velocity absorbers

A wet flue gas desulfurization scrubbing tower has means therein for evenly distributing the flue gas flowing through the tower for more efficient treatment therein including a ring plenum for evenly exhausting the flue gas around the periphery of the tower through a series of differently sized openings and a centrally located annular opening for evenly exhausting the flue gas to the center of the tower.

Wet flue gas scrubber having an evenly distributed flue gas inlet

An integrated spray header tray assembly (18) for a wet flue gas desulfurization spray tower (10) wherein a series of spray headers (22) having opposed nozzles (26) for desulfurizing spray are located along a perforated plate (24) acting as one set of baffles (30) while a second set of baffles (32) positioned perpendicularly thereto forms a baffled tray with the perforated plate (24) and headers (22) while allowing the introduction of desulfurizing spray from the header nozzles (22) parallel to the perforated tray (24).

Growing community of inventors

Barberton, OH, United States of America

Wadie F Gohara