Catalytic reduction apparatus for NO.sub.X reduction

• US 5,738,024 A
• Filed: 04/19/1996
• Issued: 04/14/1998
• Est. Priority Date: 04/19/1996
• Status: Expired due to Term

• Current Assignee: Phillip Winegar
• Original Assignee: Phillip Winegar
• Inventors: Winegar, Phillip
• Primary Examiner(s): Bennett, Henry A.
• Assistant Examiner(s): WILSON, GREGORY A
• Application Number:
  US08/634,775
• Time in Patent Office: 725 Days
• Field of Search: 423/239, 110/345, 422/171, 422/172, 422/175
• US Class Current: 110/345
• CPC Class Codes: B01D 53/8631 Processes characterised by a specific device

Abstract

An apparatus and method for reducing NO_x pollution in flue gas produced by a power plant uses heat exchanger elements having extended surfaces which contain a SCR catalyst, with the heat exchanger elements located in the flue gas stream. Coolant is passed through the heat exchanger elements to cool the catalyst, with a temperature control system used to maintain the catalyst at its optimum temperature such that the maximum conversion of NO_x is achieved. Utilizing the present invention, temperature cycling of the catalyst is avoided, prolonging the life of the catalyst, while at the same time optimizing the efficiency of conversion regardless of variations in the flue gas flow or temperature.

Claims

1. A constant temperature selective catalyst reduction apparatus comprising:

at least one heat exchange element having extended surfaces, an SCR catalyst disposed at least on the extended surfaces thereof,

means for providing a cooling medium to the heat exchange element for removing heat from the catalyst, and

temperature control means for controlling the cooling medium and thereby controlling the temperature of the catalyst, so as to maintain the catalyst at or near a temperature optimum for the conversion of NO_x to nitrogen and water.

2. The catalyst reduction apparatus of claim 1, wherein the SCR catalyst is selected from the group consisting of platinum, vanadium pentoxide, titanium dioxide, zeolites, copper, iron or cerium and combination thereof.

3. The catalyst reduction apparatus of claim 2, further comprising other catalytic materials selected from the group consisting of tungsten, iron, tin, molybdenum, zirconium, chrome or silica and combinations thereof.

4. The catalyst reduction apparatus of claim 1 further comprising a reactive material injected in the flue gas stream to promote conversion of the NO_x to nitrogen and water.

5. The catalyst reduction apparatus of claim 4 wherein the reactive material is ammonia, urea, amines and combinations thereof.

6. The catalyst reduction apparatus of claim 1, further comprising a second heat exchanger, located in the flue gas stream before or after the heat exchange element, to cool the flue gas stream.

7. The catalyst reduction apparatus of claim 1, further comprising a boiler, a fuel and air mixed in the boiler and combusted, to produce the flue gas stream, tubes associated with the boiler for producing steam.

8. The catalyst reduction apparatus of claim 1, wherein the temperature control means comprises a first temperature sensor associated with the flue gas, a second temperature sensor associated with the heat exchange element and a third temperature sensor associated with the cooling medium, a controller for accepting signals from the temperature sensors and to output a signal to control the flow of cool medium through the heat exchange element.

9. The catalyst reduction apparatus of claim 1, wherein temperature control means comprises a first temperature sensor associated with the flue gas, a second temperature sensor associated with the heat exchange element and a third temperature sensor associated with the cooling medium, a controller for accepting signals from the temperature sensors and to output a signal to control the temperature of the cooling medium passing through the heat exchange element.