Catalytic denitrification control process and system for combustion flue gases

• US 5,047,220 A
• Filed: 03/27/1989
• Issued: 09/10/1991
• Est. Priority Date: 03/27/1989
• Status: Expired due to Term

• Current Assignee: Foster Wheeler Energy Applications Incorporated
• Original Assignee: Foster Wheeler Energy Limited (John Wood Group PLC)
• Inventors: Polcer, John
• Primary Examiner(s): HELLER, GREGORY
• Application Number:
  US07/329,143
• Time in Patent Office: 897 Days
• Field of Search: 423/239, 423/239 A, 423/235, 423/235 D, 422/62
• US Class Current: 423/239.1
• CPC Class Codes: B01D 53/8625 Nitrogen oxides
• CPC Class Codes: Y02A 50/20 Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

A control process and system for catalytic denitrification of NO_x containing flue gases derived from a fuel combustion unit such as a gas turbine by ammonia addition to the flue gas upstream of a catalytic denitrification unit. The ammonia addition rate is controlled based on a basic signal which is generated based on functional parameters including the fuel being burned, its combustion temperature, flue gas flow rate, ammonia flow rate and the catalytic activity, so as to inject initially into the flue gas stream less ammonia than is theoretically required. Then the NO_x concentration in the exhaust gas downstream of the catalytic unit is compared with the appropriate standard, the ammonia quantity initially being added is further adjusted until the NO_x concentration is gas emitted to the atmopshere is reduced sufficiently to meet local clean air standards while avoiding unsatisfactory excess ammonia injection and system oscillation.

Claims

1. A process for controlling the catalytic denitrification of flue gases by ammonia addition to the flue gas, said process comprising:

(a) withdrawing from a combustion process a flue gas stream containing at least about 20 volume parts NO_x per million of flue gas, and controllably adding ammonia gas to said flue gas stream;

(b) passing the flue gas and ammonia mixture through a catalytic denitrification unit containing a denitrification catalyst material and reducing the NO_x concentration in the flue gas;

(c) obtaining a control signal based on process parameter signals including the volume flow rate of said flue gas, and determining the quantity of ammonia initially added to the flue gas so that it is less than the amount theoretically required to reduce all of the NO_x in the flue gas;

(d) obtaining a trim signal based on comparing the NO_x concentration measured in the flue gas downstream of the catalytic dentrification unit and a desired NO_x concentration; and

(e) providing additional ammonia injection based on the trim signal by adjusting the ammonia addition flow rate as needed to provide the desired reduced NO_x concentration in the flue gas being emitted to the atmosphere and to avoid excess ammonia injection and system oscillation.

2. The control process of claim 1, wherein the ammonia flow is diluted with air to provide an air-ammonia volume ratio in the range of 15:

1 to 50;

1.

3. The control process of claim 1, wherein the ammonia injection is located upstream of the catalytic unit by a distance sufficient to provide an elapsed time for the flue gas flow of 0.3-1 second.

4. The control process of claim 1, wherein the exhaust gas temperature upstream of the denitrification unit is cooled to 500-1000°

F.

5. The control process of claim 1, wherein the flue gas is exhausted from a gas turbine and the basic signal includes fuel flow rate to an afterburner provided in the gas turbine exhaust casing upstream of the ammonia injection location.

6. The control process of claim 1, wherein the flue gas is passed through a honeycomb type catalytic denitrification unit containing a catalyst material impregnated therein.

7. The control process of claim 6, wherein the catalyst material includes titanium oxide, vanadium oxide, or platinum.

8. The control process of claim 1, wherein the basic signal includes parameters of flue gas flow rate and nitrous oxide content, and the ammonia temperature, pressure and flow rate.

10. The control process of claim 1, wherein the initial quantity of ammonia added is 80-85% of the amount theoretically required.

11. The control process of claim 10, wherein the process parameter signals, upon which the control signal is based, further include combustion temperature, fuel composition and catalytic activity in the catalytic denitrification unit.

9. A process for controlling the catalytic denitrification of exhaust gas from a gas turbine by ammonia addition to the exhaust gas, said process comprising:

(a) withdrawing from a gas turbine an exhaust gas stream containing at least about 20 volume parts NO_x per million parts of exhaust gas, and controllably injecting an ammonia-containing gas stream into said exhaust gas stream so that the amount of ammonia is less than the amount theoretically required to reduce all of the NO_x in the exhaust gas;

(b) passing said exhaust gas and ammonia mixture through a honeycomb type catalytic denitrification unit containing a denitrification catalyst, and initially reducing NO_x concentration of the exhaust gas;

(c) generating a basic control signal based on process parameter signals of exhaust gas flow rate and NO_x content, and the ammonia temperature, pressure and flow rate;

(d) providing a trim signal based on comparing said basic signal with NO_x concentration of the exhaust gas at a location downstream of said catalytic denitrification unit and desired NO_x concentration; and

(e) providing additional ammonia injection based on the trim signal by adjusting the ammonia injection rate as needed to provide the desired reduced NO_x concentration in the turbine exhaust gas being emitted to the atmosphere and to avoid excess ammonia injection and system oscillation.