Dynamic matrix control of steam temperature with prevention of saturated steam entry into superheater

• US 9,217,565 B2
• Filed: 02/07/2011
• Issued: 12/22/2015
• Est. Priority Date: 08/16/2010
• Status: Active Grant

• Current Assignee: Emerson Process Management Power & Water Solutions Incorporated (Emerson Electric Company)
• Original Assignee: Emerson Process Management Power & Water Solutions Incorporated (Emerson Electric Company)
• Inventors: Beveridge, Robert Allen, Whalen, Richard J. Jr.
• Primary Examiner(s): Huson, Gregory
• Assistant Examiner(s): GORMAN, ERIC DAVID
• Application Number:
  US13/022,324
• Publication Number:
  US 20120040299A1
• Time in Patent Office: 1,779 Days
• Field of Search: None
• US Class Current: 1/1
• CPC Class Codes: F01K 13/02 Controlling, e.g. stopping or starting
• CPC Class Codes: F22B 35/004 Control systems for steam generators of nuclear power plants
• CPC Class Codes: F22B 35/18 Applications of computers to steam boiler control

Abstract

A technique of controlling a steam generating boiler system using dynamic matrix control includes preventing saturated steam from entering a superheater section. A dynamic matrix control block uses a rate of change of a disturbance variable, a current output steam temperature, and an output steam setpoint as inputs to generate a control signal. A prevention block modifies the control signal based on a saturated steam temperature and an intermediate steam temperature. In some embodiments, the control signal is modified based on a threshold and/or an adjustable function g(x). The modified control signal is used to control a field device that, at least in part, affects the intermediate steam and output steam of the boiler system. In some embodiments, the prevention block is included in the dynamic matrix control block.

Claims

1. A fuzzifier unit for use in a steam generating boiler system, comprising:

a first input to receive a signal indicative of a magnitude of a difference between a saturated steam temperature and a temperature of intermediate steam generated by the steam generating boiler system that is a once-through boiler system providing a continuous flow of steam within the system to drive a turbine, wherein the temperature of the intermediate steam is determined upstream of a location at which a temperature of output steam is determined, the output steam generated by the steam generating boiler system for delivery to drive the turbine;

a second input communicatively coupling the fuzzifier unit to a dynamic matrix controller that is feed forward or predictive, the second input of the fuzzifier unit to receive a control signal generated by the dynamic matrix controller, wherein the control signal (i) is generated, by the dynamic matrix controller, based on a signal, received as an input by the dynamic matrix controller, that is indicative of a current rate of change of a disturbance variable used in the steam generating boiler system, and (ii) is generated, by the dynamic matrix controller, not based on any input, to the dynamic matrix controller, that is indicative of the temperature of the intermediate steam;

an adjustment routine that adjusts the control signal received at the second input of the fuzzifier unit based on the magnitude of the difference between the saturated steam temperature and the temperature of the intermediate steam; and

an output communicatively coupling the fuzzifier unit to a field device, the output of the fuzzifier unit to provide the adjusted control signal to the field device to control the temperature of the intermediate steam.

2. The fuzzifier unit of claim 1, wherein:

the adjustment routine includes a threshold, and

the control signal is adjusted based on a comparison of the magnitude of the difference between the saturated steam temperature and the temperature of the intermediate steam and the threshold.

3. The fuzzifier unit of claim 2, wherein the threshold is modifiable.

4. The fuzzifier unit of claim 1, wherein the control signal generated by the dynamic matrix controller is further based on the temperature of the output steam and a setpoint corresponding to the temperature of the output steam.

5. The fuzzifier unit of claim 1, wherein the field device is a spray valve.

6. The fuzzifier unit of claim 1, wherein the intermediate steam is provided to a superheater section of the steam generating boiler system.

7. The fuzzifier unit of claim 6, wherein the superheater section is a final superheater section.

8. The fuzzifier unit of claim 1, wherein the adjustment routine is modifiable.

9. The fuzzifier unit of claim 1, wherein:

the signal that is indicative of the magnitude of the difference between the saturated steam temperature and the temperature of the intermediate steam and that is received at the first input of the fuzzifier is generated by a comparator unit; and

the comparator unit and the fuzzifier unit are included in a prevention unit of the steam generating boiler system.

10. The fuzzifier unit of claim 9, wherein:

the prevention unit further includes a steam table to (i) determine the saturated steam temperature based on a current atmospheric pressure, and to (ii) provide a signal indicative of the saturated steam temperature to an input of the comparator unit.

11. The fuzzifier unit of claim 1, wherein the disturbance variable corresponds to at least one of:

a manipulated variable of a first control loop;

a control variable of the first control loop or a second control loop;

a fuel to air ratio;

a damper position;

a furnace burner tilt position;

a steam flow;

an amount of soot blowing;

a damper position;

a power setting;

a fuel to air mixture ratio;

a firing rate;

a spray flow;

a water wall steam temperature;

a load signal corresponding to one of a target load or an actual load of a turbine;

a flow temperature;

a fuel to feed water ratio;

a temperature of output steam;

a quantity of fuel;

or a type of fuel.

12. The fuzzifier unit of claim 1, wherein the adjustment routine adjusts the control signal based on a direction of change of the difference between the saturated steam temperature and the temperature of the intermediate steam.

13. The fuzzifier unit of claim 1, wherein the adjustment routine adjusts the control signal based on a rate of change of the difference between the saturated steam temperature and the temperature of the intermediate steam.

14. The fuzzifier unit of claim 1, wherein the adjustment routine adjusts the control signal by using a multiplier.

15. The fuzzifier unit of claim 14, wherein a value of the multiplier is based on the difference between the saturated steam temperature and the temperature of the intermediate steam.

16. The fuzzifier unit of claim 14, wherein the multiplier is applied to the signal indicative of the magnitude of the difference between the saturated steam temperature and the temperature of the intermediate steam.

17. The fuzzifier unit of claim 2, wherein:

the control signal is adjusted when the magnitude of the difference between the saturated steam temperature and the temperature of the intermediate steam is less than the threshold, and

the control signal is not adjusted when the magnitude of the difference between the saturated steam temperature and the temperature of the intermediate steam is at least one of greater than or equal to the threshold.

18. The fuzzifier unit of claim 8, wherein the adjustment routine is at least one of automatically modifiable or manually modifiable.