Method for controlling additive feed in a boiler system

• US 4,793,268 A
• Filed: 11/27/1987
• Issued: 12/27/1988
• Est. Priority Date: 11/27/1987
• Status: Expired due to Fees

• Current Assignee: Apollo Technologies International Corporation 130 Speedwell Avenue Morris Plains New Jersey
• Original Assignee: Apollo Technologies Incorporated (Ecolab, Inc.)
• Inventors: Pepe, William C., Kukin, Ira
• Primary Examiner(s): Favors, Edward G.
• Application Number:
  US07/125,926
• Time in Patent Office: 396 Days
• Field of Search: 236/15 E, 110/342, 110/343, 110/344, 110/345, 122/448 R, 122/448 B, 44/1 SR
• US Class Current: 110/343
• CPC Class Codes: F23J 7/00 Arrangement of devices for supplying chemicals to fire
• CPC Class Codes: F23N 1/082 using electronic means
• CPC Class Codes: G05D 11/131 by measuring the values related to the quantity of the individual components G05D11/139 takes precedence

Abstract

The method of operation of a boiler system to which an additive is to be fed at a controlled rate and in which the optimal additive rate depends upon a plurality of changing parameters of the boiler system, in which the relationship between each of those parameters and the optimal additive feed rate is determined, the relevant parameters are sensed during the operation of the system, their effects on optimum additive feed are computed in accordance with said relationships and combined on a continuous basis to produce a control signal representative of the desired rate of additive feed, and controlling the additive feed in accordance therewith, all preferably continuously.

Claims

1. A method of controlling the feed of an additive to a fuel-burning boiler system which comprises:

(a) detecting a plurality of boiler operational parameter values and converting said values to corresponding boiler parameter signals;

(b) converting each of said boiler parameter signals to a control signal in accordance with its own characteristic conversion program;

(c) combining each of said control signals in accordance with a predetermined schedule;

(d) detecting the existing additive feed and producing a corresponding computed additive feed signal, and

(e) comparing said existing additive feed signal and said computed additive feed signal and modifying the additive feed to cause it to conform to said computed additive feed signal if necessary.

2. The method of claim 1, in which some of said boiler parameter signals are converted to corresponding control signals in real time and others of said boiler parameter signals are combined over a predetermined period of time before being converted into a corresponding control signal.

3. In the method of either of claims 1 or 2, sensing when the boiler system is not operating within a normal range and (a) producing a computed additive feed signal corresponding to that boiler operation without regard to the other boiler parameter signals and (b) maintaining that computed additive feed signal, and causing the additive feed to correspond thereto, for a predetermined period of time.

4. The method of either of claims 1 or 2, in which desired ones of said feed signals are displayed for operator monitoring.

5. The method of either of claims 1 or 2, in which one of said parameters is a sulfur trioxide content parameter which involves separate value determinations by (a) the output of a sulfur trioxide monitor, (b) the output of an acid dew point meter, and (c) a theoretical computation based upon other boiler operational parameters, with the effective SO₃ content signal being produced by combining those three values in a predetermined fashion.

6. The method of either of claims 1 or 2, in which one of said parameters is a sensed load parameter and in which, if the sensed load parameter is at a predetermined level lower than normal, the computed additive feed signal is increased by a predetermined amount before being compared with the existing additive feed signal.

7. The method of either of claims 1 or 2, in which said predetermined schedule for combining each of said control signals to produce said computed additive feed signal includes using as factors heat value, fuel flow, an excess air-fuel flow factor and SO₃ content.

8. The method of either of claims 1 or 2, in which said predetermined schedule for combining each of said control signals to produce said computed additive feed signal includes using as factors heat value, fuel flow, an excess air-fuel flow factor and SO₃ content and using as an additive a factor reflecting the degree of use of generated steam for pre-heating purposes.

9. The method of either of claims 1 or 2, in which a plurality-of different additives are involved with each additive having its own set of characteristic programs for converting boiler parameter signals to corresponding control signals and each has its own predetermined schedule for combining its respective control signals to produce its own computed additive feed signal, with the feed of each additive being individually controlled in accordance therewith.

10. The method of either of claims 1 or 2, in which additive is fed simultaneously to a plurality of different boiler systems, the method of the parent claim being carried out individually for each such boiler system.

11. A method of controlling the feed of an additive to a fuel-burning boiler system which comprises:

(a) detecting a plurality of boiler operational parameter values, said parameters being members of the group consisting of load, fuel feed, amount and temperature of combustion air, sulfur trioxide content, exit gas temperature and effluent opacity, and converting said values to corresponding boiler parameter signals;

(b) converting each of said boiler parameter signals to a control signal in accordance with its own characteristic conversion program;

(c) combining each of said control signals in accordance with a predetermined schedule;

(d) detecting the existing additive feed and producing a corresponding computed additive feed signal, and

(e) comparing said existing additive feed signal and said computed additive feed signal and modifying the additive feed to cause it to conform to said computed additive feed signal if necessary.

12. The method of claim 11, in which some of said boiler parameter signals are converted to corresponding control signals in real time and others of said boiler parameter signals are combined over a predetermined period of time before being converted into a corresponding control signal.

13. In the method of either of claims 11 or 12, sensing when the boiler system is not operating within a normal range and (a) producing a computed additive feed signal corresponding to that boiler. operation without regard to the other boiler parameter signals and (b) maintaining that computed additive feed signal, and causing the additive feed to correspond thereto, for a predetermined period of time.

14. The method of either of claims 11 or 12, in which desired ones of said feed signals are displayed for operator monitoring.

15. The method of either of claims 11 or 12, in which the sulfur trioxide content parameter involves separate value determinations by (a) the output of a sulfur trioxide monitor, (b) the output of an acid dew point meter, and (c) a theoretical computation based upon other boiler operational parameters, with the effective SO₃ content signal being produced by combining those three values in a predetermined fashion.

16. The method of either of claims 11 or 12, in which, if the sensed load parameter is at a predetermined level lower than normal, the computed additive feed signal is increased by a predetermined amount before being compared with the existing additive feed signal.

17. In the method of claim 16, sensing when the boiler system is not operating within a normal range and (a) producing a computed additive feed signal corresponding to that boiler operation without regard to the other boiler parameter signals and (b) maintaining that computed additive feed signal, and causing the additive feed to correspond thereto, for a predetermined period of time.

18. The method of claim 16, in which the sulfur trioxide content parameter involves separate value determinations by (a) the output of a sulfur trioxide monitor, (b) the output of an acid dew point meter, and (c) a theoretical computation based upon other boiler operational parameters, with the effective SO₃ content signal being produced by combining those three values in a predetermined fashion.

19. The method of claim 16, in which said predetermined schedule for combining each of said control signals to produce said computed additive feed signal includes using as factors heat value, fuel flow, an excess air-fuel flow factor and SO₃ content.

20. The method of either of claims 11 or 2, in which said predetermined schedule for combining each of said control signals to produce said computed additive feed signal includes using as factors heat value, fuel flow, an excess air-fuel flow factor and SO₃ content

21. The method of either of claims 11 or 12, in which said predetermined schedule for combining each of said control signals to produce said computed additive feed signal includes using as factors heat value, fuel flow, an excess air-fuel flow factor and SO₃ content and using as an additive a factor reflecting the degree of use of generated steam for pre-heating purposes.

22. The method of either of claims 11 or 12, in which a plurality of different additives are involved with each additive having its own set of characteristic programs for converting boiler parameter signals to corresponding control signals and each has its own predetermined schedule for combining its respective control signals to produce its own computed additive feed signal, with the feed of each additive being individually controlled in accordance therewith.

23. The method of either of claims 11 or 12, in which additive is fed simultaneously to a plurality of different boiler systems, the method of the parent claim being carried out individually for each such boiler system.