Automated setup process for metered combustion control systems

• US 9,028,245 B2
• Filed: 11/25/2008
• Issued: 05/12/2015
• Est. Priority Date: 11/25/2008
• Status: Active Grant

• Current Assignee: UTC Fire & Security Corporation (Raytheon Technologies Corporation d/b/a RTX)
• Original Assignee: UTC Fire & Security Corporation (Raytheon Technologies Corporation d/b/a RTX)
• Inventors: Fan, Junqiang, Lelic, Muhidin A.
• Primary Examiner(s): Savani, Avinash
• Assistant Examiner(s): SHIRSAT, VIVEK K
• Application Number:
  US13/127,367
• Publication Number:
  US 20110212404A1
• Time in Patent Office: 2,359 Days
• Field of Search: 431/12, 431/7, 431/4, 431/89, 431/153, 431/2, 431/115, 431/76
• US Class Current: 431/12
• CPC Class Codes: F23N 1/022 using electronic means
• CPC Class Codes: F23N 1/082 using electronic means
• CPC Class Codes: F23N 2223/44 Optimum control
• CPC Class Codes: F23N 2225/18 feedwater temperature
• CPC Class Codes: F23N 2225/19 outlet temperature water heat-exchanger
• CPC Class Codes: F23N 2227/20 Calibrating devices
• CPC Class Codes: F23N 2233/08 with variable speed
• CPC Class Codes: F23N 2235/06 at the air intake
• CPC Class Codes: F23N 2235/14 electromagnetically operated
• CPC Class Codes: F23N 2237/26 oxygen-air ratio
• CPC Class Codes: F23N 2241/04 Heating water
• CPC Class Codes: F23N 5/006 the detector being sensitive to oxygen

Abstract

A method is provided for the automated setup of a metered combustion control system for controlling operation of a boiler combustion system. The automated setup process includes both commissioning and controller tuning, rather than tuning the carbon monoxide and/or oxygen trim controller after the commissioning process has been completed. The oxygen trim controller or the carbon monoxide trim controller is used to identify the air/fuel ratio.

Claims

1. A setup method for a metered combustion control system for controlling operation of a boiler combustion system having a burner, a fuel flow control device and a fuel flow control device controller operatively associated with said fuel flow control device for supplying fuel to said burner and an air flow control device and an air flow control device controller operatively associated with said air flow control device for supplying air to said burner, the method including defining a lower limit air/fuel mass flow ratio and an upper limit air/fuel mass flow ratio at a plurality of selected firing rate points between a minimum firing rate and a maximum firing rate, said setup method comprising:

(a) selecting a first firing rate point as a selected firing rate point;

(b) at an initial setting of the fuel flow control device controller associated with the selected firing rate point, selecting a first setting of the air flow control device controller and incrementally resetting the air flow control device controller;

(c) operating the burner at the selected firing rate point at each air flow control device controller setting in (b) to supply fuel to said burner and supply air to said burner to generate a flue gas and measuring at each air flow control device controller setting;

the mass air flow, the oxygen content in the flue gas, and the carbon monoxide content in the flue gas;

(d) identifying at the selected firing rate point;

a model relating;

the air mass flow to the air flow control device controller setting, a model relating the oxygen content in the flue gas to the air flow control device controller setting, and a model relating the carbon monoxide content in the flue gas to the air flow control device controller setting;

(e) calculating a set of control parameters for an air mass flow rate feedback loop controller, for an oxygen trim feedback loop controller, and for a carbon monoxide trim feedback loop controller;

(f) resetting the air flow control device controller at the first setting and incrementally resetting the fuel flow control device controller;

(g) measuring the fuel mass flow at each fuel flow control device controller setting in (f) and identifying a model relating the fuel flow mass to the fuel flow control device controller setting;

(h) calculating a set of control parameters for a fuel mass flow rate feedback loop controller;

(i) selecting a new firing rate point as a further selected firing rate point;

(j) at an initial setting of the fuel flow control device controller associated with the further selected firing rate point, selecting a first setting of the air flow control device controller and incrementally resetting the air flow control device controller;

(k) operating the burner at the further selected firing rate point at each air flow control device controller setting in (b) to generate a flue gas and measuring at each air flow control device controller setting;

the mass air flow, the oxygen content in the flue gas, and the carbon monoxide content in the flue gas;

(l) identifying and saving a lower limit air/fuel ratio at the further selected firing rate point at which the measured carbon monoxide content in the flue gas is equal to an upper limit carbon monoxide target level;

(m) identifying and saving an upper limit air/fuel ratio at the further selected firing rate point at which the measured carbon monoxide content in the flue gas is equal to a lower limit carbon monoxide target level;

(n) repeating (i) through (m) at a plurality of selected firing rate points between a minimum firing rate and a maximum firing rate; and

(o) calculating a set point air/fuel ratio as the average of the lower limit air/fuel ratio and the upper limit air/fuel ratio at each selected firing rate point of the plurality of selected firing rate points and developing a relationship between the average air/fuel ratio and firing rate between the minimum firing rate and the maximum firing rate, the relationship between the average air/fuel ratio and firing rate between the minimum firing rate and the maximum firing rate being used for operating the boiler combustion system.

2. A method as recited in claim 1 wherein at (l) and (m) a negative feedback control loop is used to identifying the maximum and minimum air flow setpoint at each firing rate.

3. A method as recited in claim 2 wherein the negative feedback control loop comprises a carbon monoxide trim control loop.

4. A method as recited in claim 2 wherein the negative feedback control loop comprises an oxygen trim control loop.

5. A method as recited in claim 1 wherein at (l) and (m), the method includes selectively activating one of a negative feedback oxygen trim control and a negative feedback carbon monoxide trim control for use in identifying the maximum and minimum air flow setpoint at each firing rate.