The present invention relates generally to the field of gas analysis instrumentation, and more specifically to a combustion gas analyzer.
Industrial processes are used in the manufacture or combustion of various materials. It is often desirable to monitor operation of a process such that the process can be controlled and adjusted accordingly. Exhaust gas from the combustion is vented through a stack.
Combustion analyzers are used to measure the concentrations of a variety of exhaust gases in industrial combustion processes. For example, the exhaust gas in a combustion process consists of by-product and excess gases. The concentrations of exhaust gases, such as oxygen, oxides of nitrogen, sulfur dioxide and carbon monoxide, relate to the combustion efficiency of the process. Exhaust gas concentration measurements enable operators to adjust the amount of fuel supplied to the process to attain an efficient combustion.
Combustion oxygen analyzers are designed to measure the net concentration of excess oxygen in a combustion process. Excess oxygen is the oxygen remaining after all oxygen has been oxidized in the process and is related to the efficiency of the combustion process. An example of such a device is the Oxymitter 4000 manufactured and sold by Rosemount Analytical, Inc. of Orrville, Ohio. Common applications for a combustion oxygen analyzer include: glass furnaces, coking ovens, catalytic crackers, utility coal pulverizers, sulfur paint incinerators, and other industrial incinerators.
The combustion oxygen analyzer includes a sensor cell assembly which is positioned within an exhaust stack or duct which vents the exhaust gas from a combustion chamber. The sensor cell assembly includes a diffusion element and a sensing cell. As the exhaust gas is vented through the stack, it enters the sensor cell assembly and the diffusion element disperses the gas about the sensing cell. An electrical output from the sensor cell is indicative of oxygen concentration. Electrical circuitry in the transmitter reads the sensor cell output and provides an output related to oxygen concentration.
The combustion oxygen analyzer must be periodically calibrated in order to maintain accuracy in measurements. For example, the sensitivity of the sensor cell can drift over time. Calibration is through a process of standardizing the analyzer by determining the deviation between actual oxygen concentration and measured oxygen concentration. The deviation is used to adjust the output of the analyzer to bring it back into calibration. For example, to calibrate an oxygen analyzer, a calibration gas containing a mixture of oxygen and other gases has a known concentration of oxygen and is applied to the sensor cell assembly. The sensor cell assembly senses the concentration of oxygen in the calibration gas. The electrical circuitry provides an output value for the measured oxygen concentration. The measured value of oxygen is compared to the known concentration of oxygen in the calibration gas. A correction factor is calculated and can be applied to all subsequent measurements of the exhaust gas until a future calibration is performed. The correction factor can be stored, for example, in a memory in the transmitter.
In another calibration technique, the electrical circuitry in the transmitter measures impedance of the sensing cell to provide an indication of the accuracy of the sensing cell. An indication that the sensing cell is inaccurate can be used to indicate that calibration is required.
The calibration process typically requires the process to be shut down so that the analyzer can be removed from the stack for application of the calibration gas. Further, in applications where exhaust gas contains a high particle content, the diffusion element can become plugged and damaged. This also requires the industrial process to be shut down so that the diffusion element can be cleaned or replaced. Diffusion element maintenance and other procedures requiring the sensor cell assembly to be removed from service are time consuming and costly.
A combustion gas analyzer for measuring the concentration of a gas constituent in an exhaust gas stream includes a sensor cell assembly which is configured to sense the gas constituent. A filter substantially encloses the sensor cell assembly. A valve assembly is coupled to a conduit which connects to the filter. The conduit is used for supplying a calibration gas or for back washing dust particles in the filter.
Gas analyzer 10 includes sensor cell assembly 14 positioned and supported in stack 18 by flange 16. Stack 18 is a flue or duct of an industrial combustion process and carries exhaust gas 17. Sensor cell assembly 14 includes a diffusion element 15 and sensing cell 11. Diffusion element 15 disperses exhaust gas 17 about the sensing cell 11 as exhaust gas 17 enters the sensor cell assembly 14. Electrical circuitry 12 in transmitter 9 is coupled to and reads an electrical output from the sensor cell 11 indicative of gas concentration. Electrical circuitry 12 provides gas concentration output through output conductors 13.
If there is a high particle content in exhaust gas 17, the diffusion element 15 can become plugged and damaged. To replace diffusion element 15, the industrial process must be shut down so that diffusion element 15 can be cleaned or replaced. As a result of a high particle content in exhaust gas 17, cleaning or replacing diffusion element 15 is time consuming and costly. Further, as discussed in the Background section, the gas analyzer 10 may need to be removed from the stack for calibrating.
Gas analyzer system 51 also includes valve assembly 38 coupled to filter 20 by a conduit 26. Conduit 26 is approximately 0.25 inches in diameter in this example and has a first end 28 connected to filter 20 and a second end 30 connected to an outlet port 32 of valve assembly 38. Conduit 26 can be of any appropriate length such that valve assembly 38 can be positioned at the base of stack 18 where an operator can easily reach it. Valve assembly 38 also includes first inlet port 37 and second inlet port 39 as discussed below.
As filter 20 traps particulate matter in exhaust gas 17, filter 20 may become plugged and prevent a sufficient amount of exhaust gas 17 from entering the sensor cell assembly 14. One technique to clean filter 20 is to shut down the industrial process and clean or replace filter 20 in the stack. This technique of cleaning or replacing filter 20 is time consuming and costly. Therefore, in one aspect of the invention, gas analyzer system 51 includes a blow-back operation to periodically purge and dislodge particulate matter in filter 20.
First inlet port 37 of valve assembly 38 is coupled to pressurized blow-back gas 46 which is set, for example, to more then 10 psig higher than the industrial process. When filter 20 becomes plugged with trapped particulate matter, pressurized blow-back gas 46 is directed from first inlet 37 of valve assembly 38 to exit outlet port 32 through valve assembly 38. Valve assembly 38 can be manually operated, operated by gas analyzer 10 or operated by another controller such as controller 44. Pressurized blow-back gas 46 travels through conduit 26 and enters filter 20. For example, when gas analyzer 10 is a combustion oxygen analyzer, pressurized blow-back gas 46 can consist of dry pressurized air or dry pressurized nitrogen.
In another aspect of the invention, gas analyzer 10 must be periodically calibrated in order to maintain accuracy in gas concentration measurements. Gas analyzer system 51 includes a calibration operation. Gas analyzer 10 is calibrated using calibration gas 48. Second inlet port 39 is coupled to the pressurized calibration gas 48 which is at least 10 psig higher than the industrial process. Valve assembly 38 is operated to allow pressurized calibration gas 48 to enter second inlet 39 of valve assembly 38 and exit outlet port 32. Valve assembly 38 can be manually operated, operated by gas analyzer 10 or operated by another controller such as controller 44. Pressurized calibration gas 46 travels through conduit 26 and floods sensor cell assembly 14. When gas analyzer 10 is a combustion oxygen analyzer, pressurized calibration gas 48 consists of, for example, a mixture of nitrogen and a known concentration of oxygen.
During the calibration process, sensor cell assembly 14 senses the concentration of oxygen in the calibration gas 48. The electrical circuitry 12 provides an output value representative of the measured oxygen concentration. The measured value of oxygen concentration is compared to the known concentration of oxygen in the calibration gas 48. A correction factor is calculated and can be applied to all subsequent measurements of the exhaust gas 17 until a future calibration is performed. The correction factor can be stored, for example, in a memory in transmitter 9.
The particular implementation of valve assembly 38 can be configured as desired.
Regardless if the operation is manually operated, operated by gas analyzer 10 or oeprated by controller 44, each position of valve assembly 38 relates to whether gas analyzer system 51 is purging filter 20, calibrating the sensor cell 11, or doing neither.
Referring back to
In other embodiments of the invention, valve assembly 38 is controlled by controller 44 which stores, for example in a memory of controller 44, pre-programmed time intervals conveyed through input 52. In this configuration, a clock periodically initiates valve assembly 38 to perform the blow-back operation or the calibration operation.
In other embodiments of the invention, controller 44 has a user input 52. In this configuration, input 52 receives a signal from an operator to initiate either a blow-back or calibration operation.
All and/or some of all the above-identified inputs can be included in controller 44. Controller 44 can be a programmable logic controller (PLC), digital controller (DC), a pneumatic controller or any other process controller or comparable device.
At step 56, controller 44 determines whether a calibration is required. If a calibration is required, the process advances to step 58. At step 58, the controller opens the valve assembly 38 to allow calibration gas 48 to flood the sensor cell assembly 14. After calibration gas 48 is allowed to flood the sensor cell assembly 14, the process passes control to step 60. If a calibration is not required in step 56 the process passes control to step 60.
At step 60, controller 44 determines whether a blow-back is required. If a blow-back is required, the process advances to step 62. At step 62, controller 44 opens the valve assembly 38 to allow blow-back gas 46 to purge filter 20. After blow-back gas 46 is allowed to purge filter 20, the method ends. If a blow-back is not required in step 60 the method also ends.
When solenoid valve 34 is open and solenoid valve 36 remains closed, pressurized blow-back gas 46 is allowed to flow through conduit 26 and purge filter 20 as discussed above. When solenoid valve 36 is open and solenoid valve 34 remains closed, pressurized calibration gas 48 is allowed to flow through conduit 26 and flood sensor cell assembly 14 to calibrate the sensor cell 11 as discussed above. Lastly, when solenoid valves 34 and 36 are both closed, blow-back gas 46 and calibration gas 48 are blocked from flowing through conduit 26.
Although the present invention has been described with reference to preferred embodiments, workers skilled in the art will recognize that changes may be made in form and detail without departing from the spirit and scope of the invention.
Number | Name | Date | Kind |
---|---|---|---|
3559491 | Thoen | Feb 1971 | A |
3928161 | McIntyre et al. | Dec 1975 | A |
4094187 | Navarre, Jr. | Jun 1978 | A |
4161883 | Laird et al. | Jul 1979 | A |
4247380 | McIntyre | Jan 1981 | A |
4284487 | Barnes et al. | Aug 1981 | A |
4496433 | Annino et al. | Jan 1985 | A |
4560873 | McGowan et al. | Dec 1985 | A |
4578986 | Navarre | Apr 1986 | A |
4601882 | Benner | Jul 1986 | A |
5178022 | Tomlin | Jan 1993 | A |
5184017 | Tury et al. | Feb 1993 | A |
5376163 | Carlson et al. | Dec 1994 | A |
5507192 | Beaudin | Apr 1996 | A |
5993623 | O'Neill et al. | Nov 1999 | A |
6092430 | Liston et al. | Jul 2000 | A |
6114700 | Blades | Sep 2000 | A |
6120664 | Patel et al. | Sep 2000 | A |
6200819 | Harvey et al. | Mar 2001 | B1 |
6701255 | Batug et al. | Mar 2004 | B2 |
20030216660 | Ben-Oren et al. | Nov 2003 | A1 |
20040074279 | Forrest | Apr 2004 | A1 |
Number | Date | Country |
---|---|---|
0 909 942 | Apr 1999 | EP |
07-260740 | Oct 1995 | JP |
2000-171358 | Jun 2000 | JP |
WO 8701453 | Mar 1987 | WO |
WO 9813687 | Apr 1998 | WO |
Number | Date | Country | |
---|---|---|---|
20040182133 A1 | Sep 2004 | US |