Oil and Gas Process Equipment Burner Emission Prevention Device
An electronically controlled burner management system for oilfield process equipment. The system includes a vessel fluid temperature sensor and electronic valve for interruption of main burner fuel flow. When process equipment is retrofitted with this system total gas production is increased, reduces fugitive emissions of unburned gas, and reduces hazards. The system integrates with existing pneumatic thermostatic control, making it easy to control and can be bypassed in the event of failure.
This application claims priority to and the benefit of the filing of U.S. Provisional Patent No. 63/175,809, filed on Apr. 16, 2021, entitled “Oil and Gas Process Equipment Emission Prevention Device”, and the specification and claims thereof are incorporated herein by reference.
BACKGROUND OF THE INVENTIONThe present invention relates to the field of oil and gas process equipment burner systems, specifically to methods and apparatuses for preventing unignited methane emissions from said burner systems.
Traditional burner control of oil and gas process equipment, such as separators, tank heaters, dehydrators, in-line heaters and other process equipment, is defined here as a burner system with pneumatic thermostatic temperature control means, known in the art as T12 thermostats. It is most common for oil and gas processing equipment to utilize natural gas (primarily composed of methane) as the pneumatic supply gas and as the fuel gas supply consumed by the main burner and standing pilot flame. These pneumatic thermostats use a thermal expansion rod in direct contact with vessel contained fluid. When the contained fluids cools to point lower than the pneumatic thermostat setpoint, the thermal expansion rod cools proportionally and contracts, opening a valve to supply control gas pressure to a pressure-open valve. This pressure-open valve is responsible for the fuel gas supply to a main burner, which is ignited by a standing pilot flame. Once fuel gas is sent to the main burner, the heat transfer rate is increased, the fluid temperature rises, the thermal expansion rod expands, and control gas pressure to the pressure-open valve is terminated. This process is continued indefinitely in maintaining vessel temperature.
The process and equipment discussed above, if performing properly, is effective in maintaining vessel temperature. This reliability coupled with the simplicity of operation and simplicity of maintenance of traditional burner control, has driven mass deployment in today's oil and gas fields. Additionally, electronic burner management systems and auto-igniters are a relatively recent invention and with active process equipment dating as far back as the 1950's or further, traditional burner control are the majority of burner control systems in today's oil and gas fields.
The short coming of traditional burner control is the system's complete in-ability to recognize or solve the extinguishment of the standing pilot. Extinguishment of the standing pilot can be caused by numerous conditions. Examples are: liquid can condense in the pilot fuel gas line causing a momentary obstruction in the pilot orifice while exiting the orifice; the condensed fluid can also freeze when ambient temperatures are low enough causing the halt of pilot fuel gas flow; solid particulates can plug the small pilot orifice; strong gusts of wind can blow the pilot flame out; or other scenarios not mentioned. Once the pilot flame is extinguished, the system cannot recognize such, and when vessel temperature cools to a point that fuel gas is supplied to the main burner, unignited fuel gas is vented from the main burner uncontrollably until manual intervention to relite the standing pilot flame. With the remoteness of some locations, manual intervention can be delayed by periods of days. With the large size of process equipment burners, substantial volumes of fuel gas (primarily methane) can be emitted to the atmosphere increasing the world's greenhouse gas concern. This short coming not only creates a serious emission issue, but the fact that substantial amounts of fuel gas are essentially lost forever, a considerable loss of revenue can be experienced during the lifetime of a producing oil or gas well.
There are currently marketed burner management control systems and auto-igniters that can address this emission issue, and re-light the pilot or act as the ignition source for the main burner. Inherent issues lie within these products that cause resistance in wide deployment into a vast market with legitimate needs. One such issue is the added complexity these systems add to the burner system. As described above, traditional burner control is mechanical and simple. Additionally, technicians have more experience with traditional burner control and pneumatic gas systems in general. The addition of igniters, flame sensors, electrical harnesses and other required components, increase complexity during maintenance. Furthermore, marketed burner management systems and auto-igniters have the issue of introducing the dependency of the process equipment for vessel temperature. For example, if the battery bank has run down or an electrical component has failed, the equipment has no capability of re-introducing heat into the vessel. The remoteness of locations and the inexperience of technicians with electrical automation cause for real issues, especially during winter months. Another, and perhaps the larger source of resistance to widely addressing the market issue, is the cost of these complex units in both cost of goods sold and in installation. Well economics on many low producing wells does not allow for the purchase of these products. This issue is especially apparent in older, existing locations. Original Equipment Manufacture (OEM) installation of burner management systems and auto-igniters is much more economical compared to retrofitting existing locations that can be remote and are most likely equipped with traditional burner control.
Accordingly, there is a need for a-methods and apparatuses for supervision and control of the burner system that are sufficiently simple, reliable and rugged for oil and gas process equipment.
SUMMARY OF THE INVENTIONThe present invention provides apparatuses and methods for monitoring vessel temperature and shutting off the burners if undesired vessel temperature characteristics are recorded. Further, the present invention provides methods and devices for the control of process equipment burners as to avoid natural gas emissions and overheating scenarios.
Advantages and novel features will become apparent to those skilled in the art upon examination of the following description and can be learned by the practice of the invention.
The present invention embodiment depicted in
Mounting/sensor fixture 7 will thread into the dedicated thermowell for analog temperature gauge 6 utilizing male fixture threads 17, preferably matching the female threads of the thermowell. Additionally, female fixture threads 18, preferably matching the thermowell threads as well, allows access for the analog temperature gauge 6 into the thermowell as well. Temperature sensor lead 19 connects circuit board 29 to temperature probe 16 through temperature sensor port 20. Temperature senor probe 16 is preferably made of a rigid material forming a column that parallels the stem of analog temperature gauge 6. Another embodiment of temperature probe 16 is a composition of flexible material and a clip located at the end of temperature probe 16 that attaches temperature probe 16 to analog temperature gauge 6 stem. In either embodiment, temperature probe 16 is held in proper contact with vessel 2 fluid. Mounting fixture 22 acts in fixing controller 24 to vessel 2 via fasteners installed through fastener ports 21. Furthermore, temperature sensor lead 19 can be communicated through temperature sensor port 20 and into controller 24.
With the essential elements of the present invention described, the typical function will now be described. The primary goal of the present invention in any embodiment is to eliminate uncontrolled methane emissions via the main burner and ultimately exhaust stack 3 of oil and gas process equipment. The preferred method is executed, first, by recognizing the request for main burner from pneumatic thermostat 8. Pressure sensor 31, preferably a normally-open pressure switch with a contact that completes the circuit board 29 power circuit, turns on circuit board 29 when the output pressure of pneumatic thermostat 8 is high enough to close the pressure sensor 31 contact. Circuit board 29 begins recording vessel 2 in either embodiment disclosed. If circuit board 29 registers an unlit main burner, an output will be sent to solenoid valve 32, closing it and ceasing fuel flow to the main burner. Circuit board 29 registers that the main burner is unlit based on the heat transfer rate of the burner system should be increased to a minimum point that vessel 2 temperature should not continue to decline. Due to this characteristic, the logic of circuit board 29 microcontroller 54 can decide to shut-in the main burner based off continued vessel 2 temperature decline or based on a minimum temperature threshold.
During initialization or reset after the shut-in of the main burner by the present invention, reset button 5 is positioned on the outside of controller 24. The technician will press reset button 5 which will set solenoid valve 32 to an open state, at which point the burner system can be initialized as per traditional control protocols. The present invention can then follow a protocol of non-intervention for a period of time or allow fuel pressure to the main burner based on a desired heating characteristic tracked in the vessel 2 temperature trendline.
Another feature of the present invention is, if set to continuous mode (as described in paragraph [0027]), a high temperature shutdown can be implemented. If the present invention is configured to continually observe vessel 2 temperature, it would then be capable of shutting down the main burner if a high temperature threshold is reached. This feature would help process equipment avoid overheating damage to the equipment in cases of pneumatic thermostat 8 malfunction or if pneumatic thermostat 8 is set to high.
For the purpose of disclosure, approximately is defined here as plus or minus 10%.
Claims
1. A system for managing a process equipment's burner system, the system comprising:
- a temperature sensor;
- a controller;
- a fixture for said controller and temperature sensor;
- and an electronic valve.
2. The system of claim 1 wherein said electronic valve is bypassable.
3. The system of claim 2 wherein said electronic valve is a three-way venting latching solenoid valve.
4. The system of claim 1 wherein said fixture is magnetic.
5. The system of claim 3 wherein said fixture uses a compressible seal surrounding the temperature sensor.
6. The system of claim 1 further comprising a pressure sensor configured to measure pressure supplied from a pneumatic thermostat to a pressure open valve configured to control a main burner.
7. The system of claim 1 comprising a second electronic valve configured to control fuel to a pilot burner.
8. The system of claim 7 wherein said second electronic valve is bypassable.
9. The system of claim 1 further comprising an ignition element installed on the pilot burner.
10. The system of claim 9 further comprising a high voltage module wired to said ignition element.
11. A method of installing a burner control system on a piece of process equipment, the method comprising:
- installing a controller;
- installing an electronic valve between the pneumatic thermostat and a pressure open valve configured for control of a main burner;
- and installing a temperature sensor for measurement of vessel contained fluids;
- wherein the method is performed without removing a pneumatic thermostat configured to measure a temperature within the process equipment and flame sensor is not installed.
12. The method of claim 11 comprising installing an electronic valve configured for control of fuel to a pilot burner.
13. The method of claim 11 comprising installing a pressure sensor between the pneumatic thermostat and the pressure open valve.
14. The method of claim 14 comprising supplying power to the claimed system when pressure sensor is activated.
15. The method of claim 11 comprising mounting controller and temperature sensor with a magnetic fixture.
Type: Application
Filed: Apr 13, 2022
Publication Date: Oct 20, 2022
Inventors: Ty Freeman Davis (La Plata, NM), Jeffrey Odell Davis (La Plata, NM)
Application Number: 17/719,838