Patent Application
20220349575
Embodiments of the present invention relate to a method and apparatus for eliminating hydrocarbon gas venting from pneumatic controllers—more particularly for eliminating hydrocarbon gas venting from pneumatic controllers for oil and gas production and/or processing equipment.
It is well known that many systems designed to produce natural gas and hydrocarbon liquids utilize natural gas pressure from the production stream to operate pneumatic process controls on the production systems. These pneumatic controls are utilized to open, close, or modulate process control devices to dump collected liquids, effect process temperatures, divert production streams, or stop flow by any number of different configurations. The pneumatic controllers may operate at pressures as high as 60 pounds per square inch gauge (“psig”) or as low as 5 psig. When a process condition dictates, the pneumatic controller sends a pneumatic pressure signal to a control device, or devices, which typically includes a pressure containing chamber that houses a diaphragm that imparts movement to an inner valve via a connecting stem. This configuration is commonly referred to as a motor valve. When the pneumatic pressure signal is applied to the pressure containing chamber of a motor valve, the pneumatic pressure causes the diaphragm to move in relation to the applied pneumatic pressure thus moving the position of the inner valve and redirecting the process fluids, either liquid or gas, to either begin flow in the desired direction, stop flow, split flow, or accomplish any number of process configurations. When a process condition changes, the pneumatic controller removes all or part of the pneumatic pressure signal from the pressure containing chamber of the motor valve which moves the diaphragm and the inner valve to a new position consistent with maintaining proper process control. Removal of the pneumatic pressure signal is accomplished by venting all or part of the pneumatic pressure from the pressure containing chamber. Historically, the gases vented by pneumatic control devices are released directly to the atmosphere where they contribute to the accumulation of greenhouse gas emissions in the atmosphere. In addition, the vented gas from the pneumatic controllers has an economic value to the operator of the production system, which is therefore being lost.
Gas vented from pneumatic controllers has, in most cases, been released directly to the atmosphere. Without a method and apparatus as described herein, which is capable of recovering, collecting, and burning the vented gas, the gas released through the pneumatic controllers will be vented to the atmosphere and wasted. In known systems, which are designed to collect and burn the vent gases, for example flares and thermal oxidizers, the heat energy released by burning the vent gas is wasted to the atmosphere and adds to the total amount of the products of combustion, including but not limited to carbon dioxide, released to the atmosphere. With the method and apparatus of the present invention, the vent gases can be utilized in the process and will not contribute to any additional products of combustion.
Many natural gas and hydrocarbon liquid production systems utilize a natural gas fired, natural draft burner and firetube system to add heat to the process. Typically, the burner system will include a main burner designed to burn natural gas as a fuel, adding the necessary heat to the process by a firetube, a continuously lit high-pressure standing pilot designed to burn natural gas as a fuel, whose purpose is to ignite the main burner on demand, and a system of pressure vessels, valves, and controls designed to flow the proper volume of natural gas fuel to the main burner in relation to the heat load desired, and to the standing high-pressure pilot. A typical natural gas burner device utilizes a mixer to intimately mix the fuel gas with air and direct the mixture to a tip designed to disperse the fuel mixture into the firetube where the standing high-pressure pilot ignites the mixture. Typically, the main burner operates at a fuel gas pressure in the range of about two psig to about fifteen psig when the process is desiring heat. The standing high-pressure pilot typically operates at a continuous fuel gas pressure of about five psig to about eight psig regardless of the fuel gas pressure flowing to the main burner. Typically, it is desired that the pilot remains lit continuously. A continuously lit standing high-pressure pilot consumes approximately 14 cubic feet per hour (“ft3/hr”) to about 18 ft3/hr of fuel gas. This volume of gas equates to approximately 14,000 British thermal units (“Btu”) per hour (“hr”) to approximately 18,000 Btu/hr heat input to the process.
Many natural gas and hydrocarbon liquid production systems utilize an internal combustion natural gas fueled engine system as a prime mover. The natural gas fueled engine can be connected or coupled to one or more different machines including but not limited to, compressors to supply air or other gases at increased pressure, electrical generators to produce electrical power, and/or pumps to supply liquids at an increased pressure. Typically, the engine system will include a naturally aspirated carburetor system designed to intimately mix the fuel gas with air and direct the mixture to the engine cylinders to be burned, an electronic ignition system comprising the necessary electronic circuits, usually by transistors controlled by sensors, to generate the electric pulses which in turn generate the spark to ignite the air and fuel gas mixture within the engine system, and a system of pressure vessels, valves, and controls designed to flow the proper volume of natural gas fuel to the engine carburetor in relation to the engine load desired. Typically, the fuel gas pressure to the engine carburetor will be in the range of about 0.5 inches water column (“wc”) to about 14 inches we (about 0.02 to about 0.51 psig) when the engine is running. It is often desired that the engine remains running continuously.
Systems have been marketed to collect the vent gas from pneumatic controllers. Ignoring operating problems that occur with the currently available recovery systems, including for example flares and vapor recovery units, the biggest problem limiting their application has been capital cost. The volume of vent gas produced by pneumatic controllers is relatively small compared to the volume of gases vented from hydrocarbon storage tanks and triethylene glycol (“TEG”) dehydrators. In addition, the usable pressure of the vent gas is negligible, and collection typically involves applying a vacuum to the pneumatic controller vent port and collecting the vent gas either mechanically, which can include for example a vapor recovery unit, or by induction, which can include for example using a device that employees the physical effects of a venturi including but not limited to a flare. Both devices require supplying additional energy, either mechanical, including for example an electric motor, or physical, which itself can include for example the additional natural gas required at the venturi, which is necessary to produce the forces required to move the vent gases. In these cases, the energy required to collect the vent gas is much greater than the energy that the recovered vent gas can produce. Both systems above are net energy consumers. Until now, collecting and utilizing pneumatic controller vent gas has been avoided because of the issues described above.
An additional problem associated with collecting the vented gas is O2 entrainment. Enclosures for pneumatic controllers, for the most part, are usually not airtight. Many pneumatic controllers vent gas into the controller enclosure and out through a vent opening in the enclosure. As stated before, the usable pressure of the vented gas is negligible and an artificial or otherwise augmented system for moving the vent gas to collection is used. If a vacuum is induced on the controller housing, there is a possibility of inducing O2 into the collection system by ingress through the controller enclosure. For collection systems that utilize a compressor or other mechanical apparatus to move the vapors, O2 ingress can be a problem—especially if the compressor is discharging into the sales gas line.
Currently, within the industry, the best practices are alleged to be the replacement and/or modification of high-bleed devices with low-bleed devices. While this reduces vent gas, it does not eliminate it. Further, it is estimated that the cost to convert and/or replace a device is about $500 each.
There is thus a need for a method and apparatus that eliminates the problems of collecting the pneumatic controller vent gas while enabling the use of that gas instead of simply venting it or flaring it unnecessarily.
Embodiments of the present invention relate to a method for eliminating hydrocarbon gas venting, the method including capturing hydrocarbon gas vented by one or more pneumatic controls, storing the captured hydrocarbon gas in a vessel, and directing the captured hydrocarbon gas to an apparatus, the apparatus not including a compressor. Optionally, directing the captured hydrocarbon gas to an apparatus can include directing the captured hydrocarbon gas to a hydrocarbon gas burner assembly. In the method, directing the captured hydrocarbon gas to an apparatus can include directing the captured hydrocarbon gas to an engine. Optionally, directing the captured hydrocarbon gas to a hydrocarbon gas burner assembly can include directing the captured hydrocarbon gas to a pilot of the hydrocarbon gas burner assembly.
In one embodiment, the method can also include supplementing a supply of the captured hydrocarbon gas with an additional supply of hydrocarbon gas, which itself can include supplementing a supply of the captured hydrocarbon gas with a fuel gas train, which fuel train can include the fuel gas train of a burner of the hydrocarbon gas burner assembly. In one embodiment, supplementing a supply of the captured hydrocarbon gas can include regulating at least a portion of the additional supply of hydrocarbon gas with a pressure control valve, which can include regulating least a of the additional supply of hydrocarbon gas at a pressure less than an expected venting pressure of the one or more pneumatic controls but greater than a minimum operating pressure of at least a portion of the hydrocarbon gas burner assembly. Optionally, the method can include regulating at least a portion of the additional supply of hydrocarbon gas at a pressure greater than a minimum operating pressure of a pilot of the hydrocarbon gas burner assembly.
Embodiments of the present invention also relate to a system for capturing and using pneumatic control hydrocarbon vent gas that includes a supply line configured to collect hydrocarbon gas vented from one or more pneumatic controls, a vessel, the vessel can include an inlet coupled to the supply line, and an outlet of the vessel coupled an apparatus, the apparatus not including a compressor. The apparatus can include a hydrocarbon gas burner assembly. The outlet of the vessel can be coupled to a pilot of the hydrocarbon gas burner assembly. The system can also include an additional supply of hydrocarbon gas, which can optionally be derived from a fuel gas train, which itself can optionally include a fuel gas train for a burner. The apparatus can include an engine. Optionally, the system can also include an additional supply of hydrocarbon gas. Optionally, the system can include a make-up pressure regulator set at or about a minimum operating pressure of the engine.
Objects, advantages and novel features, and further scope of applicability of the present invention will be set forth in part in the detailed description to follow, taken in conjunction with the accompanying drawings, and in part will become apparent to those skilled in the art upon examination of the following, or may be learned by practice of the invention. The objects and advantages of the invention may be realized and attained by means of the instrumentalities and combinations particularly pointed out in the appended claims.
The accompanying drawings, which are incorporated into and form a part of the specification, illustrate one or more embodiments of the present invention and, together with the description, serve to explain the principles of the invention. The drawings are only for the purpose of illustrating one or more embodiments of the invention and are not to be construed as limiting the invention. In the drawings:
Embodiments of the present invention relate to system for collecting gas from pneumatic control units, storing it, and using it in a low-pressure pilot light for a gas burner. Embodiments of the present invention also relate to a system for collecting gas from pneumatic control units, storing it, and using it in a low-pressure fuel system for a natural gas fueled engine. Because this low-pressure fuel system supplements the fuel requirements to operate the engine, embodiments of the present invention thus enable operators to sell the fuel that would otherwise have been used to power the engine. Embodiments of the present invention thus not only generate additional revenue for the operator but also provide an effective and efficient system that allows operators to avoid venting natural gas into the atmosphere.
As best illustrated in
For embodiments, where the volume of pneumatic control vent gas may not be sufficient to reliably maintain ignition of low-pressure pilot 12, a flow of existing fuel gas 30 can be passed through pressure control valve 32, which is coupled to main burner fuel vessel 34. Main burner fuel vessel 34 preferably comprises drain valve 36 and/or pressure relief valve 38. Optionally, pressure gauge 40, which can comprise a pressure sensor, is preferably positioned to monitor pressure within main burner fuel vessel 34. An outlet of main burner fuel vessel 34 is preferably coupled to pressure control valve 42, an outlet of which can be coupled to, and thus have its outlet pressure monitored by, pressure gauge 44, which can optionally comprise a pressure sensor. An outlet of pressure control valve 42 is preferably coupled to valve 46 before being directed into pilot fuel vessel 20. Optionally, pressure control valve 48 can be disposed between valve 46 and pilot fuel vessel 20. In one embodiment, pressure control valve 48 can be set such that it discharges at a pressure that is below an expected venting pressure of collected pneumatic control vent gas 16, but at or above a minimum required operating pressure for low-pressure pilot 12. Thus, in one embodiment, pressure control valve 48 is preferably configured to have a discharge pressure of about 2 inches wc to about 12 inches wc and more preferably about 3 inches wc to about 7 inches wc. In one embodiment, pressure control valve 42 and/or pressure gauge 44 are optionally not provided.
In addition to an outlet of main burner fuel vessel 34 being directed through pressure control valve 42, an outlet of main burner fuel vessel 34 can also be coupled to pressure control valve 50 before passing to natural gas burner 14. Optionally, an outlet of pressure control valve 50 can be coupled to and thus monitored by pressure gauge 52, which can optionally comprise a sensor. Temperature control valve 54 can be provided to control a flow of gas entering natural gas burner 14. Optionally, valve 56 can also be provided between main burner fuel vessel 34 and natural gas burner 14. One or more of the various foregoing pressure and/or temperature control valves can be electrical or pneumatic. In one embodiment of the present invention, pneumatic controllers are used to control the various control and/or temperature valve. In one embodiment, the electrical control and/or temperature valves can comprise electrical control valves. In this embodiment, an electric control module preferably monitors one or more sensors, which can include one or more pressure and/or temperature sensors. The electric control module then controls one or more of the control and/or temperature valves based at least in part on the outputs of the one or more sensors.
Although numerous devices can be used and will provide desirable results, depending on the details of a particular application, in one embodiment, the following have been found to provide particularly desirable results for some applications:
pressure control valve 48 can include a FISHER® 912N, 250 Psig maximum inlet pressure, 3″-7″ wc outlet pressure, ¼″ FNPT inlet, ¼″ FNPT outlet (FISHER is a registered trademark of Fisher Controls International, LLC);
pressure relief valve 24 can include a Control Devices model 36JN37, brass body, 20 psig maximum operating pressure, set at 0.5 psig, brass seat, SS spring, ⅜″ MNPT connection;
check valve 18 can include a CHECK-ALL® Model U3DCSVT.125SS, carbon steel body, VITON® seat, 0.125 psig cracking pressure, SS spring, ½″ FNPT body connections (CHECK-ALL is a registered trademark of International Valve Corporation DBA Check-All Valve Manufacturing Co., VITON is a registered trademark of Dupont Down Elastomers L.L.C.);
One or more of the various pressure gauges can include a MARSH® model G22704, 2 ½″ dial face, 0-30″ wc range, brass socket, ¼″ MNPT bottom mount (MARSH is a registered trademark of Bellofram Corporation); and
Low-pressure pilot 12 can include an Eclipse LP injector model 04A, 20,000 Btu/hr@7″ wc pressure, ¼″ FNPT gas inlet, 1″ FNPT injector outlet.
By routing the vent gas to a system utilizing a low-pressure pilot capable of operating at about 3.5″ to about 28″ water column fuel pressure (about 0.125 psig to about 1 psig) instead of the traditional high-pressure pilot fuel pressures of about 5 psig to about 8 psig, embodiments of the present invention enable the consumption of the pneumatic controller vent gas in the pilot process, saving fuel gas that is traditionally used for the high-pressure pilot. In addition, the low-pressure pilot of embodiments of the present invention consumes approximately the same amount of fuel gas as the traditional pilot operating at about 5 psig to about 8 psig, so there is no significant increase or decrease in the heat input into the process or in the products of combustion released into the atmosphere when compared to a traditional high-pressure pilot. If, on occasion, there is a brief increase in the pilot heat output, the process thermostat will compensate by reducing the main burner output. A standard oil and gas production unit, typical of the Denver Basin, Colo., which utilizes pneumatic controllers designed to the preferred Environmental Protection Agency (“EPA”) National Gas Star Best Management Practices, produces approximately 10 ft3/hr to approximately 14 ft3/hr of vent gas from the pneumatic controls. This volume closely matches the volume of fuel gas used by a typical high-pressure pilot. Thus, in one embodiment, low-pressure pilot system 10 be used to replace a high-pressure pilot on legacy oil and gas production systems in the field today and/or can be incorporated into new production systems in lieu of a high-pressure pilot system. Replacing a high-pressure pilot system with low-pressure pilot system 10 eliminates the venting of pneumatic controller vent gas to the atmosphere as well as the need to add costly and ineffective add-on control devices that are required to collect the vent gas. Often, the add-on control devices are prone to poor online run times, which allows the pneumatic controllers to vent to the atmosphere uncontrolled for the period the add-on device is not operating.
Embodiments of low-pressure pilot system 10 can be integral to the operation of the process. Standing pilot technology and practice is well accepted, customary, and utilized all over the world. Embodiments of the present invention enable the use of most of the existing fuel gas and control systems on existing production units in the field today, for both large and small volume venting applications. Low-pressure pilot system 10 can collect all the vent gas available and route it to the low-pressure pilot. In one embodiment, low-pressure pilot system 10 preferably has the capacity to consume approximately 20 ft3/hr to about 60 ft3/hr and more preferably about 40 ft3/hr of vent gas when operating at about 28″ water column (about 1 psig) operating pressure. This pilot capacity enables embodiments of the present invention to be installed on many large modules utilizing numerous pneumatic controls, far greater in number than what would typically be encountered on a typical oil field production unit.
If an embodiment of the present invention is installed on small applications where the volume of vent gas is not sufficient to maintain a stable low-pressure pilot flame, embodiments of the present invention preferably incorporate a separate low-pressure pilot fuel gas system, which includes a make-up fuel pressure regulator set to a minimum operating pressure and volume that is needed to maintain a stable flame at the low-pressure pilot tip, and a pilot fuel vessel adequate in volume to smooth-out any sudden increase in vent gas (multiple pneumatic controllers venting at once as an example) without upsetting the operation of the pilot or over pressuring the pilot fuel gas system. Although the volume of pilot fuel vessel can be constructed to any desired size, in one embodiment, the volume of the pilot fuel vessel is most preferably about 1.5 cubic feet to about 4 cubic feet.
Although in one embodiment, low-pressure pilot 12 can remain continuously lit, as a standing pilot, in one embodiment, low-pressure pilot 12 is preferably only ignited shortly before natural gas burner 14 is to be ignited. In this embodiment, an electric arc can be initiated to ignite low-pressure pilot 12. Thus, in one embodiment, low-pressure pilot 12 does not remain continuously lit and thus is not a standing pilot. Optionally, the control unit can provide a burner management process such that a valve coupled to low-pressure pilot 12 is opened and an electric spark is initiated to ignite low-pressure pilot before gas is sent to natural gas burner 14. In one embodiment, the control unit can include an algorithm which initiates ignition of low-pressure pilot 12 based on pressure within vessel 20 and/or based on heat demand.
Referring now to
For embodiments, where the volume of pneumatic control vent gas will not be sufficient to reliably maintain fuel to engine 58, a flow of existing fuel gas 67 can be passed through fuel pressure control valve 68, which is preferably coupled to the engine low-pressure fuel gas valve 69, through fuel line 70. Optionally, pressure gauge 71, which can comprise a sensor, is preferably positioned to monitor pressure downstream of fuel gas pressure control valve 68. An outlet of fuel gas pressure control valve 68 is preferably coupled to fuel gas low-pressure control valve 69 through fuel line 72. An outlet of fuel gas low-pressure fuel gas valve 69 can be directed through fuel line 70 into vent gas vessel 61, an outlet of which can be coupled to, and thus have its outlet pressure monitored by, pressure gauge 64, which can optionally comprise a sensor. An outlet of vent gas vessel 61 is preferably coupled to valve 66 before being directed into the inlet of the carburetor or fuel injection system of engine 58, which can optionally include a naturally aspirated engine, through fuel line 65. One or more of the various foregoing pressure control valves can be electrical or pneumatic. In one embodiment of the present invention, pneumatic controllers can be used to control the various control valves. In one embodiment, the electrical control can comprise electrical control valves. In this embodiment, an electric control module preferably monitors one or more sensors, which can include one or more pressure and/or temperature sensors. The electric control module then controls one or more of the control valves based at least in part on the outputs of the one or more sensors.
Although numerous devices can be used and will provide desirable results, depending on the details of a particular application, in one embodiment, the following have been found to provide particularly desirable results for some applications:
pressure control valve 69 can include a IMPCO® Model KN regulator, 13.4″ wc maximum inlet pressure, 8″-10″ wc outlet pressure, ¾″ FNPT inlet, ⅜″ FNPT outlet (IMPCO is a registered trademark of EMPCO, LLC);
pressure relief valve 63 can include a Control Devices model 36JN37, brass body, 20 psig max. operating pressure, set at 0.75 psig, brass seat, SS spring, ⅜″ MNPT connection;
check valve 60 can include a CHECK-ALL® Model U3DCSVT.125SS, carbon steel body, Viton seat, 0.125 psig cracking pressure, SS spring, ½″ FNPT body connections;
One or more of the various pressure gauges can include a MARSH® model G22704, 2 ½″ dial face, 0-30″ wc range, brass socket, ¼″ MNPT bottom mount.
By routing the vent gas to a fuel system utilizing a low-pressure regulator capable of operating from about 0.5″ to about 14″ water column fuel pressure (about 0.02 psig to about 0.51 psig), embodiments of the present invention enable the consumption of the pneumatic controller vent gas in the engine fuel system, saving fuel gas that is traditionally vented to the atmosphere. In addition, a typical natural gas fueled engine of the horsepower size common in the industry consumes much greater amounts of fuel gas per hour than that what is typically produced by pneumatic controls. A typical 95 brake horsepower (“bhp”) natural gas fueled engine running at approximately 75% load will consume approximately 7850 Btu/bhp-hr fuel gas, or approximately 560 standard cubic feet per hour (“scf/hr”) of natural gas. A standard oil and gas industry wellhead compression system utilizing a naturally aspirated natural gas fueled engine system typical of the Denver Basin, Colo., which utilizes pneumatic controllers designed to the preferred Environmental Protection Agency (“EPA”) National Gas Star Best Management Practices, produces approximately 10 ft3/hr to approximately 14 ft3/hr of vent gas from the pneumatic controls. For a typical 95 bhp engine system operating at or near 75% load, there is no increase in the products of combustion released into the atmosphere when compared to a traditional engine fuel gas system. If, on occasion, there is a brief increase in the vent gas volume, the engine fuel intake system will compensate by reducing the volume of fuel introduced into the vent vessel through the low-pressure regulator. Thus, in one embodiment, low-pressure fuel system 57 be retrofitted to capture pneumatic controller vent gas on legacy engine systems in the field today and/or can be incorporated into new engine systems. Installation of low-pressure fuel system 57 eliminates venting of pneumatic controller vent gas to the atmosphere as well as the need to add costly and ineffective add-on control devices that are required to collect the vent gas. Often, the add-on control devices are prone to poor online run times, which allows the pneumatic controllers to vent to the atmosphere uncontrolled for the period the add-on device is not operating.
Embodiments of low-pressure fuel system 57 can be integral to the operation of the process. Low-pressure natural gas engine fuel technology and practice is well accepted, customary, and utilized all over the world. Embodiments of the present invention enable the use, with some modification, of most of the existing fuel gas and control systems on existing engine systems in the field today, for both large and small horsepower applications. Low-pressure fuel system 57 can collect all the vent gas available and route it to the engine fuel inlet. In one embodiment, low-pressure fuel system 57 has the capacity to consume approximately 60 ft3/hr and more of vent gas when operating at about 10″ water column (about 0.37 psig) operating pressure. This capacity enables embodiments of the present invention to be installed on many large modules utilizing numerous pneumatic controls, far greater in number than what would typically be encountered on a typical engine system.
If an embodiment of the present invention is installed on small horsepower applications where the volume of vent gas is not sufficient to maintain a stable running engine, embodiments of the present invention preferably incorporate a separate low-pressure fuel gas system, which includes a make-up fuel pressure regulator set to at or about minimum operating pressure and volume that is needed to maintain a stable running engine, vent gas vessel adequate in volume to smooth-out any sudden increase in vent gas (multiple pneumatic controllers venting at once as an example) without upsetting the operation of the engine or over pressuring the engine fuel gas system. Although the volume of the vent gas vessel can be constructed to any desired size, in one embodiment, the volume of the vent gas vessel is most preferably about 1.5 cubic feet to about 4 cubic feet. In one embodiment, collected pneumatic control vent gas can be stored and routed to a pilot of the natural draft gas burner. Optionally, collected pneumatic control vent gas can be sent to any other desired location, including other low-pressure systems. For example, in one embodiment, the recovered vapors can be sent to oil storage tanks, where additional vapors accumulate and are collected and used in other processes. Throughout the application, where reference is made to a gauge, such gauge can optionally include one or more of a mechanical gauge, and/or an electronic sensor, which can be monitored by a microcontroller, processor, and/or circuit, which can perform one or more functions based on sensor output and/or measurement, including but not limited to displaying a value, and/or causing activation of one or more valves.
In one embodiment, the present invention utilizes captured vent gas from one or more pneumatic controls without compressing the captured vent gas. The term “vent gas” as used herein can include gas that was used to activate a control. In one embodiment, the captured control vent gas can be sent to a burner assembly.
Optionally, the control unit, if provided, can include a field programmable gate array and/or a general or specific purpose computer or distributed system programmed with computer software implementing steps described above, which computer software may be in any appropriate computer language, including but not limited to C, C++, FORTRAN, BASIC, Java, Python, Linux, assembly language, microcode, distributed programming languages, etc. The control unit can include a plurality of such computers/distributed systems (e.g., connected over the Internet and/or one or more intranets) in a variety of hardware implementations. For example, data processing can be performed by an appropriately programmed microprocessor, microcontroller, computing cloud, Application Specific Integrated Circuit (ASIC), or the like, in conjunction with appropriate memory, network, and bus elements. One or more processors and/or microcontrollers can operate via instructions of the computer code and the software is preferably stored on one or more tangible non-transitive memory-storage devices. All computer software disclosed herein may be embodied on any non-transitory computer-readable medium (including combinations of mediums), including without limitation CD-ROMs, DVD-ROMs, hard drives (local or network storage device), USB keys, other removable drives, ROM, and firmware.
Embodiments of the present invention can be used with high-bleed pneumatic control devices and/or low-bleed control devices. In one embodiment, high-bleed devices can optionally be used to power a natural-gas engine, while low-bleed control devices can be used to provide fuel to a low-pressure pilot. Thus, embodiments of the present invention can be used for controllers that have not yet been replaced and/or modified to low-bleed devices and embodiments of the present invention can be used to eliminate the venting of natural gas from controllers that have already been remediated according to current industry-recognized “best practices”.
Note that in the specification and claims, “about”, “approximately”, and/or “substantially” means within twenty percent (20%) of the amount, value, or condition given.
Embodiments of the present invention can include every combination of features that are disclosed herein independently from each other. Although the invention has been described in detail with particular reference to the disclosed embodiments, other embodiments can achieve the same results. Variations and modifications of the present invention will be obvious to those skilled in the art and it is intended to cover in the appended claims all such modifications and equivalents. The entire disclosures of all references, applications, patents, and publications cited above are hereby incorporated by reference. Unless specifically stated as being “essential” above, none of the various components or the interrelationship thereof are essential to the operation of the invention. Rather, desirable results can be achieved by substituting various components and/or reconfiguring their relationships with one another.
This application claims priority to and the benefit of the filing of U.S. Provisional Patent Application No. 63/180,977, entitled “Method and Apparatus for Eliminating Hydrocarbon Gas Venting From Pneumatic Controllers”, filed on Apr. 28, 2021, as well as U.S. Provisional Patent Application No. 63/195,563, entitled “Method and Apparatus for Eliminating Hydrocarbon Gas Venting From Pneumatic Controllers”, filed on Jun. 1, 2021, and the specifications thereof are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 63180977 | Apr 2021 | US | |
| 63195563 | Jun 2021 | US |
