Partial pre-mix flare burner and method
A flare burner that is particularly suitable for use in connection with ground flares and other types of flares in which it is important to control the height of the flame envelope created by the burner is provided. The flare burner includes a pre-mix zone including a pre-mix chamber into which air is entrained. A uniform mixture of fuel and air is formed in the pre-mix zone and caused to exit an air/fuel outlet in the top of the pre-mix chamber. In one embodiment, the amount of air in the fuel/air mixture that exits the air/fuel outlet is in excess of the stoichiometric amount of air required to support combustion of the fuel in the mixture. Fuel is injected around the perimeter of the air/fuel outlet, combustion is initiated and a flame envelope is created. By injecting a mixture of fuel and air that includes excess air into the center of the flame envelope, combustion of the central portion of the flame envelope is accelerated which allows more fuel to be flared with a given flame envelope height. The invention also includes a ground flare and a method of flaring fuel with a flare burner.
The present invention relates to flare apparatus and methods of flaring flammable waste gases and diverted fuel stock. In one embodiment, the invention relates to ground flare burners, ground flares and associated methods.
Flare apparatus and methods are utilized to burn and dispose flammable waste gases and diverted fuel stock in a variety of applications. For example, flares are typically located at production facilities, refineries, processing plants and the like for disposing of flammable waste gases that are dumped and/or fuel stock streams that are diverted during venting, shut-downs, upsets or emergencies. The flaring of flammable waste gases and diverted fuel stock (hereinafter referred to as “fuel”) without producing smoke is usually desirable or even mandatory. Smokeless flaring is accomplished by assuring that non-oxidized soot does not form in a sufficient quantity to leave the flame. This is accomplished by assuring that a sufficient amount of oxygen is mixed with the fuel to prevent a situation in which the mixture becomes too fuel rich to be effective.
In many applications, the length of the flame envelope created by the flare is also important. Examples of types of flares in which a relatively short flame envelope is desirable include aesthetic flares such as pit-type enclosed flares, ground flares and high pressure flares on floating production facilities. In such flares, it is often necessary to prevent the flames from being visible to the surrounding community. On the other hand, such flares need to have the capacity to combust a large volume of fuel at any given time. The length of the flame envelope tends to increase as the volume of fuel being flared increases.
Ground flares, also referred to as multi-point flares, are typically used in applications in which the amount of fuel to be flared at a given time can vary from a relatively small volume to a very high volume (for example, 1,000,000 pounds per hour or higher). In order to accommodate the variance in fuel volume and allow the fuel to be combusted in a smokeless manner, multiple stages of burners are utilized. The flow to each stage of burners is directed by a control system that is responsive to the pressure and volume of fuel to be flared. In this way, sufficient pressure is available to each burner in operation to assure that an appropriate amount of air is entrained and that sufficient mixing of the air and fuel occurs to ensure smokeless combustion in the range of application.
A ground flare system is typically spread out over a large area, for example, three acres, and surrounded by a large fence or other enclosure. The enclosure functions to exclude personnel and animals from the flame area and minimize radiation, visibility and noise to the surrounding area. The enclosure is typically made of metal or some other heat refracting material and is from 20 to 60 feet high. As a result, the enclosure can be costly to erect and maintain.
The spacing of the burners and flow rate of fuel in a ground flare system is also important. The burners need to be close enough to one another for cross-lighting to occur and packed close enough in general to reduce the overall size of the system and the surrounding enclosure. For cost reasons, a minimal number of ignition pilots are desirable. Typical units include a single pilot at the end of each row of burners. On the other hand, the burners must not be so close to one another as to restrict air flow and hinder smokeless burning or cause the flames to coalesce into a ball of fire that exceeds the height of the enclosure. Also, the flow rate of the fuel must be controlled so that the height of the individual flames does not exceed the height of the enclosure.
One type of ground flare burner utilized heretofore includes a plurality of diffusion jets to distribute the fuel and draw in the air required for combustion. The jets are injected into the atmosphere at a sufficient velocity to draw combustion air into the jets. Upon ignition of the fuel, air from the surrounding environment is laterally entrained from above the discharge point of the fuel. As the velocity of the stream diminishes, the buoyancy effect of the hot gases then contributes to the overall mixing regimen of the fuel and air which allows combustion of the remaining fuel to be completed.
The overall flame envelope created by utilizing only diffusion jets to distribute the fuel and laterally entrain the air required for combustion includes a dense, central core of fuel. This central core of fuel remains intact until the outer portions of the flame envelope begin to burn off. As the outer portions of the flame envelope combust, air can then enter the inner confines of the flame envelope to complete the oxidation process. Unfortunately, due to the interaction of the individual fuel jets, the dense core of fuel formed at the center of the flame envelope makes it difficult to increase the flow rate of the fuel to support a larger capacity without causing the length of the flame envelope to increase and/or smoke to occur. An increase in the length of the flame envelope often requires the enclosure surrounding the ground flare to be higher which can significantly increase the cost of the enclosure.
By the present invention, a flare burner is provided which is useful in association with ground flares, high pressure flares and other types of flares. For example, the inventive flare burner overcomes the problems associated with the ground flare burners utilized heretofore. The invention also provides a ground flare apparatus and a method of burning fuel in a flare burner.
SUMMARY OF THE INVENTIONIn accordance with the invention, a flare burner is provided that is capable of combusting a high volume of fuel with a relatively short flame envelope. The decrease in the length of the flame envelope leads to many advantages. For example, the height of the surrounding enclosure of a ground flare can be decreased or the volume of the fuel that can be flared with an existing enclosure height can be increased.
The inventive flare burner comprises a pre-mix zone including a pre-mix chamber, a supplemental fuel inlet for injecting fuel into the pre-mix zone, and a main fuel outlet. Preferably, the inventive flare burner further comprises a fuel feed conduit in fluid communication with the supplemental fuel inlet and the main fuel outlet.
The pre-mix chamber includes a top, a bottom and a sidewall connecting the top to the bottom. The sidewall includes an interior surface and an exterior surface. An air inlet is disposed in one of the bottom and the sidewall, and an air/fuel outlet is disposed in the top.
The supplemental fuel inlet is located in a position with respect to the pre-mix zone such that the injection of fuel from the supplemental fuel inlet into the pre-mix zone entrains air into the pre-mix zone whereby a mixture of fuel and air is formed in the pre-mix zone and caused to exit the air/fuel outlet of the pre-mix chamber.
The main fuel outlet is located in a position with respect to the top of the pre-mix chamber such that fuel can be injected from the main fuel outlet around the perimeter of the air/fuel outlet of the pre-mix chamber. In one embodiment, the main fuel outlet is spaced outwardly from the pre-mix chamber to provide a space between the exterior surface of the sidewall of the pre-mix chamber and the main fuel outlet. As discussed further below, this space allows fresh air to be entrained from below the burner to a point adjacent to the fuel ports disposed on an inner portion of the main fuel outlet. The enhanced mixing created by such entrainment can be important in certain applications, such as when heavy hydrocarbons or unsaturated fuels are being flared.
The fuel feed conduit conducts fuel to the supplemental fuel gas inlet and the main fuel gas outlet. The fuel can be supplied to the supplemental fuel inlet and the main fuel outlet at the same pressure or different pressures depending on the application.
The inventive flare burner can further comprise a fuel membrane disposed around the outside perimeter of the pre-mix chamber. The fuel membrane includes a fuel inlet and is in fluid communication with the main fuel outlet. In some embodiments, the fuel membrane is also in fluid communication with the supplemental fuel inlet. In order to provide the air entrainment space described above, the fuel membrane can be spaced outwardly from the exterior surface of the sidewall of the pre-mix chamber.
Depending on the particular configuration of the inventive flare burner, the pre-mix zone can consist of the pre-mix chamber alone or can include the pre-mix chamber together with areas below and/or above the actual pre-mix chamber. For example, when the air inlet of the pre-mix chamber is in the bottom of the pre-mix chamber and the supplemental fuel inlet is spaced below the air inlet, the fuel and air begin to mix below the air inlet and pre-mix chamber. Also, the fuel and air typically continue to mix above the air/fuel outlet disposed in the top of the pre-mix chamber prior to ignition and combustion in the combustion zone.
The pre-mix chamber and fuel membrane can be formed in a variety of shapes and sizes. In one embodiment, the pre-mix chamber and fuel membrane have a round cross-section. In another embodiment, the pre-mix chamber and fuel membrane have a rectangular cross-section.
In order to enhance the entrainment of air caused by injecting fuel through the supplemental fuel inlet into the pre-mix zone, the interior surface of the pre-mix chamber can include a section that is a Coanda surface. The supplemental fuel inlet is located in a position with respect to the pre-mix chamber such that fuel can be injected from the supplemental fuel inlet onto the Coanda surface. The fuel tends to adhere to and follow the path of the Coanda surface and form into a relatively thin film which causes more air to be entrained into the pre-mix chamber and better mixing of the air with the fuel to occur in the pre-mix chamber.
The pre-mix chamber can have a length to inside hydraulic diameter ratio in the range of from about 0.25:1 to about 4:1. A unit with a pre-mix chamber having a length to inside hydraulic diameter ratio greater than 4:1 would function with an added benefit but would generally be cost prohibitive. In one embodiment, the pre-mix chamber has a length to inside hydraulic diameter ratio in the range of from about 1:1 to about 3:1. In another embodiment, the pre-mix chamber has a length to inside hydraulic diameter ratio of about 1:1 or less. A relatively short length of the pre-mix chamber can be advantageous in ground flare and other flare applications in which the length (or height) of the burner is important, or in applications in which highly reactive fuels might lead to internal burning. Also, in some configurations the fuel is injected from the supplemental fuel inlet under conditions (for example, a plurality of small jets; high pressure) that allow a uniform mixture of air and fuel to be achieved even when the pre-mix chamber has a very low length to inside hydraulic diameter ratio.
The inventive ground flare comprises a plurality of flare burners, a fence or other enclosure extending around the flare burners and a fuel supply line for supplying fuel to the flare burners. At least one of the flare burners is the inventive flare burner described above.
The invention also includes a method of flaring fuel with a flare burner wherein the fuel to be flared is injected through a fuel outlet of the burner into a combustion zone and ignited to create a flame envelope and combust the fuel. In accordance with the inventive method, a portion of the fuel is introduced into a pre-mix zone of the flare burner in a manner that entrains air into the pre-mix zone and creates a mixture of air and fuel within the pre-mix zone. The mixture of air and fuel is injected from the pre-mix zone into a central portion of the flame envelope.
The amount of air entrained into the pre-mix zone and injected into the central portion of the flame envelope is preferably at least about 15% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone. In some applications, injection of a “fuel-rich” mixture of fuel and air (i.e., a mixture having less than 100% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone) into the central portion of the flame envelope is suitable. In most applications, however, injection of a “lean” mixture of fuel and air (i.e., a mixture having more than 100% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone) into the central portion of the flame envelope is desired. In most applications, the amount of air entrained into the pre-mix zone and injected into the central portion of the flame envelope is in the range of from about 125% to about 300% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone.
The amount of fuel introduced into the pre-mix zone is preferably in the range of from about 5% to about 50% of the total amount of fuel to be flared by the flare burner. Due to the injection of a pre-mixed fuel stream into a central portion of the flame envelope in accordance with the inventive method, the flame envelope includes combustion at its center as well as its outer surface. The resulting toroidal flame creates additional mixing and turbulence which results in more uniform and faster combustion of the flame envelope. As a result, the height of the flame envelope can be decreased or the volume of fuel that can be flared with a given flame envelope can be increased. Other advantages are achieved by the inventive flare burner and method as well.
It is, therefore, a general object of the present invention to provide a flare burner and associated method by which a high volume of fuel can be combusted in a relatively short and uniform flame envelope.
Other and further objects, features and advantages of the present invention will be readily apparent to those skilled in the art upon a reading of the description of preferred embodiments which follows when taken in conjunction with the accompanying drawings.
Referring now to the drawings, and particularly to
Referring now to
In the embodiment illustrated by
The pre-mix chamber 32 has a length (or height) to inside hydraulic diameter ratio in the range of from about 0.25:1 to about 4:1, preferably about 1:1 to about 3:1. The exact ratio of the length (or height) to inside hydraulic diameter of the pre-mix chamber 32 will depend in part on the type of fuel to be flared and the pressure available for entrainment and mixing. Generally, a longer pre-mix chamber can result in better mixing of fuel and air therein; however, this advantage is balanced against cost and other considerations. In a preferred embodiment, the length (or height) to inside hydraulic diameter ratio of the pre-mix chamber 32 is approximately 1.5:1. As used herein and in the appended claims, “inside hydraulic diameter” means four (4) times the area within the pre-mix chamber divided by the perimeter of the interior surface of the sidewall of the pre-mix chamber.
The supplemental fuel inlet 34 is located in a position with respect to the pre-mix zone 31 such that the injection of fuel from the supplemental fuel inlet into the pre-mix zone entrains air into the pre-mix space 31(a) and through the air inlet 48 into the pre-mix chamber 32 whereby a mixture, preferably a substantially homogenous mixture, of fuel and air is formed in the pre-mix zone and caused to exit the air/fuel outlet 50 in the top 42 of the pre-mix chamber. The fuel and air continue to mix in the pre-mix space 31(c). Combustion of the mixture of fuel and air does not typically occur until the mixture exits the air/fuel outlet 50, generally a detached distance from the air/fuel outlet. The distance from the air/fuel outlet 50 at which combustion occurs varies due to the amount of air in the mixture and the velocity at which the mixture is discharged from the air/fuel outlet. In some cases, due to short de-stage timing sequences, combustion can occur in the pre-mix zone (for example, in short duration, very low pressure scenarios). As shown by
An annular fuel membrane 60 is disposed around the outside perimeter of the pre-mix chamber 32. The fuel membrane 60 is connected to the fuel feed conduit 38 and in fluid communication with the main fuel outlet 36. The fuel membrane 60 comprises an open top 62, a bottom 64, and an external sidewall 66 and internal sidewall 67 connecting the top to the bottom. In the embodiment shown by
The main fuel outlet 36 is located in a position with respect to the top 42 of the pre-mix chamber such that fuel can be injected from the main fuel outlet 36 around the perimeter 69 of the air/fuel outlet 50 of the pre-mix chamber. As best shown by
As shown by
An alternative embodiment of the annular fuel injector body 70 is shown by
The fuel feed conduit 38 is in fluid communication with the supplemental fuel inlet 34 and the main fuel outlet 36 for conducting fuel thereto. The fuel feed conduit 38 includes a main branch 80 having a first end 82 and a second end 84. The first end 82 includes a flange 86 for connecting the first end to a source of the fuel (as understood by those skilled in the art, these types of connections are more typically made by welding the pipe sections directly together or with some other mechanical connection that does not require gaskets; e.g., the gaskets between corresponding flanges generally cannot withstand the radiant heat in the surrounding environment). The second end 84 is connected to a corresponding inlet 88 in the external sidewall 66 of the fuel membrane 60. The fuel feed conduit 38 also includes a supplemental branch 90 which connects the fuel feed conduit to the supplemental fuel inlet 34. The supplemental branch 90 includes a first end 92 and a second end 94. The first end 92 is connected to the main branch 90 of the feed conduit 38. A coupling 96 connects the second end 94 to the supplemental fuel inlet 34. Alternatively, separate fuel feed conduits or risers can conduct fuel to the supplemental fuel inlet 34 and main fuel outlet 36 (as opposed to the single integrated conduit or riser 38). The separate conduits or risers will typically run from a common fuel header.
Referring to
Referring now to
In the embodiment illustrated by
As best shown by
The pre-mix chamber 132 has a length (or height) to inside hydraulic diameter ratio in the range of from about 0.25:1 to 4:1, preferably about 1:1 to about 3:1. The exact ratio of the length (or height) to inside hydraulic diameter of the pre-mix chamber 132 will depend in part on the type of fuel to be flared and the pressure available for entrainment and mixing. Generally, a longer pre-mix chamber can result in better mixing of fuel and air therein; however, this advantage is balanced against cost and other considerations. In a preferred embodiment, the length (or height) to inside hydraulic diameter ratio of the pre-mix chamber 132 is approximately 1.5:1.
The supplemental fuel inlet 134 is located in a position with respect to the pre-mix zone 131 such that the injection of fuel from the supplemental fuel inlet into the pre-mix zone entrains air into the pre-mix space 131(a) and through the air inlet 148 into the pre-mix chamber whereby a mixture, preferably a substantially homogenous mixture, of fuel and air is formed in the pre-mix zone and caused to exit the air/fuel outlet 150 in the top 142 of the pre-mix chamber. The fuel and air continue to mix in the pre-mix space 131(c). Combustion of the mixture of fuel and air does not typically occur until the mixture exits the air/fuel outlet 150, generally a detached distance from the air/fuel outlet. The distance from the air/fuel outlet 150 at which combustion occurs varies due to the amount of air in the mixture and the velocity at which the mixture is discharged from the air/fuel outlet. In some cases, due to short de-stage timing sequences, combustion can occur in the pre-mix zone (for example, in short duration, very low pressure scenarios). As shown by
An annular fuel membrane 170 is disposed around the outside perimeter of the pre-mix chamber 132. The fuel membrane 170 is connected to the fuel feed conduit 138 and in fluid communication with both the main fuel outlet 136 and the supplemental fuel inlet 134. The fuel membrane 170 comprises an open top 172, a bottom 174, and an external sidewall 176 and internal sidewall 177 connecting the top to the bottom. In the embodiment shown by
Supplemental fuel feed conduits 180(a), 180(b), 180(c) and 180(d) extend from the annular fuel membrane 170 to the supplemental fuel inlet 134 (i.e., to the annular distribution manifold 164) to deliver fuel from the fuel membrane 170 to the inlet 134 (i.e., the manifold 164). Each of the supplemental fuel feed conduits 180(a), 180(b), 180(c) and 180(d) includes a first end 182 attached to the membrane 170 and a second end 184 attached to the inlet 134 (i.e., the manifold 164).
The main fuel outlet 136 is located in a position with respect to the top 142 of the pre-mix chamber 132 such that fuel can be injected from the main fuel outlet around the perimeter 186 of the air/fuel outlet 150 of the pre-mix chamber. As best shown by
As shown by
The fuel feed conduit 138 is in fluid communication with the supplemental fuel inlet 134 and the main fuel outlet 136 for conducting fuel thereto. The fuel feed conduit 138 has a first end 200 and a second end 202. The first end 200 includes a flange 204 for connecting the first end to a source of the fuel (again, these types of connections are more typically made by welding). The second end 202 is connected to a corresponding inlet 206 in the external sidewall 176 of the annular gas membrane 170. Alternatively, separate fuel feed conduits or risers can conduct fuel to the supplemental fuel inlet 134 and main fuel outlet 136 (as opposed to the single integrated conduit or riser 138). The separate conduits or risers will typically run from a common fuel header.
Referring to
The flare burner 130 achieves the same advantages that are achieved by the flare burner 30. The flame envelope 100 generally depicted by
Referring now to
In the embodiment illustrated by
As best shown by
The sidewall 246 of the pre-mix chamber 232 includes four sides 246(a), 246(b), 246(c) and 246(d). Each of the sides 246(a), 246(b), 246(c) and 246(d) includes an interior surface 254 and an exterior surface 256. A lower portion 258 of each of the sides 246(a), 246(b), 246(c) and 246(d) is flared outwardly in a curvilinear manner to impart an annular Coanda surface 260 to the interior surface 254 of the side. The pre-mix chamber 232 has a length (or height) to inside hydraulic diameter ratio in the range of from about 0.25:1 to 4:1, preferably about 1.1 to about 3:1. The exact ratio of the length (or height) to inside hydraulic diameter of the pre-mix chamber 232 will depend in part on the type of fuel to be flared and the pressure available for entrainment and mixing. Generally, a longer pre-mix chamber can result in better mixing of fuel and air therein; however, this advantage is balanced against cost and other considerations. In a preferred embodiment, the length (or height) to inside hydraulic diameter ratio of the pre-mix chamber 232 is approximately 1.5:1.
The supplemental fuel inlet 234 is located in a position with respect to the pre-mix zone 231 such that the injection of fuel from the supplemental fuel inlet into the pre-mix zone entrains air into the pre-mix space 231(a) and through the air inlet 248 into the pre-mix chamber 232 whereby a mixture, preferably a substantially homogenous mixture, of fuel gas and air is formed in the pre-mix zone and caused to exit the air/fuel outlet 250 in the top 242 of the pre-mix chamber. Combustion of the mixture of fuel and air does not typically occur until the mixture exits the air/fuel outlet 250, generally a detached distance from the air/fuel outlet. The distance from the air/fuel outlet 250 at which combustion occurs varies due to the amount of air in the mixture and the velocity at which the mixture is discharged from the air/fuel outlet. In some cases, due to short de-stage timing sequences, combustion can occur in the pre-mix zone (for example, in short duration, very low pressure scenarios).
As best shown by
A rectangular fuel membrane 270 is disposed around the outside perimeter of the pre-mix chamber 232. The fuel membrane 270 is connected to the fuel feed conduit 238 and in fluid communication with both the main fuel outlet 236 and the supplemental fuel inlet 234. The membrane 270 comprises an open top 272, a bottom 274, and an external sidewall 276 and internal sidewall 277 connecting the top to the bottom. In the embodiment shown by
Supplemental fuel feed conduits 280(a), 280(b), 280(c) and 280(d) extend from the fuel membrane 270 to the supplemental fuel inlet 234, that is to the tubular distribution manifolds 264(a) and 264(b), to deliver fuel from the fuel membrane thereto. Each of the supplemental fuel feed conduits 280(a), 280(b), 280(c) and 280(d) includes a first end 282 attached to the fuel membrane 270 and a second end 284. The second ends 284 of the conduits 280(a) and 280(d) are attached to opposing ends of the tubular distribution manifold 264(a). The second ends 284 of the conduits 280(b) and 280(c) are attached to opposing ends of the tubular distribution manifold 264(b).
The main fuel outlet 236 is located in a position with respect to the top 242 of the pre-mix chamber 232 such that fuel can be injected from the main fuel outlet around the perimeter 286 of the air/fuel outlet 250 of the pre-mix chamber. As best shown by
As shown by
The fuel feed conduit 238 is in fluid communication with the supplemental fuel inlet 234 and the main fuel outlet 236 for conducting fuel gas thereto. The fuel feed conduit 238 has a first end 300 and a second end 302. As shown, the first end 300 includes a flange 304 for connecting the first end to a source of the fuel gas (again, these types of connections are more typically made by welding). The second end 302 is connected to a corresponding inlet 306 in the external sidewall 276 of the annular fuel membrane 270. Alternatively, separate fuel feed conduits or risers can conduct fuel to the supplemental fuel inlet 234 and main fuel outlet 236 (as opposed to the single integrated conduit or riser 238). The separate conduits or risers will typically run from a common fuel header.
Referring to
The flare burner 230 achieves the same advantages that are achieved by the flare burners 30 and 130. The flame envelope 100 generally depicted by
The polygonal (rectangular in the embodiment illustrated) shape of the flare burner 230 may allow more flexibility in spacing the flare burners in a ground flare application. Also, such a shape may allow more flexibility in how the fuel is directed from the diffusion gas ports 292 due to the fact that the geometry can be rotated to change the interaction zones.
Referring now to
A mixture (preferably a substantially homogenous mixture) of fuel and air can be formed in the pre-mix zone 331 including the pre-mix chamber 332. As discussed below, the mixture formed in the pre-mix zone 331 can be either fuel-rich or fuel-lean. The pre-mix chamber 332 includes a round cross-section and has a cylindrical shape. The pre-mix chamber includes a top 342, a bottom 344, a sidewall 346 connecting the top to the bottom, an air inlet 348 disposed in the bottom 344 and an air/fuel outlet 350 disposed in the top 342. The sidewall 346 includes an interior surface 347 and an exterior surface 349. As shown, the top 342 and bottom 344 are open thereby forming the air inlet 348 and air/fuel outlet 350. As a result, the air inlet 348 and air/fuel outlet 350 each also have a round cross-section. The pre-mix chamber 332 has a length (or height) to inside hydraulic diameter ratio in the range of from about 0.25:1 to about 4:1.
In the embodiment shown by
The supplemental fuel inlet 334 is located in a position with respect to the pre-mix zone 331 such that the injection of fuel from the supplemental fuel inlet into the pre-mix zone entrains air into the pre-mix space 331(a) and through the air inlet 348 into the pre-mix chamber 332 whereby a mixture, preferably a substantially homogenous mixture, of fuel gas and air is formed in the pre-mix zone and caused to exit the air/fuel outlet 350 in the top 342 of the pre-mix chamber. Combustion of the mixture of fuel and air does not typically occur until the mixture exits the air/fuel outlet 350, generally a detached distance away from the air/fuel outlet. The distance from the air/fuel outlet 350 at which combustion occurs varies due to the amount of air in the mixture and the velocity at which the mixture is discharged from the air/fuel outlet. In some cases, due to short de-stage timing sequences, combustion can occur in the pre-mix zone (for example, in short duration, very low pressure scenarios).
As shown by
Each fuel outlet arm 354 and the bull nose 353 include a plurality of fuel ports 356. The ports 356 are linearly arranged along the longitudinal axis of each fuel outlet arm 354. An alternative embodiment of the supplemental fuel inlet 334 is shown by
An annular fuel membrane 360 is disposed around the outside perimeter of the pre-mix chamber 332. The fuel membrane 360 is connected to the fuel feed conduit 338 and in fluid communication with the main fuel outlet 336. The membrane 360 comprises an open top 362, a bottom 364, and an external sidewall 366 and internal sidewall 367 connecting the top to the bottom. In a preferred embodiment, the external sidewall 366 is spaced approximately three inches from the internal sidewall 367 (this distance depends on the nature of the fuel and the overall configuration of the burner). In the embodiment shown by
The main fuel outlet 336 is located in a position with respect to the top 342 of the pre-mix chamber such that fuel can be injected from the main fuel outlet 336 around the perimeter 368 of the air/fuel outlet 350 of the pre-mix chamber. As best shown by
As shown by
The fuel feed conduit 338 is in fluid communication with the supplemental fuel inlet 334 and the main fuel outlet 336 for conducting fuel thereto. The fuel feed conduit 338 includes a main branch 380 having a first end 382 and a second end 384. The first end 382 includes a flange 386 for connecting the first end to a source of the fuel (again, these types of connections are more typically made by welding). The second end 384 is connected to a corresponding inlet 388 in the external sidewall 366 of the fuel membrane 360. The fuel feed conduit 338 also includes a supplemental branch 390 which connects the fuel feed conduit to the supplemental fuel inlet 334. The supplemental branch 390 includes a first end 392 and a second end 394. The first end 392 is connected to the main branch 390 of the feed conduit 338. The second end 394 is connected to the supplemental fuel inlet 334 (specifically the casting 352). Alternatively, separate fuel feed conduits or risers can conduct fuel to the supplemental fuel inlet 334 and main fuel outlet 336 (as opposed to the single integrated conduit or riser 338). The separate conduits or risers will typically run from a common fuel header.
Referring now specifically to
Due to the pre-mix chamber extension cylinder 400, the top 342 and air/fuel outlet 350 of the pre-mix chamber 332 are spaced above the main fuel outlet 336. The top 342 and air/fuel outlet 350 of the pre-mix chamber 332 are in the range of from about 0.5 inches to about 10 inches, preferably in the range of from about 6 inches to about 8 inches, above the main fuel outlet 336. The exact distance can vary depending on the type of fuel being flared, the particular application, the permitted height of the flame envelope and other factors. The bottom 344 of the pre-mix chamber 332 is approximately flush with or about one inch above the supplemental fuel inlet 334. As shown by
The top section 402 of the pre-mix chamber extension cylinder 400 serves both as a wind shield as well as a physical barrier to delay ignition. Specifically, the top section 402 offsets the detrimental cross flow air effects which can force the flame inside the diameter of the pre-mix chamber and interfere with the smokeless capacity of the flare burner. The top section 402 also functions to isolate the pre-mix fuel stream from the diffusion flame ignition. Similarly, the bottom section 404 of the cylinder 400 serves as a bottom wind shield and helps prevent the flame from being pulled back and causing premature ignition. Again, the increased length of the pre-mix chamber 332 created by the extension cylinder 400 enhances mixing of the fuel and air in the pre-mix chamber. The extension cylinder is not necessary in all applications; e.g., it may not be necessary when cross-flow effects are not an issue or when low molecular weight fuels are being flared. The inclusion or non-inclusion of the shield will depend on the molecular weight and heating value of the fuel to be flared, whether the fuel contains saturated or unsaturated hydrocarbons, the involved temperature and pressure and other factors.
In the embodiment shown by
Referring to
The flare burner 330 achieves the same advantages that are achieved by the flare burners 30, 130 and 230. The flame envelope 100 generally depicted by
Referring now to
In this embodiment, the flare burner 330 includes the pre-mix chamber extension cylinder 400. However, instead of being attached directly to fuel membrane 360, the extension cylinder 400 (and hence the pre-mix chamber 332) is spaced inwardly from the fuel membrane to provide an air pathway between the extension cylinder and fuel membrane to allow air to effectively reach the fuel ports 374 disposed on the inner portion of the main fuel outlet 336. The diameter of the extension cylinder 400 (and hence the pre-mix chamber 332) is significantly smaller than the inside diameter of the fuel membrane 360. In this embodiment, the pre-mix chamber has a length (or height) to inside hydraulic diameter ratio in the range of from about 0.5:1 to about 4:1, more preferably in the range of from about 1:1 to about 3:1. Most preferably, the pre-mix chamber has a length (or height) to inside hydraulic diameter ratio in the range of from about 1.5:1.
Due to the smaller diameter of the extension shield 400, an annular space 430 exists between the internal sidewall 367 of the fuel membrane 360 and the exterior surface of the extension cylinder 400 (which is also the exterior surface 349 of the sidewall 346 of the pre-mix chamber 332). A plurality of thin, rectangular gusset plates 432 are utilized to center and hold the extension cylinder 400 (and hence the pre-mix chamber 332) within the fuel membrane 360. As illustrated, four plates 432 are disposed 90° apart within the annular space 430. One end of each plate 432 is attached to the internal sidewall 367 of the fuel membrane 360. The other end of each of the plates 432 is attached to the exterior surface of the extension cylinder 400 (which is also the exterior surface 349 of the sidewall 346 of the pre-mix chamber 332). Other than this above modification, the burner 330 illustrated by
The main fuel outlet 336 is still located in a position with respect to the top 342 of the pre-mix chamber such that fuel can be injected from the main fuel outlet 336 around the perimeter 368 of the air/fuel outlet 350 of the pre-mix chamber. The annular space 430 merely provides an air pathway between the extension cylinder and fuel membrane to allow fresh oxidizer to effectively reach the fuel ports 374 disposed on the inner portion of the main fuel outlet 336. The operation of the burner 330 remains the same, except fresh air is entrained from below the burner by the motive force of the inner row of fuel ports 374 through the annular space 430. The entrained air is in close proximity to the fuel being discharged by the inner row of fuel ports 374 on the main fuel outlet 336 and mixes therewith. For example, the enhanced mixing regimen provided by the annular space 430 is useful when relatively heavy and unsaturated fuel stocks, which tend to smoke more readily, are flared. It optimizes the burner for soot free combustion.
As will be understood by those skilled in the art, the same modification can also be made to the other three embodiments of the inventive flare burner described above. For example, in modifying the embodiment illustrated by
The partial pre-mix approach of the present invention allows two flame zones to be initiated within the same flame envelope as the fuel is flared. The outer flame zone is typical to what would normally be observed with a burner of the type utilized heretofore, i.e., a type utilizing only diffusion mixing. The outer layers of gas are shredded away to expose consecutive layers of gas for repeated diffusion and subsequent combustion. The second flame zone is created by the pre-mix zone of the burner which delivers a combustible mixture to the inside of the main flame envelope. This combusting flow field serves to create an appreciable turbulent regime at the core of the flame which is atypical of a normal diffusion flame. As the pre-mix zone becomes more fuel lean, the flame will become shorter due to the additional oxidizer delivered to the core of the flame. The excess air is utilized by the remaining flame cloud and functions to shorten the flame (or allow the mass flow to be increased) while also serving further as a quench mechanism to diminish emissions such as nitrous oxides and carbon monoxide. The excess air also reduces the formation of soot and results in the combustion of any unburned hydrocarbons.
Each of the flare burners 30, 130, 230 and 330 is preferably designed and operated such that the amount of air entrained into the pre-mix zone and injected into the central portion of the flame envelope is in the range of from about 15% to about 300% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone. Thus, both a fuel-rich approach (the injection of a mixture of fuel and air having less than 100% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone into the central portion of the flame envelope) and a fuel-lean approach (the injection of a mixture of fuel and air having more than 100% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone into the central portion of the flame envelope) can be utilized. Each approach has its own advantages as compared to the typical diffusion/free jet driven combustion regimen utilized heretofore. The particular approach utilized will depend upon the particular application including the type of fuel to be flared and the available pressure. The approach can be modified by typical porting and fuel delivery mechanisms.
When a fuel rich approach is utilized, the fraction of fuel injected into the center of the flame envelope will initiate a smaller envelope of combustion at the core of the flame which will serve to shorten the flame while also creating an additional turbulent combustion zone at the center of the flame envelope. When a fuel-lean approach is utilized, the flame envelope will be shortened appreciably due to the larger pre-mixed fuel fraction combusting at the core of the flame. The excess air carried by the pre-mix flow regimen then serves to further initiate combustion relative to the center of the remaining flame envelope. The additional turbulence created by the fuel expanding at the center of the flame during combustion then serves to increase the mixing regimen for the remaining fuel by fracturing the dense fuel core and pushing it to the outer flame boundary.
When a fuel-rich approach is utilized, it is important for the pre-mix stream delivered to the center of the flame envelope to remain within the range of combustibility. If not, the augmented mixing and combustion in the center of the flame envelope may not occur. The enhanced mixing is benefited by a pre-mixed flame which initiates at the core of the flame and expands at an appreciable velocity to create significant turbulence at the core of the flame.
In most applications, however, injection of a “lean” mixture of fuel and air (i.e., a mixture having more than 100% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone) into the central portion of the flame envelope is desired. In most applications, the amount of air entrained into the pre-mix zone and injected into the central portion of the flame envelope is in the range of from about 125% to about 300% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone. Preferably, the amount of air entrained into the pre-mix zone is in the range of from about 150% to about 300%, more preferably from about 175% to about 300%, of the stoichiometric amount of air required to support combustion of the fuel injected into the pre-mix zone. As the amount of excess air entrained into the pre-mix zone increases (that is, as the amount of air entrained into the pre-mix zone in excess of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone increases), the benefit with respect to flame length and emissions also increases. Although an amount of air entrained into the pre-mix zone greater than 300% of the stoichiometric amount of air required to support combustion of the fuel injected into the pre-mix zone would be advantageous, it would require an extraneous source of air entrainment (such as steam injection) and possibly other modifications, and may therefore be cost prohibitive.
The amount of air entrained into the pre-mix zones of each of the burners 30, 130, 230 and 330 is highly dependent on the pressure and mass flow of the fuel injected from the supplemental fuel inlet, the type of fuel being flared, the structure of the supplemental fuel inlet including the number and size of the ports therein, the placement of the supplemental fuel inlet with respect to the air inlet into the pre-mix chamber and the size of the air inlet. In most applications, the ultimate goal is to achieve a highly dilute, preferably inflammable mixture of fuel and air. An inflammable, lean mixture will quickly assimilate the fuel required to become again combustible once inside the core of the flame envelope. Once a flammable mixture is achieved, the air and gas will then create a large flame zone on the inside of the flame envelope which will significantly increase the rate at which the fuel is oxidized while also creating significant turbulence to augment the diffusion mixing on the external surface of the flame zone as well. The additional mass transported to the center of the flame envelope also serves as a quench mechanism to lower the production of emissions such as nitrous oxides and carbon monoxide. The added rate at which combustion occurs while maintaining two flame fronts also serves to lower the production of carbon monoxide and soot, and further reduces the release of unburned hydrocarbons.
The fuel is injected into the pre-mix zone with sufficient momentum to entrain air radially and from below the burner into the jet(s) of fuel and pre-mix zone. Depending upon the molecular weight of the fuel and the delivery pressure available for entrainment, the burner can entrain air from up to 2 feet below the supplemental fuel inlet.
Preferably, the amount of fuel introduced into the pre-mix zone of each of the burners 30, 130, 230 and 330 is in the range of from about 5% to about 50%, more preferably in the range of from about 10% to about 30%, of the total amount of fuel to be flared by the flare burner. Most preferably, the amount of fuel introduced into the pre-mix chamber is in the range of from about 10% to about 25% of the total amount of fuel to be flared by the flare burner. The amount of fuel introduced into the pre-mix zone can be controlled by manipulating the diameter of the fuel ports and the pressure of the fuel.
The greater the percentage of fuel introduced into the pre-mix zone, the shorter the flame and the greater the smokeless capacity of the burner. However, a proper balance between the percentage of fuel injected into the pre-mix zone and the amount of air that can be entrained into the pre-mix zone must be achieved. When a fuel-lean approach is utilized, it is usually important for the amount of air entrained into the pre-mix zone to be at least about 125% of the stoichiometric amount of air required to support combustion of the fuel injected into the pre-mix zone. A lesser amount of air could create a very reactive (combustible) mixture that could make the burner prone to either burn-back or flashback at maximum rates, eventually causing damage to the burner. The greater the amount of entrained air the greater the quench effect and the lower the flame speed of the fuel. This condition is ideal for augmenting the delay in ignition of the pre-mix stream in order to ensure that the ignition point of the pre-mix stream is local to the core of the flame prior to combustion for maximum benefit.
A sufficiently dilute stream of air and fuel will assure that the mixture of air and fuel is not ignited until the mixture exits the air/fuel outlet and reaches the center of the flame envelope. Once the mixture of fuel and air exits the air/fuel outlet and enters the flame envelope, the mixture then assimilates sufficient additional fuel to reach a combustible mixture at which time the fuel ignites inside the main flame envelope. This flow regimen creates a flame within a flame or a toroidal flame geometry combusting with two individual flame fronts. The additional turbulence created by the gas expanding at the center of the flame during combustion then serves to increase the mixing regimen for the remaining fuel by fracturing the dense fuel core and pushing it to the outer flame boundary. This approach reduces the flame's height and ability to smoke, while also increasing the overall combustion efficiency due to increased mixing.
It is important that the air/fuel mixture in the pre-mix zones of each of the burners 30, 130, 230 and 330 does not combust until it exits the air/fuel outlet of the pre-mix zone. Combustion inside of the pre-mix chamber, for example, would back pressure the pre-mix chamber and greatly reduce the amount of air entrained into the pre-mix chamber.
By delivering only a portion of the fuel to be flared to the pre-mix zones of each of the burners 30, 130, 230 and 330, the overall cross-sectional size of the burners is comparatively small. It would be size prohibitive to design and build a burner capable of supplying 100% of the air needed for combustion in a total pre-mix approach. The venturi or mixer portion of such a burner would necessarily be appreciably large and lack the ability to accommodate low fuel pressures.
Although the pre-mix chamber of each of the inventive burners 30, 130, 230 and 330 is relatively small, the set up is capable of providing sufficient air and fuel to create a pre-mixed air and fuel stream with an appreciable amount of entrained excess air. As a result, a significant increase in the overall flow of fuel may be realized with an equivalent flame height and diameter. Depending on the type of fuel to be flared, the inventive burners can easily accommodate a fuel flow rate that can be designed to deliver fuel in excess of 1.4 times the rate typically achievable by the diffusion jet-type burners utilized heretofore. In most cases, this can also be accomplished while maintaining roughly the same flame length and diameter. If a larger flame height can be tolerated, a fuel flow rate that is appreciably higher in flow rate can be achieved as compared to the diffusion jet-type burners utilized heretofore. In addition, in connection with each embodiment of the inventive burner, the ignition spacing and turn down capabilities can be conserved while the fuel flow rates are increased. In connection with low molecular weight fuels, the radiant fraction of the flame may also be somewhat decreased with the tempering of the flame, reducing the overall flame temperature. In some cases, this allows the burners to maintain or only minimally increase the distance between the burners and the fencing even though the fuel flow rate has been increased. The excess air delivered to the center of the flame serves not only to impart air to the center of the flame but also to decrease the timed rate in which the resulting fuel cloud is oxidized upon exiting the tip of the burner. This results in a cleaner, smoke-free flame that is proportionally shorter for a given heat release. The dilution and subsequent quench effect to the flame also serves to decrease nitrous oxide and carbon monoxide emissions. The flow of fuel and air through the pre-mix chamber also aids in cooling the burner assembly.
Various configurations of the supplemental fuel inlet have been described. Additional configurations are also possible, including multi-point injector bodies or headers drilled to maximize air entrainment and mixing in view of available fuel pressures. The lower section of each of the embodiments described above can include a Coanda surface or can be a straight section. If Coanda surfaces are utilized, the ports in the supplemental fuel inlet can be round orifices (jets) or slots. In addition to Coanda technology, the fuel can be injected from the supplemental fuel inlet at a relatively high velocity to rapidly achieve a mixture of fuel and air that can be injected into the center of the flame envelope. The dimensions of the various components of the inventive flare burner including the dimensions of the pre-mix chamber and fuel membrane can vary. Further, a myriad of port configurations (for example, sizes of ports; spacing between ports) can be used in association with the main fuel outlet and the supplemental fuel inlet. The particular dimensions and configurations utilized will depend on the type of fuel and the molecular weight, temperature, heating value and reactivity thereof, operational parameters (for example, the available pressure) and other factors.
Although it is not generally necessary, a tertiary inerting fluid can be injected into the pre-mix zone of the inventive flare burner (any of the embodiments of the flare burner) to enhance the entrainment of air into the pre-mix zone. Examples of tertiary inerting fluids that can be used include steam, air and nitrogen. Steam is preferred.
The drawings illustrate round and rectangular (polygonal) embodiments of the inventive flare burner. Each embodiment of the inventive flare burner can be formed in other geometries as well. For example, in addition to round and rectangular shapes, elliptical, triangular, square, pentagonal, octagonal and other polygonal shapes can be employed. These other geometric shapes may prove beneficial from a cost or fabrication standpoint. The optimum approach is to create a dilute excess air stream which can then be delivered from the pre-mix chamber to the center of the main body of the flame. A fuel rich stream, however, still offers benefits over the diffusion only type burners utilized heretofore due to the enhanced mixing created by the inventive burner.
The Inventive Ground FlareReferring now to
The flare burners are arranged in rows 430(a)-(f) and rows 432(a)-(e). Rows 430(a)-(f) form a first stage 434 of the flare burners 422, whereas the rows 432(a)-(e) form a second stage 436 of the flare burners. At least one of the flare burners 422 is one of the embodiments of the inventive flare burner described above. Preferably, each of the flare burners 422 in the second stage 436 of flare burners 422 (the burners utilized when a relatively high volume of fuel needs to be flared) is one of the embodiments of the inventive flare burner described above. If desired, each of the flare burners 422 in both the first stage 434 of burners and the second stage 436 of burners is one of the embodiments of the inventive flare burner described above.
The fuel supply line 426 comprises a main line 440 which terminates in a distribution manifold 442. A first stage supply line 444 and a second stage supply line 446 are attached and in fluid communication with the distribution manifold 442. Individual first stage supply lines 450(a)-(f) run from the first stage fuel supply line 444 to corresponding burner rows 430(a)-(f). Similarly, individual second stage supply lines 452(a)-(e) run from the second stage fuel supply line 446 to corresponding burner rows 432(a)-(e). For example, the first end 382 of the main branch 380 of the fuel feed conduit 338 of the inventive flare burner 330 is attached to one of the individual supply lines 450(a)-(f) or 452(a)-(e). If another type of flare burner is also utilized in the ground flare 420, the fuel feed conduit of such burner is attached as appropriate to one of the individual supply lines 450(a)-(f) or 452(a)-(e).
A series of pilots 460(a)-(f) are in fluid communication with the first stage supply line 444 and positioned with the appropriate burner and fuel separation prior to ignition. Pilots are typically located adjacent to the first flare burner 422 in corresponding rows 430(a)-(f). Similarly, a series of pilots 462(a)-(e) are in fluid communication with the second stage supply line 446 and positioned adjacent to the first flare burner 422 in corresponding rows 432(a)-(e).
The enclosure 424 surrounds the flare burners 422 and comprises a plurality of posts 470 and fence sections 472 connected between the posts. The enclosure or fence is in the range of from about 30 feet to about 60 feet high. The enclosure 424 is designed such that air can be pulled into the ground flare through and under the enclosure.
In operation of the inventive ground flare 420, fuel to be flared is conducted through the main line 440 to the distribution manifold 442. A valve control system (not shown) functions to distribute the fuel to either the first stage fuel supply line 444 or both the first stage fuel supply line 444 and the second stage fuel supply line 446. If a relatively low volume of fuel is conducted to the distribution manifold 442, the valve system directs the fuel only to the first stage fuel supply line 444. If the volume of fuel gas conducted to the distribution manifold 442 is relatively high, the fuel is conducted to both the first stage fuel supply line 444 and the second stage fuel supply line 446. Additional staging can also be incorporated to cycle in and out as needed. Fuel is conducted from one or both of the fuel supply lines 444 and 446, depending on the volume of the fuel, to the corresponding individual supply lines 450(a)-(f) and/or 452(a)-(e). The fuel is conducted from the individual supply lines 450(a)-(f) and/or 452(a)-(e) to the flare burners 422 in the corresponding rows 430(a)-(f) and 432(a)-(e).
As necessary, the pilots 460(a)-(f) and 460(a)-(e) ignite the fuel discharged from the corresponding first burner 422 in each of the row. The ignited fuel from the first burner 422 in each row then ignites the fuel being discharged from the adjacent burner which in turn ignites the fuel being discharged from the next burner in the row and so on until the fuel being discharged from each of the burners in the row has been ignited. The air required for combustion is pulled through and/or under the walls of the enclosure 424. It is not necessary to separately supply air to the burners 422 or ground flare.
The inventive ground flare can be used to combust from a relatively small volume of fuel (for example, 3,000 pounds per hour or less) to a very large volume of fuel gas (for example, 10,000 to 15,000 pounds per hour and up depending on the molecular weight of the fuel to be flared, pressure availability, temperature and other factors). Even at a very high flow rate (for example, 10,000 pounds per hour), the flame envelope created by the inventive ground flare burner can be contained in a typical ground flare enclosure. Due to the structure of the inventive flare burner, a higher volume of fuel can be flared with smaller ports and higher pressures without significantly increasing the height of the flame envelopes created by the ground flare. Alternatively, the flame heights can be decreased allowing the enclosure 424 to be reduced in height. The inventive burners pump air from below the burners which allows the burners to be placed closer to the ground, again resulting in a reduction in the required height of the enclosure 424. A smaller portion of land may be required due to a smaller number of burners and related components.
In many cases, existing ground flares can be retrofitted with the inventive flare burner 422 to allow more fuel to be flared without causing the height of the flame envelope to significantly exceed the height of the enclosure surrounding the ground flare. Also, due to the structure of the burner, the smokeless rate for a given flare tip may be significantly larger in range. With a realized increase in throughput, more gas can be delivered per an individual header. This can result in fewer headers coupled with fewer control mechanisms such as gas control valves, shut-off valves, regulators and physical piping. Increased capacity with fewer headers also allows for a smaller enclosure 434.
The inventive ground flare can be used to flare various types of fuel gas. Examples include saturated and unsaturated hydrocarbons such as propane and propylene and mixtures thereof, alone or with hydrogen, water vapor and/or inert gases such as nitrogen, carbon monoxide, argon, etc.
The above description of the inventive ground flare is intended to illustrate the ground flare and particularly how the inventive flare burner is used in association therewith. As understood by those skilled in the art, ground flare installations can vary widely in terms of how they are configured, the number and types of burners, headers, flow systems, control valves and related components, the type and height of the enclosure surrounding the installation and in many other ways. The inventive ground flare encompasses any ground flare installation in which the inventive flare burner is utilized.
The Inventive MethodIn accordance with the inventive method, fuel is burned in one of the inventive flare burners 30, 130, 230, or 330. Referring to
As discussed above, the amount of air entrained into the pre-mix zone and injected into the central portion of the flame envelope is preferably at least about 15% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone. In some applications, injection of a “fuel-rich” mixture of fuel and air (i.e., a mixture having less than 100% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone) into the central portion of the flame envelope is suitable. In most applications, however, injection of a “lean” mixture of fuel and air (i.e., a mixture having more than 100% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone) into the central portion of the flame envelope is desired. In most applications, the amount of air entrained into the pre-mix zone and injected into the central portion of the flame envelope is in the range of from about 125% to about 300% of the stoichiometric amount of air required to support combustion of the fuel introduced into the pre-mix zone.
The amount of fuel introduced into the pre-mix zone and pre-mix chamber (i.e., the pre-mix chamber 32, 132, 232 or 332) is in the range of from about 5% to about 50%, more preferably from about 10% to about 30%, most preferably from about 10% to about 25%, of the total amount of fuel to be flared by the flare burner.
In order to further illustrate the invention, the following examples are given.
EXAMPLE 1The first embodiment of the inventive flare burner, flare burner 30, was compared to a prior art high capacity diffusion-type ground flare burner, namely the burner illustrated in
The inventive flare burners were first tested singularly. Tests were carried out using propane and propylene. Approximately 20% of the fuel was injected into the pre-mix chamber of each of the inventive flare burners. The remaining fuel was then injected around the perimeter of the air/fuel mixture discharged from the pre-mix chamber. It was determined that with both types of fuels, each of the inventive flare burners were able to support a significant flow of fuel while developing a smokeless flame. The flame envelope from each burner was found to be very stable, capable of significant turndown ratios, and also very symmetrical throughout the range of heat releases fired. The flame envelopes from each burner were observed as being very short in length and having a small diameter.
The inventive flare burner having a length of approximately 30 inches was then compared to the prior art burner. The two flare burners were tested side by side. The burners were attached to the same header to insure that the same volume of fuel was supplied to each burner.
It was observed that the inventive flare burner produced a shorter flame envelope in most of the test points observed. The inventive flare burner remained lit at lower pressures during turn down, indicating a somewhat expanded range of operability. At maximum fuel flow rates, the flame envelope generated by the inventive flare burner was shorter in overall length as compared to the prior art high capacity diffusion-type ground flare burner. In this scenario, however, the vertical cross-section (width) of the flame envelope created by the prior art flare burner was larger than the flame envelope created by the inventive flare burner. No burn-back was observed with the inventive flare burner until the pressure was notably under 1 psig. Radiation from the flame envelope generated by the inventive flare burner appeared to be equivalent to or slightly less than the radiation generated by the flame envelope produced by the prior art flare burner. During turn down conditions, the prior art flare burner smoked at approximately the same rate as the inventive flare burner. Trailing smoke typically could be noted from both burners at about the same flow rate and pressure. However, the inventive flare burner appeared to maintain a less dense trail of smoke at lower pressures than the diffusion type burner tip during initial testing. The prior art burner transitioned to heavier smoke production as pressure was reduced.
EXAMPLE IIThe third embodiment of the inventive flare burner, flare burner 230, was also tested and compared to the prior art flare burner discussed above. The performance of this embodiment of the inventive flare burner appeared to be at least equivalent to the prior art burner. However, the inventive burner produced more smoke at low pressure than the first embodiment of the inventive flare burner described in Example I. The range of smokeless operation was comparative to the smokeless performance of the prior art flare burner.
In this test, the corners of the pre-mix chamber of the inventive flare burner created complex flow patterns which visually appeared to inhibit the mixing regimen in the pre-mix chamber to some extent. As a result, spurious stratified fuel rich zones were observed to form at the corners of the pre-mix discharge area, resulting in visible smoke strata observed throughout the surface of the flame zone. On the other hand, the inventive flare burner tested was able to handle almost three times the amount of fuel that could be handled by the prior art flare burner.
A weld used in assembling the test unit of the inventive flare burner described in this example was faulty and ultimately failed (only after appreciable testing was carried out). The weld in question was utilized only for the test unit (which was made out of carbon steel); the failure of the weld was not due to a design issue and has no relevance to the operation or performance of the actual burner. In any event, the tests showed that the flare burner 230 is very capable of handling large fuel flows with minor smoke issues.
Thus, the present invention is well adapted to carry out the objects and attain the ends and advantages mentioned as well as those which are inherent therein. While numerous changes may be made by those skilled in the art, such changes are encompassed within the spirit of this invention as defined by the appended claims.
Claims
1. A flare burner, comprising:
- a pre-mix zone including a pre-mix chamber, said pre-mix chamber having a top, a bottom, a sidewall connecting said top to said bottom, an air inlet disposed in one of said bottom and said sidewall and an air/fuel outlet disposed in said top;
- a supplemental fuel inlet for injecting fuel into said pre-mix zone, said supplemental fuel inlet being located in a position with respect to said pre-mix zone such that the injection of fuel from said supplemental fuel inlet into said pre-mix zone entrains air into said pre-mix zone whereby a mixture of fuel and air is formed in said pre-mix zone and caused to exit said air/fuel outlet of said pre-mix chamber; and
- a main fuel outlet located in a position with respect to said top of said pre-mix chamber such that fuel can be injected from said main fuel outlet around the perimeter of said air/fuel outlet of said pre-mix chamber.
2. The flare burner of claim 1 wherein said air inlet is disposed in said bottom of said pre-mix chamber.
3. The flare burner of claim 1 wherein said main fuel outlet is spaced outwardly from said pre-mix chamber to provide an air entrainment space therebetween.
4. The flare burner of claim 1 further comprising a fuel membrane disposed around the outside perimeter of said pre-mix chamber, said membrane including a fuel inlet and being in fluid communication with said main fuel outlet.
5. The flare burner of claim 4 wherein said fuel membrane and said main fuel outlet are spaced outwardly from said pre-mix chamber to provide an air entrainment space therebetween.
6. The flare burner of claim 4 wherein said membrane is also in fluid communication with said supplemental fuel inlet.
7. The flare burner of claim 1 further comprising a fuel feed conduit in fluid communication with said supplemental fuel inlet and said main fuel outlet for conducting fuel to said supplemental fuel inlet and said main fuel outlet.
8. The flare burner of claim 1 wherein said main fuel outlet comprises a plurality of fuel ports disposed around the perimeter of said air/fuel outlet of said pre-mix chamber.
9. The flare burner of claim 4 wherein said pre-mix chamber, including said air/fuel outlet, and said fuel membrane and said main fuel outlet each have a round cross-section such that fuel can be injected annularly from said main fuel outlet around the perimeter of said air/fuel outlet.
10. The flare burner of claim 1 wherein said sidewall of said pre-mix chamber includes an interior surface and an exterior surface, said interior surface having a section that is a Coanda surface.
11. The flare burner of claim 10 wherein said supplemental fuel inlet is located in a position with respect to said pre-mix chamber such that fuel can be injected from said supplemental fuel inlet onto said Coanda surface.
12. The flare burner of claim 4 wherein said sidewall of said pre-mix chamber includes an interior surface and an exterior surface, said interior surface having a section that is a Coanda surface.
13. The flare burner of claim 12 wherein:
- said air inlet is disposed in said bottom of said pre-mix chamber and said pre-mix chamber, including said air inlet, and said membrane and said supplemental fuel inlet each have a round cross-section; and
- said Coanda surface annularly extends around said interior surface of said sidewall of said pre-mix chamber.
14. The flare burner of claim 13 wherein said supplemental fuel inlet is located in a position with respect to said pre-mix chamber such that fuel can be annularly injected from said supplement fuel inlet onto said Coanda surface.
15. The flare burner of claim 10 wherein said interior surface includes two opposing sections that are Coanda surfaces, and said supplemental fuel inlet is in a position with respect to said pre-mix chamber such that fuel can be injected from said supplement fuel inlet onto each of said Coanda surfaces.
16. The flare burner of claim 1 wherein said pre-mix chamber has a length to inside hydraulic diameter ratio in the range of from about 0.25:1 to about 4:1.
17. The flare burner of claim 1 wherein said pre-mix chamber has a length to inside hydraulic diameter ratio of about 1:1 or less.
18. A flare burner, comprising:
- a pre-mix zone including a pre-mix chamber, said pre-mix chamber having a top, a bottom, a sidewall connecting said top to said bottom, an air inlet disposed in said bottom, an air/fuel outlet disposed in said top and a length to inside hydraulic diameter ratio in the range of from about 0.25:1 to about 4:1;
- a supplemental fuel inlet for injecting fuel into said pre-mix zone, said supplemental fuel inlet being located in a position with respect to said pre-mix zone such that the injection of fuel from said supplemental fuel inlet into said pre-mix zone entrains air into said pre-mix zone whereby a mixture of fuel gas and air is formed in said pre-mix zone and caused to exit said air/fuel outlet of said pre-mix chamber;
- a main fuel outlet located in a position with respect to said top of said pre-mix chamber such that fuel can be injected from said main fuel outlet around the perimeter of said air/fuel outlet of said pre-mix chamber; and
- a fuel feed conduit in fluid communication with said supplemental fuel inlet and said main fuel outlet for conducting fuel to said supplemental fuel inlet and said main fuel outlet.
19. The flare burner of claim 18 wherein said pre-mix chamber, including said air inlet and said air/fuel outlet, and said main fuel outlet have round cross-sections.
20. The flare burner of claim 18 wherein said main fuel outlet is spaced outwardly from said pre-mix chamber to provide an air entrainment space therebetween.
21. The flare burner of claim 19 further comprising an annular fuel membrane disposed around the outside perimeter of said pre-mix chamber, said membrane being in fluid communication with said main fuel outlet and having a top, a bottom and a sidewall connecting said top to said bottom.
22. The flare burner of claim 21 wherein said main fuel outlet is attached to said top of said fuel membrane and comprises a plurality of fuel ports extending around the perimeter of said air/fuel outlet of said pre-mix chamber.
23. The flare burner of claim 22 wherein said fuel membrane and said main fuel outlet are spaced outwardly from said pre-mix chamber to provide an air entrainment space therebetween.
24. The flare burner of claim 18 wherein said pre-mix chamber has a length to inside hydraulic diameter ratio of about 1:1 or less.
25. The flare burner of claim 24 wherein said supplemental fuel inlet is spaced below said air inlet of said pre-mix chamber.
26. The flare burner of claim 18 wherein said air/fuel outlet of said pre-mix chamber is spaced above said main fuel outlet.
27. A ground flare comprising a plurality of flare burners, an enclosure extending around the flare burners and a fuel supply line for supplying fuel to the flare burners, wherein at least one of the flare burners includes:
- a pre-mix zone including a pre-mix chamber having a top, a bottom, a sidewall connecting said top to said bottom, an air inlet disposed in one of said bottom and said sidewall and an air/fuel outlet disposed in said top;
- a supplemental fuel inlet for injecting fuel into said pre-mix zone, said supplemental fuel inlet being located in a position with respect to said pre-mix zone such that the injection of fuel from said supplemental fuel inlet into said pre-mix zone entrains air into said pre-mix zone whereby a mixture of fuel gas and air is formed in said pre-mix zone and caused to exit said air/fuel outlet of said pre-mix chamber; and
- a main fuel outlet located in a position with respect to said top of said pre-mix chamber such that fuel can be injected from said main fuel outlet around the perimeter of said air/fuel outlet of said pre-mix chamber.
28. The ground flare of claim 27 wherein said air inlet is disposed in said bottom of said pre-mix chamber.
29. The ground flare of claim 27 wherein said main fuel outlet is spaced outwardly from said pre-mix chamber to provide an air entrainment space therebetween.
30. The ground flare of claim 27 wherein said flare burner further comprises a fuel membrane disposed around the outside perimeter of said pre-mix chamber, said membrane including a fuel inlet and being in fluid communication with said main fuel outlet.
31. The ground flare of claim 30 wherein said fuel membrane and said main fuel outlet are spaced outwardly from said pre-mix chamber to provide an air entrainment space therebetween.
32. The ground flare of claim 30 wherein said membrane is also in fluid communication with said supplemental fuel inlet.
33. The ground flare of claim 27 further comprising a fuel feed conduit in fluid communication with said supplemental fuel inlet and said main fuel outlet for conducting fuel to said supplemental fuel inlet and said main fuel outlet.
34. The ground flare of claim 27 wherein said main fuel outlet comprises a plurality of fuel ports disposed around the perimeter of said air/fuel outlet of said pre-mix chamber.
35. The ground flare of claim 30, wherein said pre-mix chamber, including said air/fuel outlet, and said fuel membrane and said main fuel outlet each have a round cross-section whereby fuel can be annularly injected from said main fuel outlet around the perimeter of said air/fuel outlet.
36. The ground flare of claim 27 wherein said sidewall of said pre-mix chamber includes an interior surface and an exterior surface, and said interior surface having a section that is a Coanda surface.
37. The ground flare of claim 36 wherein said supplemental fuel outlet is located in a position with respect to said pre-mix chamber such that fuel can be injected from said supplemental fuel outlet onto said Coanda surface.
38. The ground flare of claim 30 wherein said sidewall of said pre-mix chamber includes an interior surface and an exterior surface, said interior surface having a section that is a Coanda surface.
39. The ground flare of claim 38 wherein:
- said air inlet is disposed in said bottom of said pre-mix chamber and said pre-mix chamber, including said air inlet, and said fuel membrane and said supplemental fuel inlet each have a round cross-section; and
- said Coanda surface annularly extends around said interior surface of said sidewall of said pre-mix chamber.
40. The ground flare burner of claim 39 wherein said supplemental fuel inlet is in a position with respect to said pre-mix chamber such that fuel can be annularly injected from said supplemental fuel inlet onto said Coanda surface.
41. The ground flare burner of claim 36 wherein said interior surface includes two opposing sections that are Coanda surfaces, and said supplemental fuel inlet is in a position with respect to said pre-mix chamber such that fuel can be injected from said supplement fuel inlet onto each of said Coanda surfaces.
42. In a method of flaring fuel with a flare burner wherein fuel to be flared is injected through a fuel outlet of the burner into a combustion zone and ignited to create a flame envelope and combust the fuel, the improvement comprising:
- introducing a portion of the fuel to be burned into a pre-mix zone of said burner in a manner that entrains air into said pre-mix zone and creates a mixture of air and fuel within said pre-mix zone; and
- injecting said mixture of air and fuel from said pre-mix zone into a central portion of said flame envelope.
43. The method of claim 42 wherein the amount of air entrained into said pre-mix zone and injected into said central portion of said flame envelope is in the range of from about 125% to about 300% of the stoichiometric amount of air required to support combustion of the fuel introduced into said pre-mix zone.
44. The method of claim 43 wherein the amount of air entrained into said pre-mix zone and injected into said central portion of said flame envelope is in the range of from about 150% to about 300% of the stoichiometric amount of air required to support combustion of the fuel introduced into said pre-mix zone.
45. The method of claim 42 wherein the amount of the fuel introduced into said pre-mix zone is in the range of from about 5% to about 50. % of the total amount of fuel to be flared by said flare burner.
46. The method of claim 45 wherein the amount of the fuel introduced into said pre-mix zone is in the range of from about 10% to about 30% of the total amount of fuel to be flared by said flare burner.
Type: Application
Filed: Sep 29, 2006
Publication Date: Apr 3, 2008
Inventors: Roger L. Poe (Beggs, OK), James Wilkins (Fleet), Jeff W. White (Glenpool, OK)
Application Number: 11/540,362
International Classification: F23G 7/08 (20060101);