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.
Referring 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.
In 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.
The 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.
The 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.