WO2023057722A1 - Device for injecting dihydrogen and air - Google Patents
Device for injecting dihydrogen and air Download PDFInfo
- Publication number
- WO2023057722A1 WO2023057722A1 PCT/FR2022/051883 FR2022051883W WO2023057722A1 WO 2023057722 A1 WO2023057722 A1 WO 2023057722A1 FR 2022051883 W FR2022051883 W FR 2022051883W WO 2023057722 A1 WO2023057722 A1 WO 2023057722A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- channel
- internal
- dihydrogen
- internal channel
- downstream end
- Prior art date
Links
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 92
- 238000002485 combustion reaction Methods 0.000 claims abstract description 41
- 238000002347 injection Methods 0.000 claims abstract description 39
- 239000007924 injection Substances 0.000 claims abstract description 39
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 21
- 239000000203 mixture Substances 0.000 claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 2
- 229930195733 hydrocarbon Natural products 0.000 abstract description 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract description 2
- 239000010419 fine particle Substances 0.000 abstract 1
- 239000000779 smoke Substances 0.000 abstract 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 18
- 239000003350 kerosene Substances 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- 206010016754 Flashback Diseases 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 230000006641 stabilisation Effects 0.000 description 6
- 238000011105 stabilization Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000008033 biological extinction Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000014509 gene expression Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23R—GENERATING COMBUSTION PRODUCTS OF HIGH PRESSURE OR HIGH VELOCITY, e.g. GAS-TURBINE COMBUSTION CHAMBERS
- F23R3/00—Continuous combustion chambers using liquid or gaseous fuel
- F23R3/02—Continuous combustion chambers using liquid or gaseous fuel characterised by the air-flow or gas-flow configuration
- F23R3/04—Air inlet arrangements
- F23R3/10—Air inlet arrangements for primary air
- F23R3/12—Air inlet arrangements for primary air inducing a vortex
- F23R3/14—Air inlet arrangements for primary air inducing a vortex by using swirl vanes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23R—GENERATING COMBUSTION PRODUCTS OF HIGH PRESSURE OR HIGH VELOCITY, e.g. GAS-TURBINE COMBUSTION CHAMBERS
- F23R3/00—Continuous combustion chambers using liquid or gaseous fuel
- F23R3/28—Continuous combustion chambers using liquid or gaseous fuel characterised by the fuel supply
- F23R3/286—Continuous combustion chambers using liquid or gaseous fuel characterised by the fuel supply having fuel-air premixing devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23R—GENERATING COMBUSTION PRODUCTS OF HIGH PRESSURE OR HIGH VELOCITY, e.g. GAS-TURBINE COMBUSTION CHAMBERS
- F23R2900/00—Special features of, or arrangements for continuous combustion chambers; Combustion processes therefor
- F23R2900/00002—Gas turbine combustors adapted for fuels having low heating value [LHV]
Definitions
- This document concerns turbomachines whose combustion chamber is fed by separate injections of dihydrogen and air.
- a principle of micro-mixture burners of air and dihydrogen is known.
- such burners do not guarantee the thermal resistance of a pierced wall or the absence of flashback in the dihydrogen injection device.
- These burners also have a complex geometry system.
- Such burners have a high production cost, a high pressure drop and these burners are specific to a given combustion chamber architecture.
- This document relates to a longitudinal axis dihydrogen injection device intended to be mounted on an annular bottom of an annular combustion chamber of a turbomachine comprising an internal channel for the circulation of dihydrogen and an external annular channel circulation of a mixture comprising at least air, the internal channel and the external annular channel being coaxial, an internal swirl being housed in the internal channel and an external swirling being housed in the external annular channel, and wherein a downstream end of the inner channel is arranged upstream, at a distance r, from a downstream end of the outer annular channel.
- This device makes it possible to produce a dihydrogen/air flame which can be used in turbomachines which makes it possible both to produce low levels of nitrogen oxide emissions, a reduced thermal load on the combustion chamber and the injector as well as eliminating the risk of flashback.
- this injector has the particularity of being both simple to produce and easily adaptable to existing turbomachines running on kerosene.
- a spin makes it possible to put a flow into rotation.
- the integration of an internal spin in the internal channel makes it possible to create a recirculation zone for a flow of dihydrogen crossing said internal channel and preventing the combustion of the air and dihydrogen mixture from coming to stabilize on the downstream end of the internal channel .
- recirculation zone is meant a zone generating a centrifugation effect with a depression inside capable of producing an axial velocity component of the flow on average negative with respect to a main direction of the flow. This recirculation zone is similar to that generated inside a whirlpool in which air is sucked.
- the internal recirculation zone blocks part of the flow of dihydrogen along the longitudinal axis of said internal channel generating in an outlet section of this internal channel significant overspeeds near the walls of the internal channel with respect to a flow with uniform axial flow rate.
- the rotation of the dihydrogen of the internal channel makes it possible to avoid hanging the flame on the downstream ends of the internal channel by stabilizing it aerodynamically above the internal channel.
- the downstream end of the internal channel being arranged upstream at a distance r, this further prevents the flame from catching on the lips of the internal channel.
- This rotation of the dihydrogen in the internal channel avoids the installation of a complex cooling device for the dihydrogen injection device.
- This dihydrogen injection device produces limited pressure drops compared to other liquid injection devices using kerosene as in the prior art.
- This dihydrogen injection device has a simple geometry, a low production cost and adapts to existing combustion chamber architectures.
- This remote flame stabilization facilitates partial mixing between the mixture containing at least air with the dihydrogen exiting the internal channel, upstream of the flame, and avoiding any risk of flame rising in said channel internal and the external channel, also called "flashback" in English.
- flashback This makes it possible to achieve a combustion depleted of dihydrogen in the combustion chamber.
- the internal channel may be a tubular central channel.
- At least the internal twist of the internal channel may have a helical shape.
- This helical shape makes it possible to improve the aerodynamics of the flow of dihydrogen passing through the internal spin.
- the inner swirler can be arranged along the longitudinal axis downstream of the outer swirler.
- a rate of rotation S generated by the internal spin of the internal channel defined as a ratio between a tangential speed and a delivery speed along the longitudinal axis of a hydrogen flow at the outlet of the internal spin, can be equal or greater than 0.6.
- the internal spin of the internal channel can be arranged upstream, at a distance l, from the downstream end of the internal channel.
- the internal channel may have an internal diameter d and the external annular channel may have an internal diameter D such that a D/d ratio is between 3 and 10.
- a thickness of a wall of the internal channel e is such that an e/d ratio can be between 0.05 and 0.7.
- An l/d ratio can be between 1 and 3.
- the minimum distance l min is equal to 1 d so that a central recirculation zone enters the internal channel.
- the range chosen for l/d makes it possible to obtain a good compromise and a rotation rate S sufficient to correctly rotate the flame.
- the distance r can be between 0.05D and 0.5D. [0023] There is an optimum value for the distance r which depends on the diameter D of the outer channel. If this distance r is too high, the recirculation zone becomes unstable. The range of values chosen for r is optimized so as to obtain a stable recirculation zone.
- This distance r relative to the downstream end of the outer annular channel makes it possible to increase the operating range where the flame is detached by moving back a dihydrogen introduction zone relative to the aerodynamic stabilization zone of the flame. .
- the external spin of the external annular channel can be arranged at an upstream end of said external annular channel, at a distance L from the downstream end of the external annular channel.
- the distance L can be between 1D and 5D.
- the rate of rotation S can be greater than 0.6, a flow rate Ui of the dihydrogen in the internal channel being greater than a critical value Ui, c and verifying the following relationship:
- - P is a pressure in the annular combustion chamber
- T - T a is an air temperature in Kelvin in the external channel
- This critical value Ui, c ensures that the flame formed at the outlet of the injection device is detached from the downstream ends of the internal channel for a wide range of engine operation.
- the mixture may be air.
- This document relates to an assembly comprising the device of the aforementioned type, in which the internal channel, fluidly connected to means for supplying dihydrogen, comprises the internal swirler configured to rotate said dihydrogen, and the external annular channel , fluidly connected to air supply means, comprises the external swirler configured to rotate said air.
- FIG. 1 shows a turbomachine comprising a dihydrogen injection device arranged in an annular bottom of an annular combustion chamber according to three configurations.
- FIG. 2 shows the hydrogen injection device according to the invention.
- FIG. 3 schematically shows the formation of a recirculation zone which penetrates the dihydrogen injection device and a flame at the outlet of the dihydrogen injection device.
- FIG. 4 shows a plurality of possible configurations (FIGS. A, B, C, D, E, F, G, H) of internal channel, according to the invention.
- FIG. 5 shows a plurality of possible configurations (figures. A, B, C, D, E) of the downstream end of the outer annular channel, according to the invention.
- This document relates to a dihydrogen injection device 2 intended to be mounted on an annular bottom of an annular combustion chamber 4 of a turbomachine.
- This dihydrogen injection device 2 is used in a lean dihydrogen combustion configuration such that the flame temperatures and the formation of nitrogen oxide are reduced. It is said that the injection device is lean when there is excess oxygen in relation to combustion taking place at stoichiometry between dihydrogen and air and that the injection system is rich when there is dihydrogen in excess with respect to this combustion at stoichiometry. Combustion at stoichiometry is defined as that for which there is the right number of hydrogen and oxygen atoms necessary to consume all the fuel and only water remains in the combustion products. It is in the context of lean combustion in dihydrogen that the present invention is placed.
- the dihydrogen injection device 2 is located between the compressor and the high-pressure turbine, on the annular bottom of the annular combustion chamber 4 or on an outer shroud.
- said dihydrogen injection device comprises an internal channel 6 and an external annular channel 8.
- the internal channel 6 and the external annular channel 8 are coaxial.
- a first gas is injected from an inlet 10 located at an upstream end of the internal channel 6.
- This first gas is dihydrogen 12.
- the internal channel 6 has an internal diameter d.
- the choice of the internal diameter d of the channel depends on a desired thermal power.
- a thickness of an inner channel wall e is half the difference of an outer diameter of the inner channel and an inner diameter of the inner channel d.
- An e/d ratio is between 0.05 and 0.7.
- This internal channel 6 comprises an internal twist 14 configured to rotate a flow of dihydrogen 12 around a longitudinal axis X.
- Said internal twist 14 of the internal channel 6 is arranged at a distance l from a downstream end 16 of the internal channel.
- the distance l between the downstream end 16 of the internal channel 6 and a downstream end 18 of the internal spinner 14 is between 1d and 5d.
- a space is thus left between the internal swirler 14 and the downstream end 18 of the internal channel 6 so that a central recirculation zone 20 can be installed.
- the recirculation zone is a region around the longitudinal axis X of the injection device where an axial component of the flow is on average negative with respect to a main direction of the flow.
- This recirculation zone 20 is generated by a depression created inside the rotational movement of the flow. This depression is due to the centrifugation effect induced by this rotation of the flow.
- the recirculation zone 20 is similar to that generated inside a vortex in which air is sucked.
- the recirculation zone 20 is configured to penetrate inside the internal channel blocking part of the section of the downstream end 16 of the internal channel 6 and producing an acceleration of the flow at the periphery. This repels a flame 22 formed at the outlet of the injection device and sets it in rotation.
- the internal swirl 14 may, for example, comprise a helical part with a suitable helix pitch.
- This helix pitch is configured to define a positioning of the flame 22 at the outlet of the injection device 2, to minimize polluting emissions and define a thermal injection device.
- This helical part rotates the flow of dihydrogen with a rate of rotation characterized by a dimensionless number S.
- This rate of rotation S is defined as a ratio of an angular momentum to the product of a radius of the channel multiplied by an impulse of the flow of dihydrogen 12 set in rotation, according to the following formula: where G e is the angular momentum of the flow in an axial direction, G z is the momentum of the flow in the axial direction and d is the diameter of the channel.
- Approximate expressions are generally used to estimate G e and G z based on the tangential and axial velocities of the flow set in rotation in the channel.
- S corresponds to the ratio of a tangential speed divided by an axial speed.
- the tangential speed corresponds to a rotational component of the speed with respect to the injection axis.
- a rate of blockage of the flow of dihydrogen 12 in the internal channel 6 is established so as to be high enough to repel the flame 22 forming at a downstream end 24 of the outer annular channel 8.
- the blockage rate represents a ratio between a section occupied by the recirculation zone 20 rising inside the dihydrogen injection device 12 at the level of the downstream end 16 of the internal channel 6 with respect to a passage section of the internal channel 6.
- This blocking rate depends on the shape of the recirculation zone 20. More specifically, it is an aerodynamic element which depends on the dimensional parameters of the dihydrogen injection device 2.
- the rate of rotation S is at least equal to 0.6 and an l/d ratio is between 1 and 3.
- the downstream end 16 of the internal channel 6 can comprise variable thicknesses as well as different shapes.
- downstream end 16 of the internal channel 6 has a straight and longitudinal wall.
- downstream end 16 of the internal channel 6 has a flare shape. This downstream end 16 is configured to modify the flow of the internal channel 6 near the wall of the end 16.
- the downstream end 16 of the internal channel 6 has an outward cap effect. This downstream end 16 is configured to modify the flow of the external channel 8 near the wall of the end 16.
- the downstream end 16 of the internal channel 6 has a section which increases downstream. This fourth type of downstream end is configured to promote the increase in the rate of rotation S in the internal channel 6 containing the dihydrogen 12. Due to this configuration, the axial speed is reduced and the tangential speed is increased, hence the increase in the rate of rotation S.
- This downstream end 16 is configured to modify the flow of the internal channel 6 near the wall of the end 16 as well as the flow of the external channel 8 near the wall of the end 16.
- a thickness corresponding to a transverse dimension of a wall of the internal channel 6 is lower or greater than that in the first embodiment.
- downstream end 16 of the internal channel 6 has a bevel effect. This downstream end 16 is configured to modify the flow of the external channel 8 near the wall of the end 16.
- downstream end 16 of the internal channel 6 has an inward cap effect. This downstream end 16 is configured to modify the flow of the internal channel 6 near the wall of the end 16.
- the downstream end 16 comprises a section which is reduced downstream. This downstream end 16 is configured to modify the flow of the internal channel 6 near the wall of the end 16 as well as the flow of the external channel 8 near the wall of the end 16.
- the downstream end 16 of the internal channel 6 is arranged upstream with respect to the downstream end 24 of the external annular channel 8.
- the downstream end 24 of the external annular channel 8 is arranged at a distance r from the downstream end 16 of the internal channel 6.
- This external annular channel 8 has an internal diameter D, such that a ratio D/d with the diameter d of the internal channel 6 is between 3 and 10.
- the outer annular channel 8 is configured to receive a second gas comprising air or an air and dihydrogen mixture. This gas enters the outer annular channel through an inlet 26 arranged upstream of said outer annular channel.
- a section ratio between the internal diameter d of the internal channel 6 and the internal diameter D of the external annular channel 8 depends: i/ on the mixing ratio between the air and the desired hydrogen, and ii/ on the flow rate Ui dihydrogen in the internal channel. In this document, operation in a dihydrogen-lean regime requires that this D/d ratio be between 3 and 10.
- An outer spinner 28 is housed at an upstream end 30 of the outer annular channel 8.
- This outer spinner 28 is annular.
- This external spin 28 can be radial.
- This annular external spin 28 is arranged at a distance L from the downstream end 36 of the external annular channel 8. This distance L is between 1D and 5D.
- the fuel is then rotated in the center by the internal spinner 14 while the air or the mixture containing at least air is rotated around by the outer spinner 28. This generates a vortex assembly.
- the outer annular channel 8 can have different shapes.
- the outer annular channel 8 comprises a first annular channel 8 and a second annular channel 32.
- the first annular channel 8 corresponds to the outer annular channel 8.
- This first annular channel 8 begins at a downstream end 36 of the outer swirler 28 and opens upstream from the downstream end 30 of the outer swirler 28.
- the second annular channel 32 has an internal diameter greater than the internal diameter of the first annular channel 8. This second annular channel 32 begins at the downstream end 36 of the outer swirler 28 and emerges upstream from the downstream end 16 of the inner channel 6.
- downstream end 24 of the outer annular channel 8 has a section which increases downstream. This downstream end 24 is configured to modify the flow of the outer annular channel 8 near the wall of the end 24.
- downstream end 24 of the outer annular channel 8 has a section which is reduced downstream. This downstream end 24 is configured to modify the flow of the outer annular channel 8 near the wall of the end 24.
- the distance L can be modified.
- the external annular channel 8 comprises a single annular channel, the flow of which from the external channel 8 is rotated by the external swirler 28 axially.
- the rate of rotation S must be high in the internal channel 6. This rate of rotation S is greater than 0.6. Indeed, below 0.6, there is no formation of a recirculation zone with a sufficient depression in the center because the tangential velocity of the hydrogen flow is not sufficient.
- the outer swirl 28 also participates in the maintenance of the recirculation zone.
- Sext the dimensionless number associated with the rate of rotation generated by the external spin 28. Sext is greater than 0.6.
- S ex t is defined analogously to S, that is to say it is a ratio of a tangential velocity to an axial flow velocity of the air flow.
- a stabilization of the flame, unhooked or hooked to the downstream end 16 of the internal channel 6, depends on a stretching of a shear layer upstream of the downstream end of the internal channel on which the flame can 'hang.
- the main parameters controlling a local stretching value are the rate of rotation of the dihydrogen flow characterized by the dimensionless number S, the distance r and a discharge velocity Ui of the dihydrogen in the internal channel.
- a flow velocity Ui of the dihydrogen in the internal channel must be greater than a critical value Ui, c satisfying the following relationship:
- - P is a pressure in the annular combustion chamber
- - S is the rate of rotation generated by the internal spin 14 of the internal channel 6;
- T - T a is an air temperature in Kelvin in the external channel
- the relationship is based on three observations.
- the first observation is that a stretching of the flame causing the extinction of this flame increases as the pressure P and as the temperature T 08 .
- the second observation makes it possible to specify that the stretching of the flame increases when the rate of rotation in the internal channel increases. More precisely, the more the flow is blocked at the downstream end of the internal channel, the more the radial velocities are important, the more the flames are stretched at the level of the lips.
- the third observation specifies that for a given rate of rotation S, the blocking rate will also depend on the spin technology used, hence the power /? in the formula. The value range of /? which is between 1 and 1.5 is a good framework.
- the distance r which depends on the internal diameter D of the external annular channel. If the distance r is too high, the recirculation zone 20 becomes unstable. Under such conditions, the distance r must be between 0.05D and 0.5D.
- the mixture will take place more or less early inside the dihydrogen 2 and air injection device and if this occurs too early, the flame 22 can rise to the interior of the external annular channel 8 between the downstream end 16 of the internal channel and the downstream end 24 of the external annular channel, which is very damaging to the device and to the bottom of the combustion chamber 4.
- the rotation of the flame 22 is therefore configured to prevent the flame 22 from rising in the dihydrogen injection device 2.
- the parameters to be controlled are both the rate of rotation S of the flow in the internal channel, the rate of rotation Sext, and the distance r.
- the spins 14.28 allow to rotate a first flow relative to a second flow.
- the integration of the internal swirl 14 to the internal channel 6 makes it possible to create the recirculation zone 20 of a flow of dihydrogen passing through said internal channel 6 and preventing the flame from coming to stabilize on the downstream end of the internal channel.
- the internal twist 14 of the internal channel 6 rotates the flow of dihydrogen 2 sufficiently to create a recirculation zone penetrating inside the internal channel 6 which blocks part of the flow of dihydrogen along the axis longitudinal x of said internal channel 6 generating significant overspeeds relative to the axial flow rate near the walls of the internal channel 6.
- the rotation of the dihydrogen of the internal channel 6 makes it possible to avoid hanging the flame 22 on the downstream ends of the external annular channel 8 by stabilizing it aerodynamically above the internal channel 6.
- This rotation of the dihydrogen of the internal channel 6 avoids the installation of a complex cooling device for the dihydrogen injection device 2.
- This stabilization of the flame 22 at a distance facilitates the partial mixing of the air with the dihydrogen inside the outer channel 8 above the downstream end 16 of the inner channel, upstream of the flame 22, and avoiding any risk of flashback 22, also called "flash back" in English, in said internal channel 6 and in the annular channel external 8 upstream of the downstream end 16 of the internal channel 6.
- flashback 22 also called "flash back" in English
- the positioning of the downstream end 16 of the internal channel 6 upstream of the downstream end 24 of the external annular channel 8 makes it possible to optimize the mixture between the dihydrogen and the air. This increases the operating range where the flame 22 is detached by moving back the dihydrogen introduction zone with respect to the aerodynamic stabilization zone of the flame.
- the injection device is advantageously implemented within an assembly comprising said injection device, in which the internal channel is fluidically connected to means for supplying dihydrogen and the external annular channel is fluidically connected. to air supply means.
- the dihydrogen supply means are in particular suitable for delivering a gaseous dihydrogen stream without diluent gas, that is to say a stream comprising at least 90% of dihydrogen by mass, and in particular at least 95% of dihydrogen by mass, and advantageously at least 99% dihydrogen by mass.
- the dihydrogen supply means comprise for example at least one pressurized tank equipped with at least one valve, and/or at least one chemical generation device for gaseous dihydrogen.
- the air supply means are in particular suitable for delivering a flow of air without adding diluent gas.
- the air supply means comprise for example an atmospheric air inlet upstream of the turbine engine. This air is compressed before entering the annular combustion chamber.
- the air supply means may also include a source of oxygen for airflow enrichment in oxygen.
- the oxygen source can comprise a pressurized oxygen tank provided with a valve and/or means for the chemical generation of gaseous oxygen.
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Abstract
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Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CA3233988A CA3233988A1 (en) | 2021-10-08 | 2022-10-05 | Device for injecting dihydrogen and air |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR2110692A FR3127987A1 (en) | 2021-10-08 | 2021-10-08 | Dihydrogen and air injection device |
FRFR2110692 | 2021-10-08 | ||
FR2111267A FR3127988A1 (en) | 2021-10-08 | 2021-10-22 | Dihydrogen and air injection device |
FRFR2111267 | 2021-10-22 |
Publications (1)
Publication Number | Publication Date |
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WO2023057722A1 true WO2023057722A1 (en) | 2023-04-13 |
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PCT/FR2022/051883 WO2023057722A1 (en) | 2021-10-08 | 2022-10-05 | Device for injecting dihydrogen and air |
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CA (1) | CA3233988A1 (en) |
WO (1) | WO2023057722A1 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080163627A1 (en) * | 2007-01-10 | 2008-07-10 | Ahmed Mostafa Elkady | Fuel-flexible triple-counter-rotating swirler and method of use |
EP3336431A1 (en) * | 2016-12-16 | 2018-06-20 | Ansaldo Energia S.p.A. | Burner assembly for a gas turbine plant, gas turbine plant comprising said burner assembly and method for operating said plant |
US20190078777A1 (en) * | 2016-03-15 | 2019-03-14 | Jay Keller | Non-premixed swirl burner tip and combustion strategy |
-
2022
- 2022-10-05 CA CA3233988A patent/CA3233988A1/en active Pending
- 2022-10-05 WO PCT/FR2022/051883 patent/WO2023057722A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080163627A1 (en) * | 2007-01-10 | 2008-07-10 | Ahmed Mostafa Elkady | Fuel-flexible triple-counter-rotating swirler and method of use |
US20190078777A1 (en) * | 2016-03-15 | 2019-03-14 | Jay Keller | Non-premixed swirl burner tip and combustion strategy |
EP3336431A1 (en) * | 2016-12-16 | 2018-06-20 | Ansaldo Energia S.p.A. | Burner assembly for a gas turbine plant, gas turbine plant comprising said burner assembly and method for operating said plant |
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