MIXER
A mixer having a housing, a duct within the housing, a first and a second injector arranged to inject a fluid at a centre zone of the duct, a third and a fourth injector arranged to inject the fluid at a wall zone of the duct. The first/third injectors are at a distance D1=v/2f1 or odd integer multiples of it from the second/fourth injectors in the absence of an acoustic node between them, or at a distance D1=λconv=v/f1 or full wave length integer multiples of it in the presence of an acoustic node between them. Advantageously f1 is greater than f2.
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This application claims priority from European Patent Application No. 17159008.6 filed on Mar. 2, 2017, the disclosure of which is incorporated by reference.
TECHNICAL FIELDThe present invention relates to a mixer. In particular the mixer is part of a gas turbine and is used to supply dilution air into the hot gas passing through the gas turbine.
BACKGROUNDBetween the first combustion chamber 3 and the second combustion chamber 4 a mixer 7 can be provided in order to dilute with air (or other gas) the hot gas coming from the first combustion chamber 3 and directed into the second combustion chamber 4.
The temperature in the second burner 4a can oscillate, typically because of mass flow oscillations of the air coming from the mixer 7 and directed into the second burner 4a.
The delay time depends on, inter alia, the temperature within the second burner 4a, such that temperature oscillations in the second burner 4a cause increase/decrease of the delay time and thus axial upwards/downwards oscillations of the flame in the combustor 4b.
In order to prevent these axial oscillations of the flame, the temperature in the second burner 4a has to be maintained constant and thus the flow emerging from the mixer 7 has to be maintained constant.
The mass flow through the mixer 7 can vary because within the mixer 7 pressure oscillations exist (e.g. due to the combustion in the combustor 3b and/or 4b); these pressure oscillations cause an increase/decrease of the flow of diluting air injected into the mixer.
In order to maintain this flow constant, multiple injectors can be provided at different axial locations of the mixer 7, in such a way that oscillating pressure air supplied through upstream injectors compensate for oscillating pressure air supplied trough downstream injectors. In other words, air is injected in such a way that high pressure air injected from upstream injectors reaches the downstream injectors when low pressure air is injected through them (and vice versa); this way the high pressure and low pressure compensate for one another and are cancelled, such that the pressure within the mixer 7 stays substantially constant; air injection into the mixer can thus be constant over time.
The inventors have found a way to improve cancellation of pressure oscillations (and thus mass flow oscillations) through the cross section of the mixer.
SUMMARYAn aspect of the invention includes providing a mixer with improved flow oscillation cancellation.
These and further aspects are attained by providing a mixer in accordance with the accompanying claims.
Further characteristics and advantages will be more apparent from the description of a preferred but non-exclusive embodiment of the mixer, illustrated by way of non-limiting example in the accompanying drawings, in which:
With reference to the figures, these show the gas turbine 1 with the compressor 2, the first combustion chamber 3, the second combustion chamber 4 fed with a fluid coming from the first combustion chamber 3, the turbine 5. Between the first combustion chamber 3 and the second combustion chamber 4 it is provided the mixer 7. In addition, between the first combustion chamber 3 and the second combustion chamber 4 (upstream or downstream of the mixer 7), a high pressure turbine can be provided (
The mixer 7 comprises a housing 10, a duct 11 within the housing 10, a first injector 12 arranged to inject a fluid at the centre zone of the duct 11, a second injector 13 arranged to inject a fluid at the centre zone of the duct 11, a third injector 14 arranged to inject a fluid at the wall zone of the duct 11 and a fourth injector 15 arranged for injecting a fluid at the wall zone of the duct 11. Additional injectors can also be provided.
Each injector can comprise a row of nozzles 16 extending over the circumference or perimeter of the duct 11; in addition each injector can comprise a plurality of rows of nozzles close to one another. Additionally, nozzles 16 of different rows of nozzles of a same injector can have same or different penetration and/or nozzles 16 of a same row of nozzles can have different penetration.
For example,
In order to inject the fluid at the centre zone 18 of the duct 11 the first and second nozzles 12, 13 have a deep penetration into the duct 11; likewise in order to inject the fluid at the wall zone 17 of the duct 11 the third and fourth nozzles have a small penetration into the duct 11; generally the first and second injectors 12, 13 have a deeper penetration into the duct 11 than the third and fourth injectors 14, 15.
The relative position of the injectors can be any, i.e. any injector can be upstream and/or downstream of any other injector (upstream and downstream are referred to the fluid circulation direction identified by the arrow F in the figures).
The distance between the first injector 12 and the second injector 13 is, in case there is no acoustic node between them (i.e. in the absence of an acoustic node)
D1=λconv/2=v/2f1
or an odd integer multiple of it. In case there is an acoustic node between the first and second injectors 12, 13 (i.e. in the presence of an acoustic node) the distance D1 is
D1=λconv=v/f1
or a full wave length integer multiple of it.
Likewise, the distance between the third injector 14 and the fourth injector 15 is, in case there is no acoustic node between them (i.e. in the absence of an acoustic node)
D2=λconv/2=v/2f2
or an odd integer multiple of it. In case there is an acoustic node between the third injector 14 and the fourth injector 15 (i.e. in the presence of an acoustic node) the distance D2 is
D2=λconv=v/f2
or a full wave length integer multiple of it.
In the above formulas:
f1 is the oscillating frequency (pressure oscillation) to be damped at the wall zone 17 of the duct 11, i.e. at zones within the duct 11 that are close to the wall, e.g. at the outer part of the flame,
f2 is the oscillating frequency (pressure oscillations) to be damped at a centre zone 18 of the duct 11, e.g. at the inner or centre part of the flame,
λconv is the convective wave length, i.e. the flow velocity v through the duct divided by the frequency that should be addressed with the concept,
v is the fluid flow speed through the duct 11.
Acoustic node defines the change of sign of the pressure with reference to the nominal pressure.
In addition, the distances D1 and D2 are measured between the axes of the nozzles 16 of the injectors 12, 13, 14, 15 or, in case an injector comprises more rows of nozzles 16 (all injecting into the same zone being the centre or the wall zone), with reference to an average position between the two or more axes of the nozzles 16 of this injector (see e.g.
As an example,
Advantageously, f1 is greater than f2. Both f1 and f2 are low frequencies e.g. below 150 Hz.
The operation of the mixer and gas turbine having such a mixer is apparent from that described and illustrated and is substantially the following.
Air is compressed at the compressor 2 and is supplied into the burner 3a where fuel is supplied and mixed with the compressed air, generating a mixture that combusts in the combustor 3b with a flame 20a; the hot gas generated through this combustion passes through the transition piece 3c and enters the mixer 4 (in particular the duct 11 of the mixer 4).
At the mixer 4 air is injected into the hot gas via the first, second, third, fourth injectors 12, 13, 14, 15 and via possible additional injectors.
This configuration allows a selective cancellation of the mass flow oscillations, because different zones of the cross section of the duct 11 are responsible for generating pulsations of different frequency. In particular, as indicated above, the zones closer to the duct wall have a higher frequency while the zones farther from the duct walls (i.e. at the centre of the duct) have a lower frequency.
Naturally the features described may be independently provided from one another. For example, the features of each of the attached claims can be applied independently of the features of the other claims.
In practice the materials used and the dimensions as well as the injector shapes can be chosen at will according to requirements and to the state of the art.
REFERENCE NUMBERS
- 1 gas turbine
- 2 compressor
- 3 first combustion chamber
- 3a first burner
- 3b combustor
- 3c transition piece
- 4 second combustion chamber
- 4a second burner
- 4b combustor
- 5 turbine
- 7 mixer
- 8 lance
- 9 turbine
- 10 housing
- 11 duct
- 12 first injector
- 13 second injector
- 14 third injector
- 15 fourth injector
- 16 nozzles
- 17 wall zone
- 18 centre zone
- 20a, 20b flame
- 22 acoustic node
- D1 distance
- D2 distance
- F flow
- λconv convective wave length
- v fluid flow speed through the duct
Claims
1. A mixer comprising:
- a housing;
- a duct within the housing;
- a first injector and a second injector arranged to inject a fluid at a centre zone of the duct;
- a third injector and a fourth injector arranged to inject the fluid at a wall zone of the duct, wherein:
- the first injector is at a distance D1=v/2f1 or odd integer multiples of it from the second injector in an absence of an acoustic node between the second injector and the first injector, or at a distance D1=λconv=v/f1 or full wave length integer multiples of it in a presence of an acoustic node between the second injector and the first injector; and
- the third injector is at a distance D2=v/2f2 or odd integer multiples of it from the fourth injector in an absence of an acoustic node between the third injector and the first injector, or at a distance D2=v/f2 from the first injector in a presence of an acoustic node between the third injector and the first injector;
- wherein:
- f1 is an oscillating frequency to be damped at the wall zone of the duct;
- f2 is an oscillating frequency to be damped at the centre zone of the duct; and
- v is a fluid flow speed through the duct, wherein f1 is greater than f2.
2. The mixer of claim 1, wherein both f1 and f2 are lower than 150 Hz.
3. The mixer of claim 1, wherein the first injector and/or the second injector and/or the third injector and/or the fourth injector comprise:
- a plurality of rows of nozzles close to one another.
4. The mixer of claim 2, wherein nozzles of different rows of nozzles of a same injector have different penetration.
5. The mixer of claim 2, wherein the nozzles of a same row of nozzles have different penetration.
6. A gas turbine comprising:
- a compressor;
- a first combustion chamber;
- a second combustion chamber arranged to be fed with a fluid coming from the first combustion chamber; and
- a turbine, wherein between the first combustion chamber and the second combustion chamber a mixer is provided, which mixer includes:
- a housing;
- a duct within the housing;
- a first injector and a second injector arranged to inject a fluid at a centre zone of the duct;
- a third injector and a fourth injector arranged to inject the fluid at a wall zone of the duct, wherein:
- the first injector is at a distance D1=v/2f1 or odd integer multiples of it from the second injector in an absence of an acoustic node between the second injector and the first injector, or at a distance D1=λconv=v/f1 or full wave length integer multiples of it in a presence of an acoustic node between the second injector and the first injector; and
- the third injector is at a distance D2=v/2f2 or odd integer multiples of it from the fourth injector in an absence of an acoustic node between the third injector and the first injector, or at a distance D2=v/f2 from the first injector in a presence of an acoustic node between the third injector and the first injector;
- wherein:
- f1 is an oscillating frequency to be damped at the wall zone of the duct;
- f2 is an oscillating frequency to be damped at the centre zone of the duct; and
- v is a fluid flow speed through the duct, wherein f1 is greater than f2.
Type: Application
Filed: Feb 28, 2018
Publication Date: Sep 6, 2018
Applicant: ANSALDO ENERGIA SWITZERLAND AG (Baden)
Inventors: Mirko Ruben BOTHIEN (Zurich), Alessandro SCARPATO (Wettingen)
Application Number: 15/907,953