Method for operating a combustion device including injecting a fluid together with diluent fuel to address combustion pulsations

Abstract

A method for operating a combustion device includes supplying a fuel and an oxidizer into the combustion device and burning them. According to the method, during at least a part of a transient operation, an additional fluid is supplied together with the fuel, and its amount is regulated to counteract combustion pulsations.

Claims

1. Method for operating a combustion device comprising: supplying a fuel and an oxidizer into the combustion device and burning them; supplying, during at least a part of a transient operation, an additional fluid together with the fuel, the transient operation including one of a start-up of the combustion device, a switch-off of the combustion device or a fuel switch-over of the combustion device; and regulating the amount of the additional fluid to counteract combustion pulsations, wherein the additional fluid is an inert fluid, and the additional fluid is at least partly mixed with the fuel prior to injection.

2. The method according to claim 1, comprising choosing a first parameter indicative of a fuel feed and supplying the additional fluid only when the fuel feed reaches a predetermined value of the first parameter.

3. The method according to claim 2, wherein the first parameter is the fuel mass flow (M).

4. The method according to claim 3, comprising: supplying the additional fluid only when the fuel mass flow is below a critical value at which pulsations start to generate.

5. The method according to claim 2, wherein the first parameter is a differential pressure (ΔP) between a fuel supply and the inside of the combustion device.

6. The method according to claim 2, comprising choosing a second parameter indicative of the fuel and additional fluid feed, the regulating including maintaining the second parameter above or below a second predetermined value or maintaining the second parameter within a prefixed range (R).

7. The method according to claim 6, wherein the second parameter range (R) corresponds to the second predetermined value of the second parameter ±10% or to the second predetermined value of the second parameter ±1% or to the second predetermined value of the second parameter.

8. The method according to claim 6, wherein a bottom or a top of the range (R) correspond to the second predetermined value (SPc) of the second parameter (SP).

9. The method according to claim 6, wherein the second parameter is the fuel and additional fluid mass flow (M).

10. The method according to claim 6, wherein the second parameter is the differential pressure (ΔP) between a fuel and additional fluid supply and the inside of the combustion device.

11. The method according to claim 2, wherein the predetermined value is a value at which pulsations start to generate.

12. The method according to claim 1, wherein the fuel is supplied into the combustion device via a fuel supply, wherein the additional fluid is supplied into this fuel supply.

13. The method according to claim 1, wherein the fuel is a liquid fuel and the additional fluid is also liquid.

14. The method according to claim 1, wherein the fuel is a gaseous fuel and the additional fluid is also gaseous.

15. The method according to claim 1, comprising: supplying the additional fluid together with the fuel to create a combined flow of fluid and fuel, and the combined flow is then mixed with an oxidiser during at least a part of the transient operation.

16. The method according to claim 1, comprising: counteracting the combustion pulsations by minimising the formation of combustion pulsations.

17. Method for operating a combustion device comprising: supplying a fuel and an oxidizer into the combustion device and burning them; supplying, during at least a part of a transient operation, an additional fluid together with the fuel; regulating the amount of the additional fluid to counteract combustion pulsations; and choosing a first parameter indicative of a fuel feed and supplying the additional fluid only when the fuel feed reaches a predetermined value of the first parameter, wherein the first parameter is a differential pressure (ΔP) between a fuel supply and the inside of the combustion device.

18. Method for operating a combustion device comprising: supplying a fuel and an oxidizer into the combustion device and burning them; supplying, during at least a part of a transient operation, an additional fluid together with the fuel; regulating the amount of the additional fluid to counteract combustion pulsations; choosing a first parameter indicative of a fuel feed and supplying the additional fluid only when the fuel feed reaches a predetermined value of the first parameter; choosing a second parameter indicative of the fuel and additional fluid feed, the regulating including maintaining the second parameter above or below a second predetermined value or maintaining the second parameter within a prefixed range (R); and wherein the second parameter prefixed range (R) corresponds to the second predetermined value of the second parameter ±10% or to the second predetermined value of the second parameter ±1% or to the second predetermined value of the second parameter.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) Further characteristics and advantages of the invention will be more apparent from the description of a preferred but non-exclusive embodiment of the method, illustrated by way of non-limiting example with reference to the accompanying drawings, in which:

(2) FIGS. 1 and 2 schematically show the pressure waves P within the combustion device as a function of the circumferential angle φ or axial position x at two different periods in time t0 and t1;

(3) FIG. 3 schematically shows the mass flow injected into the combustion device as a function of the time t;

(4) FIGS. 4 through 9 show different combustion devices that can implement the method; and

(5) FIGS. 10 through 17 show different embodiments of the method.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(6) The method can be implemented with any kind of combustion device, for example adapted to generate a premixed flame, a diffusion flame, a mixed flame, etc.

(7) For example the combustion device can be a premixed combustion device 5 (FIG. 4), with conical swirl chamber 6 and combustion chamber 7 extending downstream of the swirl chamber 6; a front plate 8 is provided between them. This combustion device further includes fuel supply (for example a lance 9 that typically injects a liquid fuel) and tangential slits 10 at the swirl chamber 6 for oxidizer supply (typically air). Additional fuel supply includes injectors 11 (FIG. 5) provided on lines 12 that are connected to the wall of the swirl chamber 6, at positions close to the slits 10, for fuel injection (typically gaseous fuel). This kind of combustion device 5 is well known and is schematically shown in FIGS. 4, 5 and 9.

(8) A different kind of premixed combustion devices 15 is for example schematically shown in FIG. 6. This combustion device 15 includes a body 16 (for example a tubular body with square or trapezoidal cross section) with an inlet 17 and outlet. Within the body 16, vortex generators 19 (for example tetrahedral vortex generators but also different shapes and concepts are possible) and fuel supply including a lance 20 with fuel injectors 21 are housed. Downstream of the body 16, a combustion chamber 22 is provided.

(9) FIGS. 7 and 8 show further examples of combustion devices that are arranged to generate a diffusion flame.

(10) These combustion devices 25 have a body 26 with fuel supply including fuel injectors 27 (liquid or gaseous fuel) and oxidizer supply including oxidizer injectors 28.

(11) In all the figures, reference 30 indicates the flame and reference G indicates the hot gases generated in the combustion device and directed toward the turbine.

(12) In the following, particular reference to the embodiment of FIG. 3 is made; it is anyhow clear that the same method can be implemented in all kind of combustion devices (i.e. those described or others).

(13) The method for operating a combustion device 5 comprises supplying a fuel 35 and an oxidizer 36 into the combustion device 5 and burning them.

(14) In addition, during at least a part of a transient operation such as for example a start up, a switch off or a switch over, an additional fluid 37 is supplied into the combustion device 5 together with the fuel 35.

(15) The additional fluid 37 is advantageously supplied through the same injectors as the fuel 35 and it is typically at least partly mixed with the fuel 35.

(16) The amount of the additional fluid 37 is thus regulated to counteract combustion pulsations.

(17) With reference to FIG. 14, a first parameter FP indicative of the fuel feed is chosen and the additional fluid supply starts only when the first parameter reaches a critical value FPc. The critical value FPc can be chosen such that when the first parameter reaches or passes it, pulsations start to generate or to substantially generate. In this respect FIG. 14 shows the first parameter FP and its critical value FPc; supply of the additional fuel starts only at t5, when the first parameter reaches its critical value FPc.

(18) In different examples, the first parameter can be the fuel mass flow M or the differential pressure ΔP between a fuel supply and the inside of the combustion device 5; in these cases additional fluid supply starts when the fuel amount supplied into the combustion device or the differential pressure falls below the critical value Mc or ΔPc.

(19) In addition, a second parameter SP indicative of the fuel and additional fluid feed is also chosen; the regulation includes maintaining the second parameter above or below a given value (FIG. 15) or preferably maintaining the second parameter SP within a prefixed range R (FIG. 16).

(20) The given value can be a critical value SPc of the second parameter SP. Also in this case, the critical value can be chosen such that when the second parameter reaches or passes it, pulsations start to generate or to substantially generate.

(21) In different examples the second parameter range R corresponds to the critical value SPc of the second parameter ±10% or preferably to the critical value SPc of the second parameter ±1% or more preferably to the critical value SPc of the second parameter.

(22) Preferably, the bottom or the top of the range corresponds to the critical value SPc of the second parameter.

(23) The second parameter SP can be the fuel and additional fluid mass flow M or the differential pressure ΔP between a fuel and additional fluid supply and the inside of the combustion device 5. In these cases the regulation includes maintaining the total mass flow of fuel 35 and additional fluid 37 or differential pressure AP above the critical value or maintaining them within the prefixed range R.

(24) FIG. 17 shows an example in which the first and the second parameter are the same physical entity (for example mass flow M or differential pressure AP as indicated above). In this case the first parameter and the second parameter can be measured through the same sensors. In particular FIG. 17 shows that before t=t6 (i.e. when the fuel mass flow M or differential pressure ΔP between the fuel supply and the inside of the combustion device) are above the critical value Mc or ΔPc the sensors measure the first parameter and only fuel is injected and when the first parameter (i.e. M or ΔP) reaches the critical value Mc or ΔPc also the additional fluid 37 starts to be fed and the sensors measure the second parameter SP; in this example the second parameter is kept at the critical value Mc or ΔPc but as already described it can be kept above or below it or within a range R.

(25) To measure the differential pressure ΔP the control device shown in FIG. 9 can be used.

(26) FIG. 9 shows a control device 45 connected to sensors 46 for measuring the pressure in a line supplying the fuel (or fuel and additional fluid) to the combustion device 5 and sensors 47 for measuring the pressure within the combustion device; the control device 45 elaborates the signals from the sensors 46, 47 and provides a control signal (to a valve 48 or different component) to regulate the amount of the additional fluid 37.

(27) The fuel 35 is supplied into the combustion device 5 via a fuel supply (for example the lance 9 or the lines 11 but, in the other examples of combustion devices 15, 25, also lance 20); the additional fluid 37 is preferably also supplied into the same fuel supply (i.e. into the lance 9 or the lines 11 or lance 20).

(28) Advantageously, the additional fluid 37 is at least partly mixed with the fuel 35 and in this respect a mixer 49 can be provided.

(29) The additional fluid 37 is preferably an inert fluid; inert fluid is a fluid that does not react during burning, i.e. it is neither a fuel nor an oxidizer.

(30) In addition, when the fuel is a liquid fuel, the inert fluid is preferably a liquid fluid (for example the fuel can be oil and the additional fluid water) and when the fuel is a gaseous fuel the additional fluid is preferably a gaseous fluid (for example the fuel can be natural gas or methane and the additional fluid nitrogen).

(31) Advantageously, since when the amount of fuel becomes low the additional flow is injected with it, no fluctuating amounts of fuel are injected into the combustion device; this prevents or hinders thermal and mechanical pulsations.

(32) In the following some embodiments of the invention are described in detail.

EXAMPLE 1

Switch Over From a Fuel Being Premix Gas to Premix Oil

(33) In FIG. 10 curve 50 shows the reducing amount of premix gas injected into the combustion device and curve 51 indicates the increasing amount of premix oil. In addition, curve 52 indicates the water that is supplied together with the premix oil 51 and curve 53 indicates the differential pressure as defined in the present disclosure. The amount of water is at its maximum at the beginning of its supply and then decreases. When the first parameter for the premix oil exceeds the critical amount (for example mass flow Mc or differential pressure ΔPc), the supply of water is stopped (curve 52 goes to zero). In this example, the additional fluid is only fed together with the premix oil (but not with the premix gas).

EXAMPLE 2

Switch Over From a Fuel Being Premix Gas to Premix Oil

(34) This example is similar to the first example. In particular, in this second example two speeds for the fuel regulation are provided: a slow speed during water supply and a faster speed when no water supply is provided.

EXAMPLE 3

Switch Over From a fuel Being Premix Gas to Premix Oil

(35) Also this example is similar to the first example and, in particular, water 52 and nitrogen 54 are supplied when a first parameter of both the gas premix and the oil premix 50, 51 are below their critical value.

EXAMPLE 4

Switch Over From a Fuel Being Premix Gas to Premix Oil

(36) Also this example is similar to the first example and, in particular, supply of water starts before premix oil supply.

(37) Naturally, the features described may be independently provided from one another.

(38) In practice the materials used and the dimensions can be chosen at will according to requirements and to the state of the art.

REFERENCE NUMBERS

(39) 1 fuel mass flow at steady operation 2 theoretical fuel mass flow during transient operation 3 real fuel mass flow during transient operation 5 combustion device 6 swirl chamber 7 combustion chamber 8 front plate 9 lance 10 tangential slits 11 injectors 12 line 15 combustion device 16 body 17 inlet 19 vortex generators 20 lance 21 injectors 22 combustion chambers 25 combustion device 26 body 27 injectors 28 oxidizer injectors 30 flame 35 fuel 36 oxidizer 37 additional fluid 45 control device 46 sensor 47 sensor 48 valve 49 mixer 50 premix gas 51 premix oil 52 water 53 differential pressure 54 nitrogen t, t0, t1, t3, t4, t5, t6 time x axial position φ, φ1 angular position ΔP differential pressure ΔPc critical value of ΔP FP first parameter FPc critical value of FP G hot gases L combustion device length M mass flow Mc critical value of M P, P1, P2 pressure R range SP second parameter SPc critical value of SP