Field of the Invention
[0001] The present invention relates to the technical filed of the gas turbine assemblies
for power plants. In particular, the present invention relates to a method for operating
a sequential combustor of a gas turbine. This sequential combustor comprises an first
combustor (or upstream combustor) configured for receiving the compressed air and
mixing this air with fuel and a downstream second combustor (or reheat combustor)
configured for receiving the hot gas leaving the first combustor and adding fuel into
this hot gas for performing a self/spontaneous ignition. More in detail the present
invention refers also to a method for refurbishment the above first combustor in order
to allow a current first combustor to be fed by a highly reactive fuel, for instance
H2-based fuel.
Description of prior art
[0002] As known, a gas turbine assembly for power plants (in the following only gas turbine)
comprises a rotor provided with a compressor unit, a combustor unit and at least a
turbine unit. The compressor is configured for compressing air supplied at a compressor
inlet. The compressed air leaving the compressor flows into a plenum and from there
into a combustor. The combustor comprises a plurality of burners configured for injecting
fuel in the compressed air. The mixture of fuel and compressed air flows into a combustion
chamber where this mixture is combusted. The resulting hot gas leaves the combustion
chamber and is expanded in the turbine performing work on the rotor. As known, the
turbine comprises a plurality of stages, or rows, of rotor blades that are interposed
by a plurality of stages, or rows, of stator vanes. The rotor blades are connected
to the rotor whereas the stator vanes are connected to a vane carrier that is a concentric
casing surrounding the turbine unit.
[0003] In order to achieve a high efficiency, a high turbine inlet temperature is required.
However, in general this high temperature involves an undesired high NOx emission
level. In order to reduce this emission and to increase operational flexibility without
decreasing the efficiency, the so called "sequential" gas turbines is particularly
suitable. In general, a sequential gas turbine comprises two combustors or combustion
stages in series wherein each combustor is provided with a plurality of burners and
with at least a relative combustion chamber. Following the main gas flow direction,
usually the upstream or first combustor comprises a plurality of so-called "premix"
burners. The term "premix" emphasizes the fact that each burner of the first combustor
is configured not only for injecting the fuel directly in the compressed air forming
a diffusion flame (for instance by a so called "pilot lance") but also for mixing
(with a swirl) the compressed air and the fuel before injecting the mixture into the
combustion chamber. Therefore in the following with the terms "premix burner" we mean
the burner in the first stage of the sequential combustor wherein each premix burner
is configured for receiving the compressed air and injecting fuel in this coming air
for realizing a diffusion flame (e.g. by pilot lance without any premix) and/or a
premix flame. This kind of premix burner is today widely used because a diffusion
flame is useful under some condition (for instance during the cold starting operation)
whereas a premix flame allows to reduce the NOx emissions during the normal operation.
The downstream or second combustor is called "reheat" or "sequential" combustor and
it is fed by the hot gas leaving the first combustor. Also, the reheat combustor is
provided with a plurality of reheat burners configured for injecting fuel in the hot
gas coming from the first combustor. Due to the high gas temperature, the operating
conditions downstream the reheat burners allow a self/spontaneous ignition of the
fuel/air mixture. Also these reheat burners are configured for performing a premix
for the hot gas and the fuel before the spontaneous ignition. Therefore in the following
with terms reheat burners we mean only the burners at the second stage of combustion
in the sequential combustor.
[0004] Today two different kinds of sequential gas turbines are known. According to the
first embodiment the premix and reheat combustors are annular shaped and are physically
separated by a stage of turbine blades, called high pressure turbine. According to
a second embodiment, the gas turbine is not provided with the high pressure turbine
and the combustor unit is realized in form of a plurality of can-combustors. In this
embodiment each can-combustor comprises a premix (first stage) and the reheat (second
stage) combustor arranged directly one downstream the other inside the common can
shaped casing. In both embodiments the burners are configured for injecting different
kinds of fuel, i.e. liquid (in the following with the terms "oil fuel" it is meant
"liquid fuel" in general) and gas fuel, and carrying air, i.e. a little part of the
compressed air leaving the compressor. In view of the above, the burners are provided
with separated channels or ducts for feeding the gas fuel, liquid fuel and carrying
air to relevant burner nozzles.
[0005] Starting from the above mentioned structures of sequential gas turbines, today is
present the need of improving the fuel flexibility while keeping low emission and
high performance. In particular, a real challenge today is to use a highly reactive
fuel, e.g. with high amounts of H2 or higher hydrocarbons (e.g. ethane, propane).
Indeed, the increasing use of renewables for energy production is also accompanied
by an increasing need for flexible power production, while aiming at carbon free emissions.
The potential solutions of energy storage of excess generation from renewables through
hydrogen production and precombustion carbon capture are gaining momentum. Both scenarios
require gas turbines capable of operation with hydrogen-based fuels. At the same time,
the composition of natural gas considered for use within gas turbines is becoming
significantly more variable due to increased use of liquefied natural gas and a wider
range of gas sources and extraction methods. Fuel flexibility, both in terms of the
amount of hydrogen and higher hydrocarbons is therefore of utmost importance in modern
gas turbine development.
[0006] A change in fuel reactivity implies a change in flame location. In particular, higher
fuel reactivity (like H2) forces the flame to move upstream, increasing NOx emissions,
and potentially overheating the burners. Consequently, when burning highly reactive
fuels (e.g. fuels containing large quantities of either higher hydrocarbons or hydrogen)
the flame moves upstream compared to the case of natural gas, thus increasing the
risk of flashback. Since the position of the flame in the reheat combustor can be
effectively controlled by the temperature at the inlet of the reheat combustor (self/spontaneous
ignition), by lowering the inlet temperature it is therefore possible to move the
flame downstream. Therefore, the negative effect of higher fuel reactivity (flashback)
in the reheat combustor can be compensated by lowering the first stage temperature.
Moreover, also the premix combustor may be affected by flashback in this condition.
According to the prior art practice, in order to mitigate the flashback risks by moving
the flame back to its design position in the premix and in the reheat combustor is
obtained by simply injecting less fuel in the first stage of combustion. In this way
the position of the flame in the premix combustor is moved downstream and the inlet
temperature of the second stage is lower.
[0007] According to the current prior art practice, only minor amounts of hydrogen are allowable
in premix, non-reheat combustion system, therefore diffusion type combustors are used
to generate electricity with particularly high amounts of hydrogen as fuel. However,
this prior art practice generates high NOx emissions and therefore a large amounts
of diluents (nitrogen, steam) need to be added in the gas flow and/or selective catalytic
reduction devices have to be used to keep the NOx emissions below the limits. As known
these remedies significantly reduce the efficiency of the gas turbine plant.
[0008] Summarizing, in case of highly reactive fuels e.g. hydrogen based fuels, the prior
art practice gives the following suggestions:
- in case of generic premix systems it is not possible to use highly reactive fuels
because of emission and flashback limits on the premix burners, requiring for major
derating with detrimental effects on engine performance
- in sequential combustors, highly reactive fuels can be well used in the reheat combustor
inlet temperature but beyond a certain limit the first combustor operation is limited
by LBO;
- only in case of diffusion combustors (not premixed) it is possible to use a fuel having
a high rate of H2 (i.e. up to 100%) . However, by using this kind of combustor it
is not possible to reach the efficiency rate of a premix/reheat sequential combustor.
Moreover, this solution is not considered today an acceptable solution in view of
the detrimental impact on NOx generation and because of the limitation of fuel gas
pressure requirements.
Disclosure of the invention
[0009] Accordingly, a primary object of the present invention is to provide a sequential
combustor for a gas turbine in order to overcome the drawbacks foregoing mentioned
of the current prior art practice. In particular, the scope of the present invention
is to provide a method for refurbishment a current sequential combustor for a gas
turbine in order to allow the sequential combustor to be supplied with a highly reactive
fuel, for instance H2-based fuel having a % of H2 in vol. from 0% to 100%.
[0010] The starting point of the present invention is an innovative method developed by
the Applicant for operating a sequential combustor for a gas turbine when the combustor
is fed by a highly reactive fuel. The sequential combustor configured for carrying
out this operating method comprises:
- a first combustor provided with a plurality of first burners fed by compressed air
and configured for injecting fuel in the compressed air;
- a second combustor provided with a plurality of second burners fed by the hot gas
leaving the first combustor and configured for injecting fuel in the hot gas.
[0011] Referring to the first combustor, as known the supplied compressed air is the air
leaving a compressor upstream arranged in the gas turbine with respect to the sequential
combustor. The combustor operating method does not provide any limitation referring
to the shape of the first combustor and in the following description of the drawings
two different embodiments of the claimed first combustor will be described. Each burner
of this first combustor may be a particular kind of burner, namely a so-called "premix"
burner. It is clear for a skill person in the field of the gas turbines that the definition
"premix" burner means a burner configured for mixing the coming air and the injected
fuel before the inlet of the combustion chamber. For instance, in order to generate
this mixing the premix burner may comprise an outer conical casing configured for
generating a swirl in the air flow wherein this conical casing is also provided with
fuel injecting nozzles. In this way the air flow leaving the burner and entering the
combustion chamber is already mixed with the injected fuel. Moreover, as known, a
"premix" burner may comprises also a pilot configured for injecting fuel directly
in the air flow in the combustion chamber without any preliminary mixing feature.
For instance, this pilot may be realized in form of a lance axially extending along
the outer conical casing. Therefore, a premix burner is a burner configured for generating
to different kinds of flame in the combustion chamber, a so-called diffusion flame,
for instance generated by the fuel injected by the pilot, and a premix flame, for
instance generated by the swirled mixture air/fuel. As known a premix burner may be
operated to generate only a diffusion flame, only a premix flame or a combination
of a diffusion and a premix flame with different rate of fuel supplied in the premix
circuit and in the diffusion circuit. During normal operation the premix flame is
preferable due to a less NOx generation.
[0012] The combustor operating method developed by the Applicant does not provide any limitation
also referring to the shape of the second combustor. Each second burner is a burner
configured for injecting fuel in the hot gas flow leaving the first combustor. Due
to the high temperature of the hot gas leaving the first combustor, the second burner
is not provided with a spark igniter or any forced igniter device and the combustion
is based on a self/spontaneous ignition. This second burner is also called "reheat"
burner and the present invention does not require any structural modification of current
reheat burners.
[0013] As mentioned in the chapter referring to the prior art, today there is the need to
provide a new operation mode for a sequential combustor when the supplied fuel is
a highly reactive fuel. With the terms "highly reactive fuel" we mean a fuel having
higher reactivity compared with natural gas. An example of high reactive fuel is a
hydrogen-based fuel. When the sequential combustor is fed by a high reactive fuel
the method for operating this sequential combustor developed by the Applicant comprises
the following steps:
- switching off at least one of the first burners;
- operating the remaining active first burners for generating hybrid flames as combination
of diffusion mode and premix mode combustion. In other words, the above operating
method requires a high diffusion fuel rate wherein some burners may be operated only
in diffusion configuration.
[0014] Starting from the above, the present invention solves the problem to how safely perform
the above operating step of feeding the burner with a high diffusion fuel rate. Indeed,
a high diffusion fuel rate during the normal operation would require a high fuel pressure
drop (more than 10 bar) and this high fuel pressure drop requires in turn a very high
pressure inside the gas fuel line feeding the diffusion nozzles. This high pressure
may damage the combustion system. Furthermore the engine would require fuel gas pressure
levels not always available in the fuel gas lines.
[0015] The solution proposed by the present invention is to use in parallel another fuel
supply line already present in the burner for feeding to the diffusion nozzles at
least part of the fuel running in the gas fuel line. In particular, according to the
invention the fuel supply line used for feeding to the diffusion nozzles at least
part of the fuel running in the gas fuel line is the oil fuel line. In other words,
the solution proposed by the present invention is feeding part of the high reactive
gas fuel running in the gas fuel line into the oil (liquid) fuel line; oil fuel line
that are usually used only for oil fuel feeding. In order to allow this parallel feeding
of the high reactive gas fuel not only inside the gas line but also inside the oil
line a connection is provided between the pilot gas fuel line and the oil fuel line.
This connection is provided with a valve configured for selectively allowing the flow
of part of the high hydrogen gas fuel running in the gas line into the oil line.
[0016] Advantageously, this solution allows to reduce the pressure present in the gas fuel
line without any detrimental impact on combustion. Indeed the NOx generation level
remains the same with and without the high hydrogen gas fuel passing through the oil
fuel line.
[0017] According to a first embodiment, the valve connecting the gas line and the oil line
is an on/off valve. According to a second embodiment, the valve connecting the gas
line and the oil line is a mass flow controller.
[0018] Moreover, the present invention refers to a method for refurbishment a current sequential
combustor for a gas turbine comprising a premix burner and a reheat burner, wherein:
- each premix burner is configured for injecting fuel in the compressed air in a diffusion
mode by a pilot and in a premix mode; and
- each premix burner comprises at least a gas fuel nozzle fed by a gas fuel line and
at least a oil gas nozzle fed by a oil fuel line.
[0019] The method of the present invention comprises the step of adding a connection between
the gas fuel line and the oil fuel line wherein this connection is configured for
selectively allowing part of gas fuel running in the gas fuel line to enter in the
oil fuel line. Once fed inside the oil fuel line the spilled part gas fuel is injected
by the oil nozzles in the combustion chamber. The method may comprise the step of
providing the above connection with a valve, for instance an on/off valve or a mass
flow controller.
[0020] It is to be understood that both the foregoing general description and the following
detailed description are exemplary, and are intended to provide further explanation
of the invention as claimed. Other advantages and features of the invention will be
apparent from the following description, drawings and claims.
[0021] The features of the invention believed to be novel are set forth with particularity
in the appended claims.
Brief description of drawings
[0022] Further benefits and advantages of the present invention will become apparent after
a careful reading of the detailed description with appropriate reference to the accompanying
drawings.
[0023] The invention itself, however, may be best understood by reference to the following
detailed description of the invention, which describes an exemplary embodiment of
the invention, taken in conjunction with the accompanying drawings, in which:
- figure 1 is a schematic view of a first embodiment of a gas turbine comprising a sequential
combustor that can be provided with the innovative component according to the present
invention;
- figure 2 is a schematic view of a second embodiment of a gas turbine comprising a
sequential combustor that can be provided with the innovative component according
to the present invention;
- figure 3 is a schematic view of the sequential combustor of the gas turbine disclosed
in figure 2 in two different operation conditions;
- figures 4 and 5 are schematic views of a burner of the sequential combustor of figure
3 in two different operation conditions; and
- figure 6 is a schematic view of burner fuel lines according to an embodiment of the
present invention.
Detailed description of preferred embodiments of the invention
[0024] In cooperation with the attached drawings, the technical contents and detailed description
of the present invention are described thereinafter according to preferred embodiments,
being not used to limit its executing scope. Any equivalent variation and modification
made according to appended claims is all covered by the claims claimed by the present
invention.
[0025] Reference will now be made to the drawing figures to describe the present invention
in detail.
[0026] Reference is now made to Fig. 1 that is a schematic view of a first example of a
gas turbine 1 comprising a sequential combustor wherein the first burner with a pilot
can be provided with the pilot fuel lines according to the present invention. In particular,
figure 1 discloses a gas turbine with a high pressure and a low pressure turbine.
Following the main gas flow 2, the gas turbine 1 of figure 1 comprises a compressor
3, a first combustor 31, a high-pressure turbine 5, a second combustor 32 and a low-pressure
turbine 7. The compressor 3 and the two turbines 5, 7 are part of or are connected
to a common rotor 8 rotating around an axis 9 and surrounded by a concentric casing
10. The compressor 3 is supplied with air and is provided with rotating blades 18
and stator vanes 19 configured for compressing the air entering the compressor 3.
Once left the compressor, the compressed air flows into a plenum 11 and from there
into a plurality of first burners 12 of the first combustor 31 arranged as a ring
around the axis 9. Each first burner 12 in configured for injecting fuel (supplied
by a first fuel supply 13) in the air flow, in particular this first burner 12 may
be defined as a "premix" burner because in configured for mixing the air and the injected
fuel before the spark point. Figures 4 and 5 (that will be described in the following)
disclose an example of a premix burner with a pilot that can be provided with the
pilot fuel lines according to the present invention. Please notice that the invention
however is not limited to present of a pilot. The fuel/compressed air mixture flows
into a first combustion chamber 4 annularly shaped where this mixture are combusted
via a forced ignition, for instance by a spark igniter. The resulting hot gas leaves
the first combustor chamber 4 and is partially expanded in the high-pressure turbine
5 performing work on the rotor 8. Downstream of the high-pressure turbine 5 the hot
gas partially expanded flows into a second burner 33 where fuel supplied by a fuel
lance 14 is injected. The partially expanded gas has a high temperature and contains
sufficient oxygen for a further combustion that occurred based on a self-ignition
in the second combustion chamber 6 arranged downstream the second burner 33. This
second burner 33 is also called "reheat" burner. The reheated hot gas leaves the second
combustion chamber 6 and flows in the low-pressure turbine 7 where it is expanded
performing work on the rotor 8. The low-pressure turbine 7 comprises a plurality of
stages, or rows, of rotor blades 15 arranged in series in the main flow direction.
Such stages of blades 15 are interposed by stages of stator vanes 16. The rotor blades
15 are connected to the rotor 8 whereas the stator vanes 16 are connected to a vane
carrier 17 that is a concentric casing surrounding the low-pressure turbine 7.
[0027] Reference is now made to Fig. 2 that is a schematic view of a second example of a
gas turbine 20 comprising a sequential combustor wherein the first burner with a pilot
can be provided with the pilot fuel lines according to the present invention. In particular,
figure 2 discloses a gas turbine 20 provided with a compressor 29, one turbine 21
and a sequential combustor 22. The sequential combustor 22 of figure 2 comprises a
plurality of so-called can combustors, i.e. a plurality of cylindrical casings wherein
each can combustor houses a plurality of first burners 24, for instance four first
burners 24, a first combustion chamber 25, a second burner 26, and a second combustion
chamber 27. Upstream the second burner 26 an air mixer (not represented) may be provided
configured for adding air in the hot gas leaving the first combustion chamber 25.
The sequential combustor arrangement is at least in part housed in an outer casing
28 supporting the plurality of can combustor 22 arranged as a ring around the turbine
axis. A first fuel is introduced via a first fuel injector (not shown) into the first
burners 24 wherein the fuel is mixed with the compressed gas supplied by the compressor
29. Also each first burner 24 of this embodiment is a "premix" burner configured for
generating a premix flame and a diffusion flame. Each first burner 24 of figure 2
and each first burner 12 of figure 1 is independently operable, i.e. each first burner
may be switched off independently on the other first burners and each first burner
may be operated independently in terms of ratio between the fuel injected in the diffusion
mode and the fuel injected in the premix mode. Finally, the hot gas leaving the second
combustion chamber 27 expands in the turbine 21 performing work on a rotor 30.
[0028] Reference is now made to Fig. 3 that is a schematic view of a can combustor 22 that
may be a combustor of the turbine of figure 2. In particular, figure 3 discloses the
combustor in two different operation conditions, i.e. with two different flames positions
inside the can combustor 22. Moreover, below figure 3 a diagram is present disclosing
how the temperature varies in these two different operation conditions inside the
can combustor 22. As known and as foregoing mentioned, the can combustor 22 is today
preferable because it has significant advantages in terms of both low emissions and
fuel flexibility. The first stage premixed burner 24 utilizes aerodynamic structures
to stabilize a propagating premix flame providing excellent flame stability and combustion
efficiency over an extensive operational range. This flame having a correct distance
from the burner nozzles is represented by the reference 34'. The second burner 26
in contrast is a primarily auto-ignition controlled burner. The flame generated by
the second burner 26 is represented by the reference 35'. These two contrasting methods
of generating the flames provide a substantial advantage in minimising NOx emissions
at base load while maximising the engine's turndown capability. The flexibility of
the can combustor 22 can be applied to allow low emission performance for a wide range
of fuels. For each fuel type an operational approach through the adjustment of the
inlet temperature of the second burner 26 (temperature at ref. 46 after the reference
47 representing the air dilution mixer) can be defined which allows both flame locations
to be correctly maintained. For higher reactivity fuels (e.g. high hydrogen or higher
hydrocarbon contents) the flames at the first 24 and the second burner 26 move upstream
as represented by the references 34 and 35. These movement towards the burners involves
some drawbacks, i.e. a high flame residence time (and therefore high NOx generation)
and overheating of the burner nozzles. A solution to move downstream the flames 34
35 to a correct position of flames 34' 35' may be reducing the first stage flame temperature
(reducing fuel injected in the first stage for passing from line 36 to line 37 in
diagram of Figure 3). At the same time it also accounts for the change in auto-ignition
delay time and hence flame location of the second stage whose position for the same
flame temperature can be controlled. If, for example, instead of natural gas a more
reactive fuel, i.e. hydrogen, is burnt, the first stage temperature has to be reduced.
As can be seen in Figure 3, reducing the first stage temperature alters the ignition
delay time of the second stage in the desired way to keep the flame 35 at its design
position 35'. In order to further increase the hydrogen content of the fuel up to
100% a lower second inlet temperature is required. Applicant developed a new solution
for allowing the feeding of higly reactive fuels. This solution is to realize hybrid
flames obtained by adjusting the distribution of fuel of some active first burners
between the diffusion and premixed mode, in particular by providing a high pilot fuel
rate. In this way the lean blow out margin (low temperature) of the first stage is
extended without any drawback of the prior art practice. Therefore, the first stage
can be operated with highly reactive fuels without injecting diluents while delivering
sufficiently lower inlet temperature levels for the second stage combustor. Starting
from the above hybrid operating mode, the present invention solves the problem of
safely performing the above operating step of feeding the burner with a "high diffusion
fuel flow rate". Indeed, a high diffusion fuel flow rate during normal operation requires
a high fuel pressure drop (more than 10 bar) and this high fuel pressure drop requires
a very high fuel pressure inside the gas fuel line feeding.
[0029] Reference is now made to figures 4 and 5 that are schematic views of an non limiting
example of a first or premix burner suitable for performing the invention in two different
operation conditions. According to this example the premix burner 41 is a burner configured
for generating a diffusion flame 42 (figure 4) and a premix flame 43 (figure 5). For
generating the diffusion flame 42 the fuel is directly injected in the combustion
chamber by a pilot lance 44 without any preliminary mixing with the coming compressed
air. For generating the premix flame 43, the fuel is mixed with the compressed air
before entering the combustion chamber. For instance the mixing may be realized by
passing the air in a conical casing 45 configured for generating a swirl wherein this
conical casing 45 is also provided with nozzles for injecting fuel in this swirl.
According the present invention, when the burner is fed by reactive fuel like H2-based
fuel, the method comprises the step switching off at least one of the first burners
(for instance at least a burner for each can combustor) and operating the remaining
active first burners for generating hybrid flames as combination of diffusion mode
and premix mode. Preferably, at least one of active first burners is operated so that
a significant amount of fuel is burnt in diffusion mode, in particular at least 5%
of the fuel fed to this burner. According to a different embodiment, in a can combustor
some burners on the first stage may be operated only in premix configuration and others
only in diffusion configuration.
[0030] According to a different embodiment, different burners may be operated simultaneously
in premix and in diffusion configuration with different ratios of diffusion/premix
mode. The switch-off of some of the first stage burners may be done with a specific
pattern in order to optimize the temperature distribution.
[0031] Reference in now made to figure 6 that is a schematic view of fuel lines according
to an embodiment of the present invention. The solution proposed is feeding part of
the high reactive gas fuel running inside the gas line into the oil line (already
present in the burner and usually used only for oil fuel feeding). According to the
embodiment of figure 6, the burner is provided with a gas fuel nozzle 48 and an oil
fuel nozzle 49. The gas fuel nozzle 48 is fed by a gas fuel line 50 connected at the
opposite end to a gas fuel source 51. The oil fuel nozzle 49 is fed by a oil fuel
line 52 connected at the opposite end to an oil fuel source 53. According to the invention
the burner is also provided with a connection 54 (i.e. at least a duct) fluidly connecting
the gas fuel line 50 with oil fuel line 52. According to the embodiment disclosed
in figure 6 the connection 54 is provided with a valve 55 configured for selectively
feeding part of the gas fuel running in the gas fuel line 50 inside the oil fuel line
52 so that the pressure present in the gas line may be reduced without any detrimental
impact on combustion. Of course the burner may comprise a plurality of gas and oil
nozzles fed by a plurality of fuel lines.
[0032] Although the invention has been explained in relation to its preferred embodiment(s)
as mentioned above, it is to be understood that many other possible modifications
and variations can be made without departing from the scope of the present invention.
It is, therefore, contemplated that the appended claim or claims will cover such modifications
and variations that fall within the true scope of the invention.
1. A sequential combustor (22) for a gas turbine (1, 20); the sequential combustor (22)
comprising:
- a first combustor provided with a plurality of first burners (12, 24) fed by compressed
air and configured for injecting fuel in the compressed air in a diffusion mode (42)
and in a premix mode (43), each first burners (12, 24) comprises at least a gas fuel
nozzle (48) fed by a gas fuel line (50) and at least a liquid fuel nozzle (49) fed
by a liquid fuel line (52);
- a second combustor provided with a plurality of second burners (26, 33) fed by hot
gas leaving the first combustor and configured for injecting fuel in the hot gas;
characterized in that the combustor (22) moreover comprises a fluidly connection (54) configured for selectively
connecting the gas fuel line (50) and the liquid fuel line (52) for allowing part
of gas fuel running in the gas fuel line (50) to enter in the liquid fuel line (52)
and to be injected by the liquid fuel nozzle (49).
2. Sequential combustor (22) as claimed in claim 1, wherein, the connection (54) is provided
with an on/off valve (55).
3. Sequential combustor (22) as claimed in claim 1, wherein, the connection (54) is provided
at a mass flow controller.
4. A method for operating a sequential combustor (22) for a gas turbine (1, 20); the
method comprising the steps of:
a) providing a sequential combustor (22) comprising:
- a first combustor provided with a plurality of first burners (12, 24) fed by compressed
air and configured for injecting fuel in the compressed air in a diffusion mode (42)
and in a premix mode (43), each first burners (12, 24) comprises at least a gas fuel
nozzle (48) fed by a gas fuel line (50) and at least a liquid fuel nozzle (49) fed
by a liquid fuel line (52);
- a second combustor provided with a plurality of second burners (26, 33) fed by hot
gas leaving the first combustor and configured for injecting fuel in the hot gas;
- a fluidly connection (54) configured for selectively connecting the gas fuel line
(50) and liquid fuel line (52) for allowing part of gas fuel running in the gas fuel
line (50) to enter in the liquid fuel line (52) and to be injected by the liquid fuel
nozzle (49)
b) feeding the first (12, 24) and second burners (26, 33) with a high reactive fuel;
c) switching off at least one of the first burners (12, 24);
d) operating the remaining active first burners so as to generate hybrid flames as
combination of diffusion mode and premix mode;
e) flowing at least part of the gas fuel running inside the gas fuel line (50) into
the liquid fuel line (52) through the connection (54);
5. Method as claimed in claim 4, wherein the method comprises the step of providing the
connection (54) with a valve (55).
6. Method as claimed in claim 4, wherein the method comprises the step of providing the
connection (54) with mass flow controller.
7. Method for refurbishment a sequential combustor for a gas turbine, the method comprising
the steps of:
a) providing a sequential combustor (22) comprising:
- a first combustor provided with a plurality of first burners (12, 24) fed by compressed
air and configured for injecting fuel in the compressed air in a diffusion mode (42)
and in a premix mode (43), each first burners (12, 24) comprises at least a gas fuel
nozzle (48) fed by a gas fuel line (50) and at least a liquid fuel nozzle (49) fed
by a liquid fuel line (52);
- a second combustor provided with a plurality of second burners (26, 33) fed by hot
gas leaving the first combustor and configured for injecting fuel in the hot gas;
b) adding a connection (54) between the gas fuel line (50) and the liquid fuel line
(52) for selectively allowing part of gas fuel running in the gas fuel line (50) to
enter in the liquid fuel line (52) and to be injected by the liquid fuel nozzle (49).
8. Method as claimed in claim 7, wherein the method comprises the step of providing the
connection (54) with a valve (55).
9. Method as claimed in claim 7, wherein the method comprises the step of providing the
connection (54) with mass flow controller.