TECHNICAL FIELD
[0001] The present disclosure relates to a method as set forth in the claims.
BACKGROUND OF THE DISCLOSURE
[0002] From
EP 718 470 a gas turbine engine is known in which two combustion chambers are provided in a
fluidly serial arrangement, such that a second of said combustion chambers receives
exhaust gases from the first one of said combustion chambers, with an intermediate
expansion turbine being fluidly interposed between the two combustion chambers. Generally,
the inlet temperature of the intermediate expansion turbine is an important process
parameter for the operation of the gas turbine engine. A direct measurement of these
temperatures under field conditions is not viable in an industrial use environment.
It is known from expansion turbines to measure a temperature at the outlet of the
expansion turbine, and derive the inlet temperature to the expansion turbine based
upon the outlet temperature and a pressure ratio or pressure drop over the expansion
turbine, whereas the calculation of the inlet temperature further takes into account
characteristics of the specific expansion turbine.
[0003] In gas turbine engines of the type known from
EP 718 470, the temperature downstream the intermediate expansion turbine, or upstream the second
combustor, respectively, is measured, and the inlet temperature of the intermediate
expansion turbine is calculated based upon said outlet temperature and pressure ratio
with further consideration of the thermodynamic behaviour of the specific expansion
turbine. The person having ordinary skill in the art is perfectly familiar with the
calculation of the expansion turbine inlet temperature based upon the expansion turbine
outlet temperature and the pressure ratio over the expansion turbine.
[0004] However, in gas turbine engines of the type known from
EP 718 470, the temperature downstream or at the outlet of the intermediate expansion turbine
is still at a level significantly above that at the outlet of a last or most downstream
expansion turbine in which the expansion to the final pressure of the gas turbine
process takes place. In particular, the temperature downstream the intermediate expansion
turbine reaches values sufficiently high to enable a spontaneous ignition of fuel
introduced into the second combustion chamber. Thus, for instance thermocouples used
for determination of the outlet temperature of the intermediate expansion turbine
need to operate under a harsh environment. Further, the pressure is still significantly
elevated, such that extreme care must be taken of tightness of the feedthrough of
instrumentation. The temperature measurement instrumentation requires careful maintenance.
[0005] An analogous issue is encountered when an engine operates with a staged combustion
with no intermediate expansion turbine fluidly interposed between two fluidly serially
arranged combustion stages, and a determination of the outlet temperature of an upstream
one of said combustion stages, or the inlet temperature of a downstream one of said
combustion stages, is required. High temperatures and pressures of the fluid result
in a challenging environment for temperature measurement instrumentation.
OUTLINE OF THE SUBJECT MATTER OF THE PRESENT DISCLOSURE
[0006] The present disclosure relates to a method of the type initially mentioned. It is
an objective of the herein disclosed subject matter to provide a method which enables
the determination of a temperature at the outlet of an upstream combustion stage in
a gas turbine having at least two serially arranged combustion stages. An upstream
combustion stage shall be understood as a combustion stage upstream of a last, most
downstream combustion stage. In a more specific aspect, a method shall be provided
which allows the required temperature determination without the need to place temperature
sensors inside fluids which have temperatures and/or pressures beyond a certain threshold
value. In this respect it may prove advantageous to have temperature sensors positioned
in the working fluid no more than upstream of the most upstream combustion stage and
downstream of the most downstream turbine.
[0007] This is achieved by the subject matter described in claim 1.
[0008] Further effects and advantages of the disclosed subject matter, whether explicitly
mentioned or not, will become apparent in view of the disclosure provided below.
[0009] Accordingly, disclosed is a method for determining an outlet temperature of an upstream
combustion stage in a gas turbine engine, the gas turbine engine having at least two
serially arranged combustion stages. It shall be noted that the temperatures referred
to are working fluid temperatures. A compressor is provided in fluid communication
with and upstream a first, most upstream, of said combustion stages. A last, most
downstream, expansion turbine is provided in fluid communication with and downstream
a last, most downstream, of said combustion stages. There may or may not be other
expansion turbines present in the gas turbine engine. It is understood that the last
expansion turbine is the turbine in which the working fluid of the gas turbine engine
is expanded to a terminal, final pressure of the thermodynamic process of the gas
turbine engine. Said pressure, most commonly, is at least essentially equal to the
pressure upstream the compressor, or, for air breathing gas turbine engines, the ambient
pressure. However, as the skilled person will readily appreciate, the pressure after
the last expansion turbine might be slightly higher than the pressure at the compressor
inlet or the ambient pressure, due to potential pressure losses for instance in an
exhaust duct, a heat recovery steam generator, silencers, a scrubber, and other devices
restricting an exhaust duct. The last expansion turbine may in certain embodiments
be the one and only expansion turbine of the gas turbine engine, while in other embodiments
intermediate expansion turbines may be present and fluidly interposed between combustion
stages. The method comprises obtaining at least one first parameter representative
of the inlet temperature of the last, most downstream, expansion turbine and/or the
outlet temperature of the last, most downstream, of said combustion stages, obtaining
at least one second parameter representative of the outlet temperature of the compressor
and/or the inlet temperature of the first, most upstream, of said combustion stages,
and obtaining the fuel massflows to each combustion stage and/or a fuel massflow ratio
between the combustion stages. An outlet temperature of an upstream combustion stage
different from the most downstream combustion stage is then obtained, in particular
calculated or computed, based upon said first and second parameters and the fuel massflows
to the combustion stages and/or the fuel massflow ratios.
[0010] Upstream and downstream refer to the flow direction of the working fluid through
the gas turbine engine.
[0011] "Obtaining" a parameter or value is to be understood in a broad sense, and may comprise,
while not being limited to, measuring a value or parameter directly or deriving a
value or parameter from other values or parameters. It is in this respect understood
that obtaining any of the at least one parameter representative of the inlet temperature
of the last expansion turbine and/or the outlet temperature of the last of said combustion
stages and the at least one second parameter representative of the outlet temperature
of the compressor and/or the inlet temperature of the first of said combustion stages
may in instances comprise a direct measurement of said at least one parameter. For
instance, a compressor outlet temperature may typically be obtained through a direct
measurement. However, a compressor outlet temperature may be represented by a combination
of other values, such as for instance, for a compressor with a known thermodynamic
characteristic, by a combination of conditions at the compressor inlet and/or ambient
conditions in case of an air breathing engine and/or a compressor pressure ratio and/or
a variable inlet guide vane position. It may be necessary to consider other parameters,
such as for instance a mass flow of liquid agent injected into the compressor. The
skilled person is perfectly familiar with obtaining a compressor outlet temperature
for a given compressor from such a set of parameters. Likewise, the temperature at
the inlet of the last expansion turbine may for a given expansion turbine typically
be determined based upon measurements of the exhaust temperature downstream the last
expansion turbine and a pressure ratio over the expansion turbine in further consideration
of the expansion turbine thermodynamic characteristics. The skilled person is also
perfectly familiar with these calculations. The above examples are in no way to be
considered as exhaustive, and the skilled person will readily be aware of or come
up with an abundance of ways how to represent these temperatures.
[0012] Moreover, it is not necessary that these temperatures are explicitly used in a calculation
of the outlet temperature of the upstream combustion stage, or a formula and/or computer
program used for calculation or computation, but it may well be sufficient of the
parameters representative of the temperatures to appear in a suitable combination.
[0013] A "parameter representative of' a temperature may be broadly understood as a parameter
having an influence on or being correlated with the said temperature, such that the
parameter alone or in combination with other parameters may be used to calculate and/or
to represent said temperature. This parameter may thus be said to represent the temperature,
and in particular changes of said parameter cause changes of the temperature.
[0014] The fuel massflow ratio is representative of the relative fuel massflows to the different
combustion stages. It may be represented as the ratio of the partial fuel massflows
to the different combustion stages to each other, but also as partial fuel mass flows
related to the total fuel mass flow to all combustion stages, and other parameters
the skilled person may deem appropriate. The fuel massflow ratio may be obtained from
measured mass flows, but may in certain embodiments be obtained from control signals
and/or control valve positions and/or measured fuel pressures.
[0015] It is noted that the pressures and temperatures at the inlet and outlet of certain
components of a gas turbine engine referred to are working fluid temperatures and
pressures. Further, the pressures and temperatures referred to in the context of this
application generally mean total pressures and temperatures, that is, the pressure
and temperature of the fluid when it has isentropically been decelerated to a standstill,
including the dynamic pressure head of a fluid flow and the temperature which corresponds
to the kinetic energy of a fluid flow.
[0016] It is noted that within the framework of the present disclosure the use of the indefinite
article "a" or "an" does in no way stipulate a singularity nor does it exclude the
presence of a multitude of the named member or feature. It is thus to be read in the
sense of "at least one" or "one or a multitude of'.
[0017] In certain types of gas turbine engines, an intermediate expansion turbine may be
provided and fluidly interposed between two combustion stages. It is readily appreciated
that in such instances the outlet temperature of a combustion stage immediately upstream
an intermediate expansion turbine equals or is an equivalent to the inlet temperature
of that intermediate expansion turbine. Thus, in embodiments of the method, wherein
at least one intermediate expansion turbine is provided and fluidly interposed between
at least two serial combustion stages, the method comprises obtaining a pressure ratio
over at least one intermediate expansion turbine, and obtaining, in particular calculating
or computing, an inlet temperature of said intermediate expansion turbine, or the
outlet temperature of a combustion stage arranged immediately upstream said intermediate
expansion turbine, wherein obtaining the outlet temperature of the upstream combustion
stage comprises further considering the pressure ratio over the intermediate expansion
turbine. In still more specific embodiments the method comprises obtaining a pressure
ratio over each intermediate expansion turbine and obtaining, in particular calculating
or computing, an inlet temperature of an intermediate expansion turbine, or the outlet
temperature of a combustion stage arranged immediately upstream an intermediate expansion
turbine, respectively, wherein obtaining the outlet temperature of the upstream combustion
stage comprises further considering the pressure ratios over all intermediate expansion
turbines.
[0018] In a general context the calculation of the outlet temperature of upstream combustion
stages is based upon calculating a balance of the enthalpies from the entry into a
first, most upstream, combustion stage to the outlet of a last, most downstream, expansion
turbine. With knowledge of the pressure ratio over an expansion turbine and the outlet
temperature of the expansion turbine, for a given expansion turbine, the enthalpy
drop over the expansion turbine can be derived with knowledge of certain thermodynamic
characteristics of the specific expansion turbine, and from there the inlet temperature
of the expansion turbine can be calculated. This can be done for each expansion turbine
in the gas turbine engine. However, as outlined above, a measurement of the exhaust
temperatures of intermediate expansion turbines has shown to be subject to certain
limitations. The same applies to a measurement of temperatures between two immediately
subsequent combustion stages. In calculating the balance of enthalpies from the entry
into the first, most upstream combustor until the exit from the last, most downstream
expansion turbine, the enthalpy added along said flowpath due to combustion can be
derived. The fuel massflow to each combustion stage or fuel massflow ratio enables
to determine the enthalpy added in each combustion stage. The inventors have discovered
that this balance enables the calculation of the temperatures upstream and downstream
each combustion stage and furthermore upstream and downstream each intermediate expansion
turbine, if present. Information indicative of the temperature downstream the last,
most downstream expansion turbine and upstream the first, most upstream combustion
stage is sufficient, wherein, as mentioned above, in particular the temperature upstream
the first combustion stage may be derived from other values.
[0019] Embodiments of the herein disclosed method further comprise considering a parameter
representative of at least one coolant mass flow in intermediate expansion turbines
and/ or the combustion stages and/or between two subsequent combustion stages for
the determination of the outlet temperature of the upstream combustion stage. For
instance, said parameter may be provided as a constant or coefficient in an equation
used for calculating said outlet temperature. It should be understood that an intermediate
turbine may or may not be provided between the two aforementioned combustion stages.
More specifically, also the temperatures of the coolant mass flows may be considered
in obtaining, more specifically in calculating or computing, said outlet temperature.
[0020] In aspects, the method may further comprise considering at least one parameter representative
of a at least one inert fluid mass flow and temperature of an inert fluid injected
into the working fluid mass flow of the gas turbine engine in obtaining an outlet
temperature of an upstream combustion stage. Said parameter may be measured mass flows
and temperatures, but the mass flow may for other, non-limiting instances be provided
as control valve positions.
[0021] In still further aspects, the herein disclosed method may comprise considering combustor
pressure drops in obtaining the outlet temperature of the upstream combustion stage.
[0022] In still further aspects the method may comprise further considering the fuel temperature
in obtaining, in particular calculating or computing, the outlet temperature of the
upstream combustion stage.
[0023] In certain specific embodiments of the herein disclosed method obtaining the at least
one first parameter representative of the inlet temperature of the last expansion
turbine and/or the outlet temperature of the last of said combustion stages comprises
obtaining an outlet temperature of the last expansion turbine, obtaining a pressure
ratio over the last expansion turbine, and at least one parameter representative of
the thermodynamic behavior of the last expansion turbine. This, per se, is a method
well-known to the skilled person and may comprise the so called "TIT formula", which
in instances is a polynomial with the outlet temperature of the last expansion turbine
and the pressure ratio over the last expansion turbine as variables, and the coefficients
representing the thermodynamic characteristics of the last expansion turbine. Also,
conditions of the air at the inlet to the compressor may be considered, such as the
relative humidity of ambient air. At the exit of the last expansion turbine the pressure,
as outlined above, may at least essentially equal the pressure at the compressor inlet
of the gas turbine engine, and may more specifically essentially equal the ambient
or atmospheric pressure, with the deviations as outlined above due to pressure losses
in an exhaust duct. The skilled person will readily appreciate that "essentially equals"
is used due to the fact that in view of pressure losses in a fluid passage to the
compressor inlet and in an exhaust flow path of the gas turbine engine those values
may slightly differ from each other and/or from the ambient pressure. Thus, the statement
still provides a clear teaching to the person having skill in the art. The temperature
of the working fluid at the outlet of the last expansion turbine is in most instances
reduced to a temperature range, dependent upon the gas turbine type and operating
regime, of at most 500°C - 700°C. The pressure and temperature conditions at the outlet
of the last expansion turbine allow an unproblematic application of temperature sensors
such as for instance thermocouples in the exhaust fluid flow emanating from the last
expansion turbine. In other embodiments the at least one first parameter representative
of the outlet temperature of the most downstream combustion stage and/or inlet temperature
of the most downstream expansion turbine may be obtained by other methods known to
or conceivable by a skilled person.
[0024] Obtaining the at least one second parameter representative of the outlet temperature
of the compressor and/or the inlet temperature of the first of the combustion stages
may comprise measuring the outlet temperature of the compressor and/or the inlet temperature
of the first of the combustion stages as a second parameter. However, in other embodiments
obtaining the at least one second parameter representative of the outlet temperature
of the compressor and/or the inlet temperature of the first of the combustion stages
comprises measuring a temperature and a pressure upstream of the compressor and a
pressure at the outlet of the compressor as second parameters. The pressure and temperature
upstream the compressor may be an ambient temperature and ambient pressure. Said ambient
measurements may also comprise measurements of the ambient humidity and using the
ambient humidity as a further second parameter. The method in said instances may further
comprise obtaining the position of the vanes in a variable inlet guide vane row as
a further second parameter. This method of deducing the outlet temperature of the
compressor or the inlet temperature of the first, most upstream combustion stage from
certain other parameters for a given compressor is well-known to the person having
skill in the art. In other embodiments the at least one second parameter representative
of the outlet temperature of the compressor and/or inlet temperature of the most downstream
combustion stage may be obtained by other methods known to or conceivable by a skilled
person.
[0025] Further, a mass flow of a liquid agent may be injected into a mass flow through the
compressor upstream of or inside the compressor. Said mass flow of liquid agent may
be a further second parameter.
[0026] It is understood that the features and embodiments disclosed above may be combined
with each other. It will further be appreciated that further embodiments are conceivable
within the scope of the present disclosure and the claimed subject matter which are
obvious and apparent to the skilled person.
BRIEF DESCRIPTION OF THE DRAWINGS
[0027] The subject matter of the present disclosure is now to be explained in more detail
by means of selected exemplary embodiments shown in the accompanying drawings. The
figures show
- Fig. 1
- a first exemplary embodiment of a gas turbine engine with two serially arranged combustion
stages, and
- Fig. 2
- a second exemplary embodiment of a gas turbine engine with two serially arranged combustion
stages, wherein an intermediate expansion turbine is fluidly interposed between the
two combustion stages.
[0028] It is understood that the drawings are highly schematic, and details not required
for instruction purposes may have been omitted for the ease of understanding and depiction.
It is further understood that the drawings show only selected, illustrative embodiments,
and embodiments not shown may still be well within the scope of the herein disclosed
and/or claimed subject matter.
EXEMPLARY MODES OF CARRYING OUT THE TEACHING OF THE PRESENT DISCLOSURE
[0029] Figure 1 shows a first exemplary embodiment of an air-breathing gas turbine engine
having two serially arranged combustion stages. The gas turbine engine comprises compressor
10, first or upstream combustion stage 21 and second or downstream combustion stage
22, and expansion turbine 30. Expansion turbine 30 is coupled to compressor 10 by
shaft 40 to drive the compressor and further a load, such as for instance a generator,
which is not shown in the depiction, but familiar to the person having skill in the
art. Each of combustion stages 21 and 22 may independently from each other be supplied
with a respective fuel mass flow
ṁFuel,1 to the first, upstream combustion stage 21 and
ṁFuel,2 to the second, downstream combustion stage 22. Compressor 10 is equipped with a row
of variable inlet guide vanes 11 which allow control of the inlet volume flow to compressor
10 and thus of the working fluid mass flow of the gas turbine engine. The position
of the variable inlet guide vanes is denoted by VIGV. During operation, compressor
11 receives a flow of inlet air 52 at temperature T
0 and pressure p
0. Pressure p
0 may in common, while non-limiting, instances be at least essentially equal an ambient
pressure, apart from potential pressure losses in air filters, silencers and/or other
installations in an inlet duct. Compressor 10 compresses the flow of inlet air to
a pressure p
1, which depends on the working fluid mass flow, flow characteristics of expansion
turbine 30, the inlet temperature to the turbine and potential further influencing
parameters. Due to the compression in compressor 10 the temperature of the fluid flowing
through the compressor is raised to T
1. The air flow is discharged from the compressor into combustion stage 21, where first
combustion stage fuel mass flow
ṁFuel,1 is combusted in the compressed air. Thereby, the temperature of flue gas flow 56
discharged from the first combustion stage 21 is raised to T
2, while the pressure due to inevitable losses of total pressure has dropped to p
2. Flue gas flow 56 is discharged from upstream combustion stage 21 into downstream
combustion stage 22, where a second combustion stage fuel mass flow
ṁFuel,2 is combusted in the still oxygen-rich flue gas. Splitting the total fuel mass flow
into two partial mass flows and combusting the two partial fuel mass flows in the
dedicated combustion stages which are fluidly arranged in series may yield advantages
for instance with respect to the formation of pollutants in the flue gas. In the second,
downstream combustion stage 22 the temperature of the flue gas is raised to T
3, while the pressure drops to p
3. A mass flow of flue gas 58 at temperature T
3 and pressure p
3 is discharged from the second, downstream combustion stage 22 into expansion turbine
30. In expansion turbine 30 the flue gas mass flow 58 discharged from second combustion
stage 22 is expanded to a pressure p
4, thereby generating useful power to drive compressor 10 and an external load. Due
to the expansion in the expansion turbine the temperature of the exhaust flow 60 has
decreases to T
4. The pressure p
4 downstream expansion turbine 30 may in non-nonlimiting instances be at least essentially
equal to ambient pressure, apart from pressure losses in installations downstream
in an exhaust duct, such as tubing of a heat recovery steam generator, scrubbers and
so forth. Likewise, as the skilled person will readily appreciate, expansion turbine
outlet pressure p
4 may at least essentially equal the compressor inlet pressure po, apart from pressure
losses in the exhaust duct and in the air intake. Generally speaking, while in the
embodiment shown in figure 1 expansion turbine 30 is the only expansion turbine of
the gas turbine engine, it is at the same time a last, most downstream expansion turbine.
Likewise, second, downstream combustion stage 22 may be referred to as most downstream
or last combustion stage.
[0030] Pressures p
0, p
1 and p
4 may be readily measured. Pressures p
2 and p
3 may also be obtained through direct measurement, or otherwise be accounted for through
known pressure loss characteristics of the combustion stages. However, while temperatures
T
0 at the compressor inlet, T
1 at the compressor outlet and T
4 at the outlet of last expansion turbine 30 may be obtained through direct measurement,
a reliable measurement of temperatures T
2 and T
3 at the outlets of the combustion stages turns out at least fairly difficult, if not
unfeasible in field applications. Methods for obtaining temperature T
3 at the outlet of the last, most downstream combustion stage 22 based upon the pressure
ratio p
3/p
4 over the last, most downstream expansion turbine 30 and the temperature T
4 at the outlet of the last, most downstream expansion turbine 30 are well-known to
the person having skill in the art. The ratio of the temperatures T
3 and T
4 at the inlet and outlet of expansion turbine 30 is coupled to the ratio of the pressures
at the inlet and outlet of expansion turbine 30 by thermodynamic laws, i.e. T
3/T
4 = f(p
3/p
4). That is, with further knowledge of the thermodynamic behavior of expansion turbine
30 and the certain constants of the fluid, such as the specific heat or specific heats
and/or the gas constant, the temperature T
3 at the inlet of expansion turbine 30 can be calculated as a function of the temperature
T4 at the outlet of expansion turbine 30 and the pressure ratio p
3/p
4 over the expansion turbine. In order to control combustion kinetics and pollutant
formation in combustion stages 21 and 22 it may prove highly desirable to obtain reliable
information about temperature T
2 at the outlet of first combustion stage 21, or at the inlet of second combustion
stage 22, respectively. According to the herein disclosed method, temperature T
2 at the outlet of the first combustion stage 21, or at the inlet of the second combustion
stage 22, respectively, is determined and obtained based upon a heat balance between
the outlet of compressor 10 and the inlet of expansion turbine 30. Based upon the
fuel mass flows
ṁFuel,1 and
ṁFuel,2 to the combustion stages 21 and 22, respectively, and in further consideration of
cooling air mass flows and pressure losses in the combustion stages, temperature T
2 can be calculated based upon a set of measured values and a thermodynamic model of
the gas turbine engine, and/or the components thereof, respectively, by an enthalpy
balance between the outlet of compressor 10 and the inlet of expansion turbine 30,
and over the first and second combustion stages. The fuel mass flows may be considered
in the calculations, or computations, respectively, by a fuel massflow ratio, which
may, non-limiting, be defined as
ṁFuel,1/
ṁFuel,2. The skilled person will be readily aware of which other influencing parameters,
like coolant mass flows and temperatures and thermodynamic behavior of components,
must be additionally considered in obtaining the desired temperatures.
[0031] The embodiment shown in figure 2 differs from the embodiment discussed above in that
an intermediate expansion turbine 31 is fluidly interposed between first combustion
stage 21 and second combustion stage 22. Expansion turbine 31 is through shaft 40
mechanically coupled to expansion turbine 30 and compressor 10. A fuel gas mass flow
56 is discharged from the first combustion stage 21 into intermediate expansion turbine
31. The temperature at the outlet of the first combustion stage, or at the inlet of
intermediate expansion turbine 31, respectively, is T
21, the pressure is p
21. In the intermediate expansion turbine 31 the working fluid is expanded from pressure
p
21 to pressure p
22, whereby the temperature decreases from T
21 to T
22. Temperature T
22 and pressure p
22 are the temperature and pressure at the outlet of intermediate expansion turbine
31 and at the inlet of second combustion stage 22. The ratio of the temperatures at
the inlet and outlet of intermediate expansion turbine 31 is coupled to the ratio
of the pressures at the inlet and outlet of the intermediate expansion turbine by
thermodynamic laws, i.e. T
21/T
22 = f(p
21/p
22). That is, with further knowledge of the thermodynamic behavior of intermediate expansion
turbine 31 one of the temperatures at the inlet or outlet of intermediate expansion
turbine 31 can be calculated as a function of the other one of said temperatures and
the pressure ratio p
21/p
22 over the intermediate expansion turbine. With knowledge of certain parameters representative
of temperature T
1 at the outlet of compressor 10 or at the inlet of first combustion stage 21, respectively,
and temperature T
3 at the outlet of the last, most downstream combustion stage 22 or at the inlet of
the last, most downstream expansion turbine 30, an enthalpy balance can be calculated.
That is, the difference of the enthalpies between compressed air mass flow 54 and
flue gas mass flow 58 must be equal to the enthalpies added in the combustion stages
minus the useful work extracted in intermediate expansion turbine 31. Said useful
work in turn is a function of the difference between temperatures T
21 - T
22. That is, with knowledge of the fuel mass flows to the combustion stages, or a ratio
thereof, respectively, and further the pressure ratio over intermediate expansion
turbine 31, temperatures T
21 at the outlet of the first, upstream combustion stage or the inlet of the intermediate
expansion turbine, respectively, and T
22 at the outlet of the intermediate expansion turbine or the inlet of the second, downstream
combustion stage can be calculated. The calculation may require recursions. The skilled
person will be readily aware of which other influencing parameters, like coolant mass
flows and temperatures and thermodynamic behavior of components, must be additionally
considered in obtaining the desired temperatures.
[0032] As is shown by virtue of these exemplary embodiments, in a gas turbine engine having
a multitude of serially arranged combustion stages the thermodynamic state of the
working fluid can be obtained at the outlet of each combustion stage without the need
to place temperature measurement instrumentation in the thermally highly loaded section
of the gas turbine engine between the first, most upstream combustion stage and the
outlet of the last, most downstream expansion turbine. In certain embodiments, such
instrumentation which, in view of the high pressures and temperatures, is potentially
subject to high maintenance requirements, can be omitted throughout the entire working
fluid flow path from the inlet to the compressor to the outlet of the last, most downstream
expansion turbine. Thereby, potentially unreliable measurements can be avoided to
have an impact on engine control, while omitting the instrumentation and the potentially
required high maintenance effort reduces cost. As further shown by virtue of the above
exemplary embodiments the method may be applied in serial combustion gas turbine engines
with as well as without an intermediate expansion turbine being fluidly interposed
between two combustion stages.
[0033] While the subject matter of the disclosure has been explained by means of exemplary
embodiments, it is understood that these are in no way intended to limit the scope
of the claimed invention. It will be appreciated that the claims cover embodiments
not explicitly shown or disclosed herein, and embodiments deviating from those disclosed
in the exemplary modes of carrying out the teaching of the present disclosure will
still be covered by the claims.
1. A method for determining an outlet temperature (T2, T21) of an upstream combustion stage (21) in a gas turbine engine, the gas turbine engine
having at least two serially arranged combustion stages (21, 22),
wherein a compressor (10) is provided in fluid communication with and upstream a first,
most upstream, of said combustion stages (21), and a last expansion turbine (30) is
provided in fluid communication with and downstream a last, most downstream, of said
combustion stages (22),
characterized in obtaining at least one first parameter representative of the inlet temperature (T3) of the last, most downstream, expansion turbine (30) and/or the outlet temperature
(T3) of the last, most downstream, of said combustion stages (22),
obtaining at least one second parameter representative of the outlet temperature (T1) of the compressor (10) and/or the inlet temperature (T1) of the first, most upstream, of said combustion stages (21),
obtaining the fuel massflows (ṁFuel,1, ṁFuel,2) to and/or a fuel massflow ratio between the combustion stages (21,22), and
obtaining an outlet temperature (T2, T21) of an upstream combustion stage (21) different from the most downstream combustion
stage (22) based upon said first and second parameters and the fuel massflows and/or
the fuel massflow ratio.
2. The method according to the preceding claim, wherein at least one intermediate expansion
turbine (31) is provided and fluidly interposed between at least two serial combustion
stages (21, 22), wherein the method is characterized in obtaining a pressure ratio (p21/p22) over at least one intermediate expansion turbine (31), and obtaining an inlet temperature
(T21) of said intermediate expansion turbine, or the outlet temperature (T21) of a combustion stage (21) arranged immediately upstream said intermediate expansion
turbine, wherein obtaining the outlet temperature of the upstream combustion stage
comprises further considering the pressure ratio over the intermediate expansion turbine.
3. The method according to the preceding claim, characterized in obtaining a pressure ratio (p21/p22) over each intermediate expansion turbine and obtaining an inlet temperature (T21) of an intermediate expansion turbine, or the outlet temperature (T21) of a combustion stage arranged immediately upstream an intermediate expansion turbine,
respectively, wherein obtaining the outlet temperature of the upstream combustion
stage comprises further considering the pressure ratios over all intermediate expansion
turbines.
4. The method according to any of the preceding claims, characterized in further comprising considering a parameter representative of at least one coolant
mass flow in intermediate expansion turbines and/ or the combustion stages and/or
between two subsequent combustion stages in determining the outlet temperature of
the upstream combustion stage.
5. The method according to the preceding claim, characterized in further comprising considering a parameter representative of the temperature of the
coolant mass flows in determining the outlet temperature of the upstream combustion
stage.
6. The method according to any of the preceding claims, characterized in further comprising considering at least one parameter representative of a at least
one inert fluid mass flow and temperature of an inert fluid injected into the working
fluid mass flow of the gas turbine engine in determining an outlet temperature of
an upstream combustion stage.
7. The method according to any preceding claim, characterized in further considering combustor pressure drops in obtaining the outlet temperature
of the upstream combustion stage.
8. The method according to any preceding claim, characterized in further considering the fuel temperature in obtaining the outlet temperature of the
upstream combustion stage.
9. The method according to any of the preceding claims, characterized in that obtaining the at least one first parameter representative of the inlet temperature
(T3) of the last expansion turbine (30) and/or the outlet temperature (T3) of the last of said combustion stages (22) comprises obtaining an outlet temperature
(T4) of the last expansion turbine (30), obtaining a pressure ratio (p3/p4) over the last expansion turbine, and at least one parameter representative of the
thermodynamic behavior of the last expansion turbine.
10. The method according to any of the preceding claims, characterized in that obtaining the at least one second parameter representative of the outlet temperature
(T1) of the compressor (10) and/or the inlet temperature (T1) of the first of the combustion stages (21) comprises measuring the outlet temperature
of the compressor and/or the inlet temperature of the first of the combustion stages
as a second parameter.
11. The method according to any of the preceding claims, characterized in that obtaining the at least one second parameter representative of the outlet temperature
(T1) of the compressor (10) and/or the inlet temperature (T1) of the first of the combustion stages (21) comprises measuring a temperature (To)
and a pressure (po) upstream of the compressor and a pressure (pi) at the outlet of
the compressor as second parameters.
12. The method according to the preceding claim, characterized in obtaining the position (VIGV) of the vanes in a variable inlet guide vane row as
a further second parameter.
13. The method according to the preceding claim, characterized in further injecting a mass flow of a liquid agent injected into a mass flow through
the compressor upstream of or inside the compressor, and determining said mass flow
as a further second parameter.