The subject matter disclosed herein relates generally to a recuperator for a gas turbine engine, and in particular a recuperator for a microturbine.
Microturbines are gas turbines providing a maximum power output of up to 100 kilowatts and employing revolutions per minute ranging between 70,000 and 140,000 at maximum power.
Microturbines may be utilized in distributed energy resources and employ a compressor, combustor, turbine and electric generator to convert fuel into a local source of electric power. Their small footprint, high rotational speeds and high operating temperatures present significant design challenges.
A recuperator employs a counter-flow heat exchanger to recover heat from exhaust gas that is otherwise wasted. In the case of a gas turbine engine, providing the exhaust gas temperature exceeds the compressor outlet temperature, a recuperator can extract heat from the exhaust gas thereby to pre-heat air from the compressor outlet before mixing with fuel and further heating in the combustor. More specifically, the heat exchanger of the recuperator is arranged to provide a first flow path, into which exhaust gas from the turbine flows, and a second counter flow path, into which compressed air from the compressor flows, in such a way that heat transfer is facilitated from the first flow path to the second flow path. The pre-heated compressed air from the second flow path may then be passed on to the combustor for mixing with fuel and further heating and the cooled exhaust gas from the first flow path can be exhausted to the atmosphere. In this way recuperators can significantly increase the efficiency of a gas turbine, enabling greater extraction of useful energy from a given quantity of fuel.
The efficiency gain from the use of a recuperator is pronounced in the case of a microturbine given the relatively large temperature differential between the turbine and compressor outlets, and in this case efficiency may be doubled or more. This efficiency gain renders microturbines significantly more commercially attractive, and therefore innovation in this aspect of microturbines is undoubtedly instrumental to future widespread adoption of this technology.
A recuperator adds bulk to a gas turbine engine design. And yet in the case of a microturbine, there is a desire to maintain overall engine compactness. Prior art recuperator implementations offer unsatisfactory performance and add excessive bulk, particularly in the case of microturbine engines.
It is therefore desirable to provide a gas turbine engine recuperator offering improved efficiency whilst maintaining engine compactness, more or less necessitating a complete recuperator redesign.
Disclosed arrangements are further described hereinafter by way of example and with reference to the accompanying drawings, in which:
The gas turbine engine 100 comprises a rotor 105 mounted for rotation about an axis. The engine 100 is shown in cross section, but the skilled person will readily recognize that most of the components are substantially annular about the rotational axis of the rotor 105. This axis may be considered to define proximal and distal directions. According to the gas turbine engine 100 orientation in each of the figures of the present disclosure, the proximal direction extends to the left and distal extends to the right.
The gas turbine engine 100 comprises a proximally disposed compressor 110, e.g. a compressor wheel, and a distally disposed turbine 115, e.g. a turbine wheel, both of which are coupled to the rotor 105.
As shown in
Whilst the example shown in
As shown in
Recuperator design focuses on optimizing heat flow, extracting as much exhaust heat as possible to feed back into the system, minimizing heat loss, and controlling the volumetric footprint. A significant factor affecting these design requirements is the overall flow path adopted by the recuperator. The inventors of the present disclosure have identified that prior art recuperator implementations, particularly those for use with small gas turbine engines such as microturbines, adopt a flow path that leads to excessive heat loss, loss of efficiency and, particularly in the case of microturbines, adds excessive and unacceptable bulk.
The inventors of the present disclosure have therefore redesigned the recuperator flow path to improve overall performance and reduce the footprint.
This modified flow path of the recuperator disclosed herein shall now be described with reference to the specific example of a gas turbine engine 100 comprising recuperator 130 depicted in
To aid in understanding the flow path undertaken throughout the gas turbine engine 100 in
According to the first flow path stage, compressed air from the compressor 110 enters into first chamber 170. This chamber is in fluid communication with the bearing housing 118, turbine casing 119 and the radially outside surface of the heat exchanger 135. As shown in
Thus, the first chamber 170 provides a flow path between the compressor 110 and the axial intake 140 of the heat exchanger 135.
The positioning of the flow path according to this first flow path stage facilitates a certain amount of heat extraction from the turbine casing 119, bearing housing 118 and heat exchanger 135.
The outside surface of the heat exchanger 135 may comprise one or more of surface roughening, ribs or fins to facilitate enhanced heat extraction.
In this first flow path stage, the air may be at a pressure of around 300 kPa (3 bar) and a temperature of 470K.
Air from the first flow path stage is then heated by the heat exchanger 135 between the axial intake 140 and the axial exhaust 145 of the heat exchanger 135 via a first heat exchanger flow path 160.
According to the second flow path stage, the heated air from the axial exhaust 145 of the heat exchanger 135 enters into the second chamber 175. This second chamber 175 is in fluid communication with bellows 178, which is arranged to reduce localized pressure variation. The flow is directed to the combustion chamber 120.
Thus, the second chamber 175 provides a flow path between the axial exhaust 145 of the heat exchanger 135 and the combustion chamber 120.
The air in this second flow path stage may be at a pressure of 300 kPa (3 bar) and a temperature of 900K, having been heated by the heat exchanger 145.
Air from the second flow path stage is then combined with fuel and combusted within the combustion chamber 120, and then passed through the turbine 115 thereby to drive the rotor 105, which rotation may then be exploited by the compressor 110, for compressing intake air for the gas turbine engine 100, and converted into electric power by the electric generator 108. Air in the combustor may be at a pressure of 3 bar and a temperature of 1200K.
According to the third flow path stage, exhaust gas from the turbine exhaust 125 enters into the third chamber 180. As shown in the example of
In this example, the diffuser 182 is a radially inner surface defining the third chamber 180, which third chamber 180 can be seen to diverge in a distal direction between the turbine 115 and the radial intake 150 of the heat exchanger 135.
The exhaust gas is directed by the third chamber 180 to the radial intake 150 of the heat exchanger 135.
The exhaust gas in the third flow path stage may be at a pressure of around 100 kPa (1 bar) and 970K.
Exhaust gas from the third flow path stage is then directed through a second heat exchanger flow path 165 spanning the radial intake 150 and radial exhaust 155 of the heat exchanger 135, the heat exchanger 135 arranged to facilitate heat transfer from the second heat exchanger flow path 165 to the first heat exchanger flow path 160.
According to the fourth flow path stage, cooled exhaust gas exiting the radial exhaust 155 of the heat exchanger 135 enters into a fourth chamber 185 and is directed to an exhaust 190 of the gas turbine engine 100.
This fourth flow path stage is optional in the sense that exhaust gas could instead be exhausted directly from the heat exchanger 135.
In the specific example of
Thus the fourth chamber 185 may comprise a region surrounding a distal portion of the first chamber 170 thereby to define an interface 188 between the first chamber 170 and the fourth chamber 185, and this interface may comprise a portion disposed radially outside the heat exchanger and axially between the distal and proximal ends of the heat exchanger, this interface spanning at least half of the axial length of the heat exchanger. In this way air within the first chamber 170 is sandwiched between the radially outside surface of the heat exchanger and the cooled exhaust gas in the fourth chamber 185, facilitating further useful heat gain in the first flow path, radially inwards from the fourth chamber 185 and radially outwards from the heat exchanger 135.
The interface 188 may comprise surface one or more of surface roughening, ribs, fins or other means to increase the surface area and heat exchange potential, on the side in fluid communication with the fourth chamber 185, thereby to facilitate still greater extraction of heat from the cooled exhaust gas, which additional heat is otherwise lost.
The exhaust gas in the fourth flow path stage may be at a pressure of around 100 kPa (1 bar) and 550K.
As can be seen from the example shown
Insulative material may be provided radially inside the third chamber 180 and/or radially inside the heat exchanger 135. Such insulation facilitates reducing unwanted heat transfer in a distal direction between the hot turbine exhaust gas in the third chamber and the cooled exhaust gas in the fourth chamber, i.e. preventing a short circuit that bypasses the heat exchanger 135. For example, a heat insulation cap 184 may be provided. Alternatively substantially the entire region radially inside the heat exchanger 135 and between the third and fourth chambers may be filled with insulative material.
In the second and third examples shown in
In the example shown in
One or more of the recuperator, first to fourth chambers, heat exchanger may be annular and coaxial with the axis of the rotor 105.
As shown in the examples of
It will be recognized that the examples disclosed herein are not limiting and are capable of numerous modifications and substitutions.
Filing Document | Filing Date | Country | Kind |
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PCT/EP2020/055850 | 3/5/2020 | WO |