The present disclosure relates to aviation propulsion systems that combust hydrogen in general, and to aviation propulsion systems that utilize a hydrogen turboexpander in particular.
There is a great need within the global aviation industry to reduce carbon emissions and to reduce contributors to global warming. As the demand for air travel continues to rise, the aviation industry is developing sustainable solutions that reduce the sector's climate impacts. In the medium to long term, hydrogen may be used as a fuel that is complementary or an alternative to conventional jet fuels, sustainable aviation fuels (SAFs), or the like. to enable zero-carbon aviation. Overall system efficiency of converting renewable energy to engine power is a critical element in enabling the adoption of low or zero carbon fuel options. Engines configured to combust hydrogen may improve energy efficiency by leveraging the cryogenic properties of hydrogen through advanced thermodynamic engine cycles. The low temperature of hydrogen is an attractive heat-sink for gas turbine systems and the expansion of the stored liquid hydrogen into a gaseous state offers energy release which can improve overall system efficiency. Mechanical systems operable to improve the extraction of energy from hydrogen are desirable.
According to an aspect of the present disclosure, an aircraft propulsion system is provided that includes a gas turbine engine, a hydrogen-exhaust heat exchanger, and a hydrogen turboexpander. The gas turbine engine includes a compressor section, a combustion section having a combustor, a turbine section, and a turbine exhaust section. The gas turbine engine is in drive communication with a rotational load component. The hydrogen-exhaust heat exchanger is disposed relative to the turbine exhaust section so that a flow of exhaust gas exiting the turbine section is in communication with the hydrogen-exhaust heat exchanger. The hydrogen-exhaust heat exchanger is configured to change a flow of liquid hydrogen from a source of liquid hydrogen to a flow of gaseous hydrogen. The hydrogen turboexpander has a first rotor shaft and a second rotor shaft disposed parallel one another within a housing. The housing includes a first rotor shaft cavity configured to receive the first rotor shaft and a second rotor shaft cavity configured to receive the second rotor shaft. The housing further includes an inlet port to receive the flow of gaseous hydrogen and an exit port for the flow of gaseous hydrogen to exit the hydrogen turboexpander. The first rotor shaft and the first rotor shaft cavity define a first rotor shaft fluid flow path (RSFFP). The second rotor shaft and the second rotor shaft cavity define a second RSFFP. The hydrogen turboexpander is configured with the first RSFFP in series with the second RSFFP between the inlet port and the exit port. The exit port is in fluid communication with the combustor.
In any of the aspects or embodiments described above and herein, the first rotor shaft (FRS) has a FRS first axial end and a FRS second axial end and a plurality of first rotors, and wherein the second rotor shaft (SRS) has an SRS first axial end and an SRS second axial end and a plurality of second rotors, and the inlet port may be in fluid communication with the first rotor shaft adjacent the FRS first axial end of the first rotor shaft, and the first rotor shaft may be in fluid communication with the second rotor shaft via a first inter-rotor passage disposed adjacent the FRS second axial end and the SRS first axial end.
In any of the aspects or embodiments described above and herein, the second rotor shaft may be in fluid communication with the exit port adjacent the SRS second axial end.
In any of the aspects or embodiments described above and herein, the hydrogen turboexpander may include a bypass passage and a relief valve. The bypass passage is in fluid communication with the first inter rotor passage and in fluid communication with the second rotor shaft adjacent the SRS second axial end. The relief valve may be controllable to be in an open configuration that permits fluid flow through the bypass passage and in a closed configuration that at least substantially blocks fluid flow through the bypass passage. In the closed configuration, appreciably no fluid flow passes through the second RSFFP.
In any of the aspects or embodiments described above and herein, the relief valve may be in communication with a controller configured to control operation of the relief valve.
In any of the aspects or embodiments described above and herein, the first rotor shaft and the second rotor shaft may rotate independently of one another.
In any of the aspects or embodiments described above and herein, the hydrogen turboexpander may be configured such that the first rotor shaft rotates at a first rotational velocity, and the second rotor shaft rotates at a second rotational velocity, and the first rotational velocity equals the second rotational velocity.
In any of the aspects or embodiments described above and herein, the hydrogen turboexpander may be configured such that the first rotor shaft rotates at a first rotational velocity, and the second rotor shaft rotates at a second rotational velocity, and the first rotational velocity does not equal the second rotational velocity.
In any of the aspects or embodiments described above and herein, the hydrogen turboexpander may be configured such that the first rotor shaft produces a first amount of power from the flow of gaseous hydrogen, and the second rotor shaft produces a second amount of power from the flow of gaseous hydrogen, and the first amount of power equals the second amount of power.
In any of the aspects or embodiments described above and herein, the hydrogen turboexpander may be configured such that the first rotor shaft produces a first amount of power from the flow of gaseous hydrogen, and the second rotor shaft produces a second amount of power from the flow of gaseous hydrogen, and the first amount of power does not equal the second amount of power.
In any of the aspects or embodiments described above and herein, at least one of the first rotor shaft or the second rotor shaft may be in drive communication with a system component, and the system component may be a reduction gearbox or an electric generator.
In any of the aspects or embodiments described above and herein, the hydrogen turboexpander may further include a third rotor shaft and the housing may further include a third rotor shaft cavity configured to receive the third rotor shaft, and wherein the third rotor shaft and the third rotor shaft cavity define a third RSFFP, and wherein the first rotor shaft, the second rotor shaft, and the third rotor shaft are disposed parallel one another within a housing, and wherein the third rotor shaft (TRS) has a TRS first axial end and a TRS second axial end and a plurality of third rotors, and the inlet port may be in fluid communication with first rotor shaft adjacent the FRS first axial end, and the first rotor shaft may be in fluid communication with the second rotor shaft via a first inter rotor passage disposed adjacent the FRS second axial end, and the second rotor shaft may be in fluid communication with the third rotor shaft via a second inter rotor passage disposed adjacent to the SRS second axial end, and the third rotor shaft may be in fluid communication with the exit port adjacent the TRS second axial end.
In any of the aspects or embodiments described above and herein, the hydrogen expander may include a first bypass passage and a first relief valve, wherein the first bypass passage is in fluid communication with the first inter rotor passage and in fluid communication with the second rotor shaft adjacent the SRS second axial end, and the first relief valve may be controllable to be in a first open configuration that permits fluid flow through the first bypass passage and in a first closed configuration that at least substantially blocks fluid flow through the first bypass passage, and wherein in the first closed configuration appreciably no fluid flow passes through the second RSFFP, and the hydrogen turboexpander may include a second bypass passage and a second relief valve, wherein the second bypass passage is in fluid communication with the second inter rotor passage and in fluid communication with the third rotor shaft adjacent the TRS second axial end, and the second relief valve may be controllable to be in a second open configuration that permits fluid flow through the second bypass passage and in a second closed configuration that at least substantially blocks fluid flow through the second bypass passage, and wherein in the second closed configuration appreciably no fluid flow passes through the third RSFFP.
In any of the aspects or embodiments described above and herein, the first rotor shaft, the second rotor shaft, and the third rotor shaft may rotate independently of one another.
In any of the aspects or embodiments described above and herein, the hydrogen turboexpander may be configured such that the first rotor shaft rotates at a first rotational velocity, the second rotor shaft rotates at a second rotational velocity, and the third rotor shaft rotates at a third rotational velocity, and the hydrogen turboexpander may be operable in a first configuration wherein the first rotational velocity, the second rotational velocity, and the third rotational velocity equal one another, and may be operable in a second configuration wherein one of the first rotational velocity, the second rotational velocity, or the third rotational velocity does not equal another of the first rotational velocity, the second rotational velocity, or the third rotational velocity.
In any of the aspects or embodiments described above and herein, at least one of the first rotor shaft, the second rotor shaft, or the third rotor shaft may be in drive communication with a reduction gearbox.
In any of the aspects or embodiments described above and herein, the first rotor shaft, the second rotor shaft, and the third rotor shaft may be disposed in a symmetrical arrangement about a center of the housing.
In any of the aspects or embodiments described above and herein, at least one of the first rotor shaft, the second rotor shaft, or the third rotor shaft may be in drive communication with an electric generator.
According to an aspect of the present disclosure, a hydrogen turboexpander is provided that includes a housing, a first rotor shaft, and a second rotor shaft. The housing has a first rotor shaft cavity, a second rotor shaft cavity, a gas inlet port, and a gas exit port. The first rotor shaft is disposed in the first rotor shaft cavity. The second rotor shaft is disposed in the second rotor shaft cavity. The first and second rotor shafts are disposed parallel one another within the housing. The first rotor shaft and the first rotor shaft cavity define a first rotor shaft fluid flow path (RSFFP), and the second rotor shaft and the second rotor shaft cavity define a second RSFFP. The hydrogen turboexpander is configured with the first RSFFP in series with the second RSFFP between the inlet port and the exit port.
The foregoing features and elements may be combined in various combinations without exclusivity, unless expressly indicated otherwise. For example, aspects and/or embodiments of the present disclosure may include any one or more of the individual features or elements disclosed above and/or below alone or in any combination thereof. These features and elements as well as the operation thereof will become more apparent in light of the following description and the accompanying drawings. It should be understood, however, the following description and drawings are intended to be exemplary in nature and non-limiting.
The terms “forward”, “leading”, “aft, “trailing” may be used herein to indicate the relative position of a component or surface within the turbine engine 28. In an engine like that shown in
The turbine engine 28 includes a compressor section 32, a combustion section 34, a turbine section 36, and a shaft 54 connecting the compressor section 32 to the turbine section 36 and the rotational load component 52. The compressor section 32 represents a single compressor section or a plurality of compressor sections; e.g., a high pressure compressor (“HPC”) and a low pressure compressor (“LPC”). The compressor section 32 may include axial type compressors, or centrifugal type compressors, or any combination of axial and radial compressors. The combustion section 34 includes a combustor 56. The turbine section 36 represents a single turbine section or a plurality of turbine sections; e.g., a high pressure turbine (“HPT”) and a low pressure turbine (“LPT”). The shaft 54 represents a single shaft or multiple shafts; e.g., a low pressure shaft and a high pressure shaft. The turbine engine 28 is in drive communication with the rotational load component 52; i.e., the propulsion system 26 is configured so that the turbine engine 28 drives the rotational load component 52. As will be described herein, in some embodiments the gaseous hydrogen turboexpander 50 may also be in drive communication with the rotational load component 52. Hence, and depending on the embodiment, the rotational load component 52 may be driven by the turbine engine 28, or by the gaseous hydrogen turboexpander 50, or some combination thereof. Non-limiting examples of a rotational load component 52 include a propeller, a reduction gear box, a fan, a rotor, or the like, or any combination thereof. For example, a reduction gear box 58 (e.g., see
The hydrogen/exhaust heat exchanger 48 is disposed within the exhaust gas stream exiting the turbine section of the turbine engine 28; i.e., within the turbine exhaust section 38. The hydrogen/exhaust heat exchanger 48 is configured to receive a flow of liquid hydrogen and subject that liquid hydrogen to the high temperature exhaust gas stream exiting the turbine section 36 during operation of the turbine engine 28. The hydrogen/exhaust heat exchanger 48 is configured to keep the flow of liquid hydrogen separate from the high temperature exhaust gas stream. The thermal energy transferred from the exhaust gas stream to the liquid hydrogen via the hydrogen/exhaust heat exchanger 48 causes the liquid hydrogen (“LH2”) to change from a liquid phase to a gaseous phase (“GH2”). The system shown in
In some embodiments, the exhaust gas path upstream of the hydrogen/exhaust heat exchanger 48 may be configured to diffuse the exhaust gas flow prior to it engaging with the hydrogen/exhaust heat exchanger 48 to decrease the velocity of the exhaust gas.
The system schematically shown in
The gaseous hydrogen turboexpander 50 is configured to utilize a flow of gaseous hydrogen from the hydrogen/exhaust heat exchanger 48 to provide drive power that may be used to drive the rotational load component 52, or to drive one or more propulsion system 26 components (e.g., an electrical generator 60A, 60B), or any combination thereof. Gaseous hydrogen exiting the gaseous hydrogen turboexpander 50 is provided to the combustor 56 of the turbine engine 28 for combustion therein.
Referring to
The turboexpander 50 embodiment schematically shown in
Subject to a fluid flow bypass as will be detailed herein, the connected rotor shaft fluid flow paths 88 create a single fluid flow path for expanding the gaseous hydrogen across all the rotor shafts 66 disposed within the housing 64; e.g., from the H2 inlet port 68 to a first RSFFP 88, and then to a second RSFFP 88, and then to the H2 exit port 70 as shown schematically in
The turboexpander 50 may be configured so that the rotor shafts 66 rotate independently of one another within the housing 64. The turboexpander 50 may also be configured so that the rotor shafts 66 rotate at the same rotational velocity (RV) (i.e., S1 RV=S2 RV), or alternatively the turboexpander 50 may be configured so that different rotor shafts 66 rotate at different rotational velocities (i.e., S1 RV≠S2 RV). In some embodiments, different (or same) rotational velocities may be achieved by configuring a given rotor shaft 66 (e.g., configuring the rotor shaft 66 diameter) based on the rotor shaft 66 position in the series hydrogen expansion flow within the turboexpander 50. In some embodiments, the turboexpander 50 may be configured so that the rotor shafts 66 each produce the same amount of power, or select different amounts of power for a given flow of gaseous hydrogen. The turboexpander 50 may be configured so that each rotor shaft 66 produces a certain predetermined amount of power for a given gaseous hydrogen flow by using differently configured rotor shafts 66 in series and/or by using bypass passages 76 and relief valves 90 as will be detailed herein. As will be detailed herein, the power produced by a plurality of the rotor shafts 66 may be combined via a gearbox 58 (e.g., as described herein and shown in
A bypass passage 76 and relief valve 90 may be in fluid communication at the exit of a respective rotor shaft fluid flow path 88 that permits a subsequent/downstream rotor shaft 66 and rotor shaft fluid flow path 88 to be bypassed. The relief valve 90 may be configured to alter fluid flow within the bypass passage 76. For example, in some embodiments the relief valve 90 may be controlled to be in a fully open configuration or in a completely closed configuration. The “completely closed” configuration may block 100% of fluid flow through the bypass passage 76, or the “completely closed” configuration may block substantially all of the fluid flow through the bypass passage 76. A relief valve 90 that substantially blocks fluid flow through the bypass passage 76 may permit an inconsequential amount of fluid flow (i.e., leakage) in operational terms; e.g., the flow leakage through the substantially closed relief valve 90 does not affect the performance of the turboexpander 50. In some embodiments, the relief valve 90 may be controlled to be in a plurality of open configurations (e.g., 25% open, 50% open, 75% open, and the like) or in a completely closed configuration. The bypass passage(s) 76 and relief valve(s) 90 allow the hydrogen passing through the turboexpander 50 to bypass expansion on a downstream rotor shaft(s) 66, thereby providing flexibility to manage variable pressures from connected systems upstream and downstream of the turboexpander 50.
The hydrogen turboexpander 50 embodiment shown in
In some embodiments, the operation of components of the present disclosure propulsion system 26 may be controlled using a controller 62; e.g., see
During operation of the present disclosure propulsion system 26 shown in
While the principles of the disclosure have been described above in connection with specific apparatuses and methods, it is to be clearly understood that this description is made only by way of example and not as limitation on the scope of the disclosure. Specific details are given in the above description to provide a thorough understanding of the embodiments. However, it is understood that the embodiments may be practiced without these specific details.
It is noted that the embodiments may be described as a process which is depicted as a flowchart, a flow diagram, a block diagram, etc. Although any one of these structures may describe the operations as a sequential process, many of the operations can be performed in parallel or concurrently. In addition, the order of the operations may be rearranged. A process may correspond to a method, a function, a procedure, a subroutine, a subprogram, etc.
The singular forms “a,” “an,” and “the” refer to one or more than one, unless the context clearly dictates otherwise. For example, the term “comprising a specimen” includes single or plural specimens and is considered equivalent to the phrase “comprising at least one specimen.” The term “or” refers to a single element of stated alternative elements or a combination of two or more elements unless the context clearly indicates otherwise. As used herein, “comprises” means “includes.” Thus, “comprising A or B,” means “including A or B, or A and B,” without excluding additional elements.
It is noted that various connections are set forth between elements in the present description and drawings (the contents of which are included in this disclosure by way of reference). It is noted that these connections are general and, unless specified otherwise, may be direct or indirect and that this specification is not intended to be limiting in this respect. Any reference to attached, fixed, connected or the like may include permanent, removable, temporary, partial, full and/or any other possible attachment option.
No element, component, or method step in the present disclosure is intended to be dedicated to the public regardless of whether the element, component, or method step is explicitly recited in the claims. No claim element herein is to be construed under the provisions of 35 U.S.C. 112(f) unless the element is expressly recited using the phrase “means for.” As used herein, the terms “comprise”, “comprising”, or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
While various inventive aspects, concepts and features of the disclosures may be described and illustrated herein as embodied in combination in the exemplary embodiments, these various aspects, concepts, and features may be used in many alternative embodiments, either individually or in various combinations and sub-combinations thereof. Unless expressly excluded herein all such combinations and sub-combinations are intended to be within the scope of the present application. Still further, while various alternative embodiments as to the various aspects, concepts, and features of the disclosures—such as alternative materials, structures, configurations, methods, devices, and components, and so on—may be described herein, such descriptions are not intended to be a complete or exhaustive list of available alternative embodiments, whether presently known or later developed. Those skilled in the art may readily adopt one or more of the inventive aspects, concepts, or features into additional embodiments and uses within the scope of the present application even if such embodiments are not expressly disclosed herein. For example, in the exemplary embodiments described above within the Detailed Description portion of the present specification, elements may be described as individual units and shown as independent of one another to facilitate the description. In alternative embodiments, such elements may be configured as combined elements. It is further noted that various method or process steps for embodiments of the present disclosure are described herein. The description may present method and/or process steps as a particular sequence. However, to the extent that the method or process does not rely on the particular order of steps set forth herein, the method or process should not be limited to the particular sequence of steps described. As one of ordinary skill in the art would appreciate, other sequences of steps may be possible. Therefore, the particular order of the steps set forth in the description should not be construed as a limitation.
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