1. Introduction
Future emission-free long-distance commercial aircraft have to use the synergies between distributed electric drives and aerodynamic improvements to save energy, as proposed in [
1,
2]. The study [
3] is based on the proposals of [
1,
2] and illustrates the multi-fidelity design optimization of the long-range blended wing body in the sustainable and energy-efficient aviation (Project: Strategy-EXC 2163/1, SE
2A consortium;
Figure 1). These aerodynamics improvements can enable increased fuel efficiencies compared to designs based on the conventional tube–wing design with two or four propulsors. Here, some new air-frame technologies are used; for example, active flow control, active load alleviation, body layer ingestion (BLI), new materials, and structure concepts. Additionally, the distributed electrical propulsion (DEP) necessary for BLI enables a highly redundant drive system.
As it was shown in [
4], for an electrical drive system with conventional copper winding, the optimal current density in the winding with respect to system weight balance including the cooling devices is approximately 30–40 A/mm
2, yielding a power to weight ratio of approximately 15 kW/kg of the active material. This value is nearly halved if the power electronics and cooling system are taken into account. A more preferable option then, is electrical machines with superconducting windings. As already discussed in [
5], cryogenic hydrogen (LH2) is the most suitable approach for the storage of emission-free fuel. For superconducting machines, power densities at least of 20 kW/kg [
6] can be expected. In some papers, up to 55 kW/kg [
7] is reported. As the power losses are much smaller with superconducting machines, a much lighter and smaller cooling system can be expected, using the hydrogen flow to the fuel cell as a heat sink.
The preferred aircraft design offers space for volumetric cryotanks because of LH2’s poor volumetric energy density [
5]. Here, the feasibility of the power electronics is also discussed in detail and an approach for a lightweight highly efficient 20 kHz high-power inverter presented.
In [
8], possible solutions for the challenges of the onboard electrical power system are proposed. Wide band gap semiconductors, hybrid circuit breakers, and a DC voltage of 3 kV are the main key words. Future research and development will also focus on a feasible voltage range. Superconductors might be the solution for voltage reduction. As a power source, fuel cells combined with an advanced battery for peak loads are proposed as the most efficient (approximately 55–60%) solution. This requires high-power batteries with a high capacity of more than 2000 Wh/kg and 500 Wh/kg which will be available in the near future. An intermediate solution could be the combination of hydrogen-fueled gas turbines with superconducting generators. This design would have the disadvantage of significantly lower efficiency (approximately 35%) than a fuel cell/battery system. In [
9], the control of a fuel cell/battery system is studied and in [
10] a fuel cell-powered experimental small aircraft is presented.
As so far numerous technical challenges but no principal obstacles from physics have been recognized, the focus is now centered on the design study of superconducting electrical machines for fan drives.
7. Cooling Design and Simulations
Several proposals were made for hydrogen- or helium-cooled machines; e.g., in [
17], a capillary cooling of the superconducting coils with hydrogen in a two-phase (vapor, fluid) state is proposed. As hydrogen is excluded for safety reasons, and helium is always in the gaseous phase in the relevant temperature range, this approach is not applicable here.
In [
5], the total mass flow of hydrogen was already calculated for the example considered here, assuming an efficiency of the fuel cell of 55% and 99% each for the machines, inverters, and the DC backbone. This also incorporates the 500 kW demand of the on-board electric system. In between, higher efficiencies of machines and the DC backbone are found and investigated, yielding the modified data shown in
Table 6 for the load cases of
Table 1. The helium flow given here is the smallest flow that allows temperatures in the winding between 30 and 40 K. It was calculated with the help of numerical CFD simulation.
The cooling method of the tapes is a central design point of hts machines. The design depends on the losses on the one hand, and on the other hand, as hts motor tape coils fulfill multiple functions, it also depends on voltage, forces, and oscillations. Furthermore, thermal expansion must be regarded. A simple approach would be to integrate pipes which follow along the tape and thermal conductors to extract the heat. This can be feasible for weaker heat fluxes. Additional thermal conductors, especially metallic types, increase losses and package sizes. The concept presented here cools the hts components, and the iron parts are left warm. The coil components have to be mounted into a housing, which permits a gas flow and provides mechanical stability, as well as insulation. Experience in thermal insulation has also been gained in the construction and assembly of a high-load superconducting bearing [
18].
The general aim of the cooling design is to generate a high heat transfer coefficient at the lowest possible mass flow and lowest pressure drop to decrease pump power, mass, and also heat exchanger mass. The proposed solution to this is to drastically parallelize the flow of the cooling gas by multiple cooling channels parallel to the winding axis of the coil. As helium molecules are very small, these channels can have small diameters of some tenths of a millimeter.
Figure 15 shows an overview of the principle for four parallel tapes of a racetrack coil with integrated cooling slots.
Although the flow in these capillary tubes is nearly laminar, analytical calculations show that the difference between the temperatures of cooling gas flow and tube wall is striving towards zero, yielding high heat transfer coefficients of more than 1000 W/(m
2·K) at a pressure drop of approximately 10 mbar. This was also confirmed by CFD calculations (
Figure 16).
The slotted spacer is part of the coil and is integrated into each winding. As the gas flow is perpendicular to the winding direction, the coil has to be placed in a housing equipped with a small gap for the gas transport. All parts can be manufactured glass or carbon fiber-reinforced, which would also be beneficial to the integration of distributed cooling gas supply channels. A cylindrical vacuum housing with mechanical spacers and thermal reflectors has to be placed around the fiber-reinforced coil fixation housings to provide the thermal separation from the iron yoke. Furthermore, a plate has to be installed below and above the tape to stabilize the tapes and to conduct the high forces to the coil housing. Several CFD simulations were performed to determine gas parameters and temperatures depending on the load. One result is shown below. For this simulation, the SOLIDWORKS® Flow-Simulation was used with an input of all relevant cryogenic properties data. The objective was to keep the hts temperatures for given loads between 30 and 40 K at low gas flow rates, also at static peak load. These simulations yield, i.e., flow rates which are used for simulations of the complete circuit. For the inlet, a temperature of 30 K and a pressure of 2 bar were assumed. Boundary conditions were set to be symmetric for this case study. Due to low Reynolds numbers, the simulation was set to laminar in the course of the calculations.
Figure 16 displays the temperature results for the maximum load. Two tapes are cooled in parallel. For the whole machine, a mass flow of 76 g/s GHe at 30 K is needed. The tape then reaches a maximum temperature of 40 K. The pressure drop is rather low, reaching max. 10 mBar, decreasing to approximately 3 mBar in low load cases. A heat transfer coefficient of approximately 1500 W/(m
2·K) is reached with a Nusselt value of appr. 3.8 and a tube diameter of 100 µm.
The considerable low values in
Table 6 are due to H2’s high gravimetric energy density. Moreover, the
is only available if the plane operates in flight mode. At the airport, a small separate supply of cooling gas is necessary to maintain the superconducting state of all cryogenic devices.
The goal for superconducting tape winding is a temperature range between 30 and 50 K, to keep a safe distance to the transition temperature and to utilize high lift factors under AC operation. To maintain a low temperature of, e.g., 25–30 K, of the helium flowing into the machine, a reverse Brayton cycle cooler (RBCC) is a viable option although it adds some extra weight to the system. The system sketch in
Figure 17 shows the main components and exemplary data.
Pme: electrical power of the motor; ηm: motor efficiency.
Pth: thermal power difference.
PCw, PTw: shaft power of compressor and turbine.
PT, PC: thermal power of turbine and compressor.
ηpcT, ηpcC: polytropic efficiencies of turbine and compressor.
Compressor and turbine are fitted on the same shaft, the motor delivers the power difference. The electrical power consumption of the motor is calculated from the efficiency chain of turbine, compressor and motor.
The basic equations for the RBCC process are given in [
19]. The thermophysical data for hydrogen (para- and ortho hydrogen) and helium are taken from [
20,
21].
Table 6 gives the main input data of the RBCC for this example. The weight calculation for the turbo compressor engine set is taken also from [
19] for industrial machines. It should be kept in mind that there is an optimization potential if aerospace technology is applied to the construction. The weight will increase significantly if more than one stage is required on the turbine or the compressor.
As a heat exchanger, a plate heat exchanger in cross-counter flow design (
Figure 18) was chosen. Preferably, it is built from thin laser-welded aluminum plates. The distance between the plates was within 0.5 mm, adapted to the properties of the cooling gases. By this design, a good heat transfer coefficient is achieved. For the heat exchanger design, in a first step, the average logarithmic temperature difference was calculated from the temperatures of both media flows for all load cases. This is given by
The heat transfer in the heat exchanger itself is composed from the temperature drops between He and the heat exchanger wall, and from the temperature drop between the wall and H2. The temperature drop inside the wall was neglected. So, in a second step, the middle velocity and pressure drops were calculated with the equations given in [
22] for compressible media. To calculate the Nusselt numbers, the Gnielinski equation [
22] was used. With the obtained temperatures, the design parameters of the heat exchanger as number of cells or length and height of the cells were adapted to the average logarithmic temperature difference.
In
Figure 17, the calculated exemplary process data for one electrical 5.4 MW fan drive are given for the designing of LC 1. The shaft power of the compressor is dominant. With a polytropic efficiency of 0.8, an additional increase in temperature of 16.6 K has to be dissipated in the heat exchanger. To fully utilize an efficient counter flow heat exchanger, the temperature on the secondary entry
T2 (Point 2) has to be above the primary exit temperature
Twa (Point 6). From the power balance, the heat exchanger has to transfer the machine losses plus the compressor power input, minus the power extracted by the turbine. The results for this cooling circuit are shown in
Table 7.
It should be kept in mind that the hydrogen mass flow is prescribed by the consumption of the fuel cell. Increasing the He mass flow on the secondary side will reduce temperature T2 but also increase the compressor power. The temperature Twa drops then, with a small gradient, while the negative gradient of T2 is much higher. Furthermore, the temperature drop, ΔTWT, in the heat exchanger must be taken into account.
At a certain mass flow on the secondary equal temperatures T2 = Twa + ΔTWT appear as the limiting condition. With the data chosen here, there is a safe distance to this limit.
As a second order condition, the pressure ratio in the turbine was limited to 3.5, and in the compressor to 2.5, which are close to practice values for turbomachinery with radial machines.
The limits detected with the RBC cooler led to considerations to abandon the request for a low entry temperature
T4 = 25 K and to study a simple fan-driven secondary circuit as depicted in
Figure 19. This would avoid the largest part of the compressor power and allow a higher He mass flow with a smaller temperature rise in the machine. Additionally, a considerable saving of weight is possible.
In the simplified cooling system of
Figure 19, the same basic data as for
Figure 17 were used. As there is a higher sensitivity against the total pressure difference, the pressure drops in the piping (1a-1) and (3-3a) were estimated with additional 10 mbar.
By controlling the fan speed and pressure, the mass flow of He can be adopted to the different load cases. The exit temperatures at point 1 at the same mass flow are higher than with the RBCC, but are in the tolerable region for the superconductor. Optimization of the mass flow is possible. The limiting condition for the mass flow is now given by the equality of
T3 and
+
, with
of approximately 5–8 K. A significant saving in weight, cost, and power consumption are the main advantages of the simplified cooling system. The resulting data is presented in
Table 8. The simplified cooling system requires a lower power of below 0.8 kW compared to the Brayton cycle with about 4 kW.
A new challenge arises with load case 4: as the heat exchanger is dimensioned for LC1, a difference of the middle temperatures at LC4 (landing phase) arises. The basic reason is that the hydrogen mass flow is too small to remove the losses in LC4 at the given temperature levels. Here, an increase in the hydrogen flow from 8 g/s to 13 g/s can solve this problem. The surplus hydrogen is then recirculated to the tank. One solution to this problem could be to design a distributed helium supply system in the coil fixture to enable a helium flow reduction in the end windings at low power flight states, where losses in the active area (iron) are dominating.
In the case of a controllable rotor excitation, recirculation in this operation point would not be necessary. As a summary of above considerations, a simplified overview of a possible cooling setup of a sc motor and inverter, utilizing a blower and a heat exchanger is shown in
Figure 20. The superconducting drive is electrically powered by a fuel cell, a backup battery and an inverter.
The secondary cooling circuit cools the inverter and superconducting drive via helium, using the flow of LH2 to the fuel cell as a heat sink. From the sc machine perspective, a cryo-cooled inverter and superconducting power lines would be very beneficial to the cooling of the coils. The contribution and impact of the inverter and current lead on the cooling system are subject to further investigations, which are starting in late 2024.