
Source: Liquid Hydrogen Systems Course, Moran Innovation LLC, 2025.
I had two very interesting conversations recently that touched on aspects of thermodynamic behavior in a liquid hydrogen (LH2) system. The first was with a US organization involved with LH2 fueling stations looking at pump cavitation. The second was a company in the EU that is retrofitting and recertifying a commercial aircraft for LH2. In both cases, thermal stratification is an important design and operational consideration.
Steam Analogies
Working with LH2 and other cryogenic systems requires developing an accurate mental model and intuition about the associated thermodynamic behaviors. Many systems do not operate with a fluid near its saturation conditions as is routinely done with LH2. Notable exceptions are refrigerants and steam, with steam engines and power cycles being perhaps the closest analogous systems.
Steam engines were the original workhorses of the Industrial Revolution, and associated boiler explosions were the catalyst for developing the first ASME Boiler and Pressure Vessel Code (B&PVC). Not many are in use any more beyond a few steam engine trains, tractors, and other historical machines. Unfortunately, there are still occasional accidents with them that provide lessons to learn.
A number of years ago, a steam engine tractor heading to a county fair was pulled over by the local police because its steel treads were tearing up the asphalt road it was on. When the tractor stopped, its boiler exploded. The operator had allowed the water in the boiler to get too low and the boiler had either a malfunctioning or improperly sized pressure relief valve. Thermal stratification in the boiler wall above the low water level caused rapid vaporization and pressure increase when the tractor sloshed the puddle of water onto the much hotter portion of the boiler wall as the tractor came to a stop.
Steam power plants like the one I started my engineering career at in the early 1980s provide additional insights for LH2 systems. Below is a representative schematic showing the boiler, pressure stages, heat exchangers, and other subsystems used to maximize overall plant efficiency. At its core, it's all about managing temperature differentials and heat exchange to drive the turbines which are shaft-connected to the generator. Drop the temperatures by a several hundred degrees C, and some aspects of this system and its operation share similarities with LH2 systems.

Source: Thermal Power Plant
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Source: Liquid Hydrogen Systems Course, Moran Innovation LLC, 2025. |
Steam Analogies
Working with LH2 and other cryogenic systems requires developing an accurate mental model and intuition about the associated thermodynamic behaviors. Many systems do not operate with a fluid near its saturation conditions as is routinely done with LH2. Notable exceptions are refrigerants and steam, with steam engines and power cycles being perhaps the closest analogous systems.
Steam engines were the original workhorses of the Industrial Revolution, and associated boiler explosions were the catalyst for developing the first ASME Boiler and Pressure Vessel Code (B&PVC). Not many are in use any more beyond a few steam engine trains, tractors, and other historical machines. Unfortunately, there are still occasional accidents with them that provide lessons to learn.
A number of years ago, a steam engine tractor heading to a county fair was pulled over by the local police because its steel treads were tearing up the asphalt road it was on. When the tractor stopped, its boiler exploded. The operator had allowed the water in the boiler to get too low and the boiler had either a malfunctioning or improperly sized pressure relief valve. Thermal stratification in the boiler wall above the low water level caused rapid vaporization and pressure increase when the tractor sloshed the puddle of water onto the much hotter portion of the boiler wall as the tractor came to a stop.
Steam power plants like the one I started my engineering career at in the early 1980s provide additional insights for LH2 systems. Below is a representative schematic showing the boiler, pressure stages, heat exchangers, and other subsystems used to maximize overall plant efficiency. At its core, it's all about managing temperature differentials and heat exchange to drive the turbines which are shaft-connected to the generator. Drop the temperatures by a several hundred degrees C, and some aspects of this system and its operation share similarities with LH2 systems.
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Source: Thermal Power Plant |
Stationary LH2 Systems
Cavitation is a potential issue in all cryogenic liquid systems, and thermal stratification in the liquid of a storage tank can play a role. Cavitation occurs when the local pressure in some part of the flow system drops below the saturation pressure of the liquid. This causes vapor to form that can damage components and diminish, stall, or even reverse flow in the system.
There are two primary operational parameters that affect cavitation: liquid temperature and system pressures. The lower the liquid temperature, the lower the saturation pressure required for cavitation to occur. Thermal stratification near the interface of a stationary storage tank is important to consider in this regard since draining a tank can introduce warmer liquid into the system as the tank level reaches the liquid thermal boundary.
For local system pressures, the pressure drops through all components, pipe lengths, and elevation changes must be addressed along with the source pressure and downstream exit pressure. In addition, pumps have a net positive suction head (pressure) (NPSH or NPSP) that must be maintained during operation.
Below is an example analysis I did for a liquid nitrogen system modification designed to feed a vacuum chamber coldwall during planned static testing of a J-2X rocket engine. This was a pressure fed system with no pumps, but avoiding cavitation was still a critical concern.
Mobile LH2 Systems
In cryogenic liquid systems subject to acceleration forces due to vehicle motion, all of the above issues with thermal stratification and cavitation apply. However, another issue must also be considered: liquid sloshing. There are dynamic load effects on a vehicle during slosh that are well known for any fuel, but thermodynamic effects (pressure and temperature) must also be considered for cryogenic systems just like the old steam engines previously mentioned.
When sloshing occurs in a tank that has thermal stratification near the liquid interface, a drop in pressure can occur as the cooler bulk liquid circulates to the interface causing increased condensation. This pressure drop (or ullage collapse) impacts the mass flow out of the tank during fueling, engine feed, or fuel cell feed operations. Below is a slide showing some of the published test results we did at NASA in the early 1990s on LH2 sloshing in a spherical tank.
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Source: Liquid Hydrogen Systems Course, Moran Innovation LLC, 2025 |
Some Mitigation Strategies
It's worth mentioning that thermal stratification can also work in your favor in some situations. For example, suppose you have a LH2 storage tank sitting for a period of time and self-pressurizing due to boiloff. If you mix the liquid, the tank pressure will drop as the thermal boundary layer near the interface is disrupted thereby significantly prolonging the vent-free dormancy time. The mixing can be mechanical, or induced by vapor or liquid injection into the tank.
For other situations, a few design and operational mitigation strategies can be considered:
- Keep the entire LH2 tank near saturation conditions by warming the liquid uniformly with a heat exchanger or heater. This inhibits development of a liquid temperature stratification layer and maintains a constant saturated source pressure in the tank.
- Define or modify your concept of operations (ConOps) to ensure that any sloshing is below the threshold that would cause an unacceptable drop in tank pressure. Baffles, screens, acquisition devices, or other tank internals are an option if desired slosh control cannot be achieved with the ConOps alone.
- For cavitation concerns related to draining a tank down to the warmer thermal boundary layer of the fluid, there are two options. The first is to stop flow at that liquid level. The second is to vent the tank (preferably with vapor recovery) to bring the liquid temperature down to a new saturation condition via rapid boiling.