{"id":1984,"date":"2025-11-08T16:41:25","date_gmt":"2025-11-08T15:41:25","guid":{"rendered":"https:\/\/lth2power.com\/requirements-for-a-tlc-heat-engine\/"},"modified":"2026-06-16T09:33:23","modified_gmt":"2026-06-16T07:33:23","slug":"requirements-for-a-tlc-heat-engine","status":"publish","type":"page","link":"https:\/\/lth2power.com\/en\/requirements-for-a-tlc-heat-engine\/","title":{"rendered":"Requirements for a TLC Heat Engine"},"content":{"rendered":"\n

Steam vs. Evaporation – The Essential Difference<\/strong>
In known heat engine processes (steam power process, ORC process, Stirling process, Kalina process, …), the working medium (gas, steam) passes through the heat engine without changing its state of aggregation<\/strong>.
In contrast, the conversion of thermal energy in the TLC process is based on steam generation through flash evaporation <\/strong>of the hot working medium within the heat engine<\/strong>. This results in a temporal and spatial coexistence of steam and liquid in changing proportions<\/strong>.
For context:
In turbines and engines for steam power or ORC processes, a maximum liquid content of 5-10% in the steam is tolerated. Higher proportions pose a risk of surface damage due to droplet erosion<\/mark><\/a><\/strong>.
<\/em>Since the working medium in the TLC process is 100% liquid at the beginning of flash evaporation, there is an additional risk of surface damage due to cavitation<\/mark><\/a><\/strong>.<\/p>\n\n\n\n

Flash Evaporation in Detail<\/strong>
In the TLC process, the warm, completely liquid working medium is under high pressure at the beginning of flash evaporation, which prevents boiling and thus evaporation.
Only a reduction of this pressure to values below the current boiling pressure initiates the flash evaporation process.
Due to the decreasing pressure
\u2013 the warm, liquid working medium falls below its boiling limit
\u2013 the working medium begins to boil and steam forms
\u2013 the newly formed steam increases the volume (under the current pressure)
\u2013 this reduces the temperature of the remaining liquid part of the working medium by extracting heat of vaporization
Already existing steam continues to expand (with cooling) due to the decreasing pressure, further increasing the volume.<\/p>\n\n\n\n

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This cycle, beginning with a reduction in current pressure, steam formation, and volume increase, repeats continuously and only ends when the minimum temperature, the condensation temperature, determined by the temperature of the external heat sink, is reached.<\/p>\n\n\n\n

A Rarely Considered Parameter: Time<\/strong>
In known heat engine processes (ORC, Stirling, Kalina), where there is only a pressure reduction of the gaseous or vaporous working medium, the time required for pressure reduction is a subordinate parameter of the flow velocity.

This is different in the TLC process.
Flash evaporation<\/strong>, i.e., the continuous formation of new steam bubbles from the warm liquid working medium under continuously decreasing pressure, is a temporal process<\/strong>. A rapid pressure reduction therefore leads to conversion losses.<\/p>\n\n\n\n

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This means that for the most complete conversion of absorbed thermal energy<\/strong> into mechanical energy, the temporal course of flash evaporation is an important parameter<\/strong>. Only in this way a maximum of converted thermal energy through flash evaporation can be reached.<\/p>\n\n\n\n

The Perfect TLC Heat Engine – an All-Rounder
<\/strong>From a technical perspective, a TLC heat engine must simultaneously:
– continuously and slowly reduce the operating pressure<\/strong> to initiate the continuous flash evaporation of the warm working medium
– continuously increase the volume of the working space<\/strong> for the newly generated working medium steam or the expansion of the already existing working medium steam
– convert the expansion work performed<\/strong> by the volume increase into mechanical energy<\/strong> (= motion)<\/p>\n\n\n\n

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This cycle occurs with
– simultaneous coexistence of liquid and vaporous working medium<\/strong>
– starting with 100% liquid <\/strong>at the beginning of flash evaporation
– high pressure differences to be reduced <\/strong>of up to 40 bar
– a large volume increase<\/strong> up to 300 times the original liquid volume

The continuous volume increase, under the respective current, decreasing pressure, corresponds to the thermal energy converted into mechanical energy, which must be absorbed by the heat engine and converted into a mechanical motion (e.g., rotation).<\/p>\n\n\n\n

Summary<\/strong>
The TLC process places high demands on a suitable heat engine.
In addition to process-related parameters such as the continuous and slow reduction of operating pressure, the coexistence of liquid and steam, and the large volumetric expansion ratio, there are technical challenges such as avoiding droplet erosion and cavitation.

An analysis of the aforementioned requirements and problems led to the realization that for energy generation according to the TLC process, novel heat engines are required<\/strong> which, similar to engines for the Stirling process<\/mark><\/a><\/strong>, are adapted to the specific requirements of flash evaporation<\/strong>.
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