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Additionally, the impact of different working fluid charge volumes has also been discussed.
The present paper developed a working fluid charge oriented model for an small scale Organic Rankine Cycle to calculate the theoretical value of working fluid charge level for the system under rated condition.
For a fluid charge of 100 ml the same fluid never left the evaporator in all tests performed with rotation of the magnetic stirrer.
Furthermore, the highest thermal efficiency can be reached 6.37% under rated conditions with a working fluid charge volume of 34.6 kg.
The present study focused on improving the thermal performance of CO2 evaporators while reducing their volume and thus significantly reducing the working fluid charge.
The key roles played by both fluid charge and ambient temperature are carefully addressed, so while lower mass charge is preferable for small loads, at the same power, the operating temperature is nevertheless higher for lower ambient temperatures.
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A sintered two-layer 100 + 200 mesh wick was adopted, and the volumetric fluid charges were the same.
The outdoor tested parameters were the effect of RH, DBT, type of working fluid charged in THEs (Water, Methanol, Ethanol, Acetone, Butanol and R134a) and the air velocity.
Regenerators operate periodically and feature a loading phase during which hot fluid charges the device and an unloading phase during which the heat is transferred to a cooler fluid.
Hanging wall closure is most often sealing and, therefore, retains significant columns of hydrocarbon, often leading to high minimum effective stress and fluid charging.
When combined with the regional buried history, the early-stage fluids charged from 422 Ma to 412 Ma BP, and the late-stage fluids charged from 20 Ma to 6 Ma BP.
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