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WORKING PRINCIPLE OF THE ORC The working principle of the organic Rankine cycle is the same than that of the Rankine cycle : the working fluid is pumped to a boiler where it is evaporated, passes through a turbine and is finally re-condensed. In the ideal cycle, the expansion is Isentropic and the evaporation and condensation processes are Isobaric . In the real cycle, the presence of Irreversibilities lowers the cycle Efficiency . Those irreversibilities mainly occur :
IMPROVEMENT OF THE ORGANIC RANKINE CYCLE In the case of a "wet fluid", the cycle can be improved by the use of a regenerator : Since the fluid has not reached the two-phase state at the end of the expansion, its temperature at this point is higher than the condensing temperature. This higher temperature fluid can be used to preheat the liquid before it enters the evaporator. A counter-flow Heat Exchanger is thus installed between the expander outlet and the evaporator inlet. The power required from the heat source is therefore reduced and the efficiency is increased. APPLICATIONS FOR THE ORC The possible applications for the organic Rankine cycle technology are multiple. Among them, the most widespread and promising fields are the following:
Waste heat recovery is without doubt the most important development field for the ORC. It can be applied to heat and Power Plants (for example a small scale Cogeneration plant on a domestic water heater), or to industrial and farming processes such as organic products fermentation, hot exhausts from ovens or furnaces, exhaust gases from vehicles, intercooling of a compressor, condenser of a power cycle, etc.
The organic Rankine cycle can be used in the solar Parabolic Through technology in place of of the usual steam Rankine cycle. The ORC allows a lower collector temperature, a better collecting efficiency (reduced ambient losses) and hence the possibility of reducing the size of the solar field.
Geothermic heat sources vary in temperature from 50 to 350°C. The ORC is therefore perfectly adapted for this kind of application. However, it is important to keep in mind that for low-temperature geothermal sources (typically less than 100°C), the efficiency is very low and depends strongly on heat sink temperature (defined by the ambient temperature). CHOICE OF THE WORKING FLUID The selection of the working fluid is of key importance in low temperature Rankine Cycles. Because of the low temperature, heat transfer inefficiencies are highly prejudicial. These inefficiencies depend very strongly on the thermodynamic characteristics of the fluid and on the operating conditions. In order to recover low-grade heat, the fluid generally has a lower ebullition temperature than water. Refrigerants and hydrocarbons are the two commonly used components. Optimal characteristics of the working fluid :
Since the purpose of the ORC focuses on the recovery of low grade heat power, a superheated approach like the traditional Rankine cycle is not appropriate. Therefore, a small superheating at the exhaust of the evaporator will always be preferred, which excludes "wet" fluids (that are in two-phase state at the end of the expansion). In the case of dry fluids, a regenerator should be used.
Unlike water, organic fluids usually suffer chemical deteriorations and decomposition at high temperatures. The maximum hot source temperature is thus limited by the chemical stability of the working fluid. The freezing point should of course be lower than the lowest temperature in the cycle.
A fluid with a high latent heat and density will absorb more energy from the source in the evaporator and thus reduce the required flow rate, the size of the facility, and the pump consumption.
The main parameters taken into account are the Ozone Depletion Potential (ODP) and the Global Warming Potential (GWP).
The fluid should to be non-corrosive, non-flammable, and non-toxic. The ASHRAE safety classification of refrigerants can be used as an indicator of the fluid dangerousness level.
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