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buletinul institutului politehnic din iaşi - Universitatea Tehnică ...

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Bul. Inst. Polit. Iaşi, t. LVIII (LXII), f. 4, 2012 53<br />

system efficiencies should be expected to be equal to, or higher than, those of<br />

R404a, R717, and R134a systems. The risks represented by the flammability of<br />

the hydrocarbons must be seriously taken into account. The risks can be reduced<br />

by designing the systems for a minimum charge of refrigerant, careful leak<br />

detection during production, hermetic design with a minimum number of<br />

connections, the use of spark-proof electric components and ventilation of<br />

confined spaces.<br />

Fig. 1 – Representation of refrigerant cycle for a zeotropic refrigerant.<br />

The following matters are taken into account in this multicriteria analysis:<br />

1.COP - coefficient of performance: refrigerants with a high critical<br />

temperature give the best COP; the natural refrigerants are superior in this<br />

respect.<br />

2. qk: in HP cycles involving condensation, a refrigerant must be chosen<br />

so that this change of state will occur at a temperature somewhat below the<br />

critical temperature;<br />

3. q0: since the evaporation of the liquid is the only step in the HP cycle<br />

which produces heating, the latent heat of a refrigerant should be as high as<br />

possible. Considering condensation and evaporation, ammonia (R717) is a<br />

better heat conductor, compared with the synthetic refrigerants.<br />

4. V - swept volume flow: compressors are often some of the most critical<br />

and expensive systems at a production facility, and deserve special attention.<br />

5. W - compressor work: for the efficiency of the process the compressor<br />

work is also of interest. The compressor work of isentropic compression from<br />

the temperature of 0°C to 70°C, 60°C, 52°C, 45°C to the condensing<br />

temperature, is given for the different fluids.

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