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Bul. Inst. Polit. Iaşi, t. LVIII (LXII), f. 4, 2012 301<br />

where Δhev<br />

is enthalpy difference at evaporation working condition [kJ/kg]; M<br />

is the refrigerant mass flow rate [kg/s].<br />

Secondly, the mechanical power for the compressor was found, by<br />

(2)<br />

,<br />

W& = M& Δh<br />

cp cp<br />

where: Wcp is the mechanical power [kW];<br />

&<br />

compression working conditions [kJ/kg].<br />

Δ hcp<br />

is the enthalpy difference at<br />

Finally, the results of the coefficient of performance (COP) by<br />

Φ0<br />

COP = .<br />

W&<br />

Fin<strong>din</strong>g the annual energy consumption:<br />

The annual energy consumption (Eannual) is calculated accor<strong>din</strong>g SR EN<br />

378-1 by<br />

E = n n P<br />

(4)<br />

cp<br />

annual hours days e.<br />

Fin<strong>din</strong>g the TEWI factor<br />

The TEWI factor is calculated by SR EN 378-1 by<br />

TEWI = GWP ⋅ Ln + GWP ⋅m1− α + n E β (5)<br />

( )<br />

years rec years annual<br />

where: GWP – global warming potential [-]; L – refrigerant leak during a year<br />

working [kg].<br />

Table 2 shows the global warming and ozone depletion potential values<br />

for analysed refrigerants (Ţârlea et al., 2011).<br />

Table 2<br />

Global warming and ozone depletion potential values<br />

Refrigerant GWP ODP<br />

R404A 3260 0<br />

R717 0 0<br />

R507A 3300 0<br />

(3)<br />

L= mscm. (6)<br />

3. Theoretical Eco-Efficiency Study Results<br />

The theoretical results are presented in the next lines by tables and<br />

figures. Table 3 shows the study results for the coefficient of performance,<br />

annual energy consumption and TEWI factor (Zabet & Ţârlea, 2011).<br />

As it is shown in Fig. 2, the electrical power for R717 refrigerant is 15%<br />

smaller than R404A and R507A and this electrical power savings has a great<br />

impact over the environment pollution and maintenance cost.

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