06.03.2013 Views

buletinul institutului politehnic din iaşi - Universitatea Tehnică ...

buletinul institutului politehnic din iaşi - Universitatea Tehnică ...

buletinul institutului politehnic din iaşi - Universitatea Tehnică ...

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

Bul. Inst. Polit. Iaşi, t. LVIII (LXII), f. 4, 2012 37<br />

Fig. 1 – Schematic representation of refrigeration system: where: T1 – refrigerant<br />

temperature at suction compressor, ºC; T2 – refrigerant temperature at discharge<br />

compressor, ºC; T3 refrigerant temperature at condenser inlet, ºC; T4 – refrigerant<br />

temperature at condenser outlet, ºC; T5 – air temperature at inlet evaporator 1, ºC; T6 –<br />

air temperature at outlet evaporator 1, ºC; T7 – refrigerant temperature at discharge of<br />

evaporator 1, ºC; T8 – air temperature at inlet evaporator 2, ºC; T9 – air temperature at<br />

outlet evaporator 2, ºC; T10 – refrigerant temperature at discharge of evaporator 2, ºC;<br />

T11 – air temperature at condenser inlet, ºC; T12 – air temperature at condenser<br />

outlet, ºC.<br />

2.1. Calculation of the Theoretical Eco-efficiency Parameters<br />

The theoretical eco-efficiency parameters discussed in this paper are: the<br />

performance coefficient, annual energy consumption and TEWI factor. For<br />

fin<strong>din</strong>g the eco-efficiency parameters, classic thermodynamics relations<br />

together with parameters defined in Table 1 were used (Ţârlea et al., 2010).<br />

i) Fin<strong>din</strong>g the performance coefficient<br />

First of all was calculated the refrigerant mass flow by<br />

0 M&<br />

Φ<br />

= ,<br />

Δh<br />

(1)<br />

ev

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!