Page 185 - Defrosting for Air Source Heat Pump
P. 185

Frosting evenness coefficient                                     179


















           Fig. 6.26 Airside surface conditions of the outdoor coil at the start of defrosting operations in
           the three cases. (A) Case 1, (B) Case 2, (C) Case 3.


           exploring and concluding the defrosting performance of an ASHP unit with a verti-
           cally installed multicircuit outdoor coil when its defrosting operation starts at different
           FECs is meaningful and fundamental. As shown in Fig. 6.26, the water-collecting
           trays are installed between circuits, which take the melted frost away during
           defrosting, leading to the negative effects of downward-flowing melted frost being
           eliminated.
              As shown in Table 6.5, the results of the three experimental cases are listed
           in detail. The total mass of frost accumulated was weighed at 1000 g in Case 1,
           1052 g in Case 2, and 969 g in Case 3, respectively. The three values are nearly
           the same, with the biggest difference of 83 g, or around 7.9% (<10%), which makes
           the comparative study and the experimental results meaningful. In addition, in Case 1,
           the masses of frost accumulated on each circuit’s surface were weighed at 374 g for
           Circuit 1, 329 g for Circuit 2, and 297 g for Circuit 3, respectively. The FEC was cal-
           culated at about 79.4%. In Case 2, the frost accumulations from Circuit 1 to Circuit 3
           were weighed at 330, 362, and 360 g, respectively. The FEC was calculated at about
           91.2%, which was about 12.8% higher than that in Case 1. As to Case 3, from Circuit 1
           to Circuit 3, the frost accumulations were weighed at 317, 328, and 324 g, respec-
           tively. The FEC in Case 3 was calculated at about 96.6%, or 17.2% higher than that
           in Case 1.
              Moreover, the measured operating performances of the experimental ASHP unit
           during defrosting, corresponding to the three experimental cases, are presented in
           Figs. 6.27–6.38. Figs. 6.27–6.33 present the measured tube surface temperatures at
           the exits of the three refrigerant circuits, and the fin surface temperature at the center
           of the three refrigerant circuits during defrosting. In all these figures, for their time
           (horizontal) axis, 80 s is the chosen starting time in order to clearly show the temper-
           ature rise during defrosting. Figs. 6.34 and 6.37 show the measured temperature of the
           surrounding air and the measured temperature of the melted frost collected
           in the three cylinders during defrosting in the three cases. Finally, a variation of
           the measured refrigerant volumetric flow rate during defrosting in the three cases
           is shown in Fig. 6.38.
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