Page 221 - Defrosting for Air Source Heat Pump
P. 221

The influence of refrigerant distribution on defrosting           215

           melting stage consumed a lot of energy, with a lot of refrigerant changing phases from
           gas to liquid or a two-phase state. This might be the reason why the measured refrig-
           erant mass flow rate kept fluctuating severely from 0 to 74 s, especially during the first
           50 s into defrosting. When the defrosting process came into the water layer vaporizing
           stage described in Chapter 4, the compressor suction and discharge pressures
           increased, with the refrigerant volumetric flow rate changing from increasing to
           decreasing. As shown in Fig. 7.20, their peak values nearly both came out at 160 s
           into defrosting in the two cases. From 74 to 152 s, the refrigerant volumetric flow rate
           order of the two cases was at R 2 > R 1 . The peak value in Case 2 was slightly lower
           than that in Case 1. It is demonstrated that the defrosting operation in Case 2 was
           terminated a little quicker. For an ASHP unit with a vertically installed multicircuit
           outdoor coil, this is more proof to demonstrate the negative coupled effects of MFDF
           and URD on defrosting performance.
              Fig. 7.21 shows the variation of the measured temperatures of the surrounding air
           and the melted frost collected in the water-collecting Cylinder C in the two cases.
           Because there were no water-collecting trays installed between circuits, the melted
           frost collected in this cylinder was much more than that collected with trays installed
           between circuits, at 875 g for Case 1 and 872 g for Case 2, as listed in Table 7.4.
           Clearly, there were two suddenly decreasing points that existed in the two curves,
           at 120 s into defrosting for Case 1 and at 115 s into defrosting for Case 2. This means
           the frost was melted and flowed into the water-collecting Cylinder C, and the temper-
           ature of the melted frost was measured. Before the water was collected, during 0–120 s
           for Case 1 and 0–115 s for Case 2, the temperature of the coil surrounding the air was
           measured. It was about 5 s earlier in Case 2 than that in Case 1. This phenomenon



                       7
                                Case 1
                       6
                                Case 2
                       5
                      Temperature ( o C)  4 3  T  > T 2  T  > T  1



                                           2
                          1
                               T    T               T  > T
                       2        1  2                 2  1

                       1            60 s  90 s
                               26 s
                         0    40     80    120   160   200   240    280
                                            Time (s)

           Fig. 7.21 Measured temperatures of the surrounding air and melted frost collected during
           defrosting.
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