Page 153 - Defrosting for Air Source Heat Pump
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146                                         Defrosting for Air Source Heat Pump


          Table 5.9 Different durations and their differences in the two cases
          Item   Parameter                  Case 1   Case 2  Difference  Unit

          1      Start of tube surface      80       80      0           s
                 temperature leaving 0°C
          2      Start of fin surface temperature  60  90     30         s
                 leaving 0°C
          3      Start of tube surface      103      105      2          s
                 temperature reaching 2°C
          4      Start of fin surface temperature  95  105    10         s
                 reaching 2°C
          5      Temperature of tube surface  6.5    8.7      2.2        °C
                 increased during 30 s
          6      Temperature of fin surface  5.5     8.2      2.7        °C
                 increased during 30 s
          7      Duration of tube surface   14       11      3           s
                 temperatures all increased from
                 20°Cto24°C
          8      Duration of fin surface    15       11      4           s
                 temperatures all increased from
                 20°Cto24°C
          9      Defrosting duration (tube  186      167     19          s
                 surface temperatures all
                 reached 24°C)
          10     Duration of fin surface    188      172     16          s
                 temperatures all reaching 24°C




         the two cases are nearly the same, which met the similar total mass of melted frost
         collected listed in Table 5.8 and even frost accumulations shown in Fig. 5.18A1
         and B1. Only there is difference on fin surface temperature, with the starts of leaving
         0°C at 60 and 90 s, and the starts of reached 2°C at 95 and 105 s, respectively. The
         difference on fin surface temperature results from the effect of the melted frost during
         defrosting. Therefore, this comparative study is meaningful.
            In addition, compared with the increased temperatures of the tube and fin surfaces
         during 30 s in Case 1, at the operation period of the melted frost being manually dra-
         ined away in Case 1, those values in Case 2 always were much higher. This shows the
         negative effects of retained melted frost due to surface tension. After cleaning the
         melted frost, the durations of the tube and fin surface temperatures that increased from
         20°Cto 24°C in Case 1 were all less than those in Case 2. This phenomenon results
         from the different masses of retained melted frost on the surface of the outdoor coil,
         which also met the mass of collected retained melted frost listed in Table 5.9. Finally,
         the length of time it took the tube and fin surface temperatures to reach 24°C in Case 1
         was less than that in Case 2. Therefore, the negative effects of surface tension were
         further demonstrated.
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