Page 82 - Defrosting for Air Source Heat Pump
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74                                          Defrosting for Air Source Heat Pump


          Table 4.1 Two semiempirical models
          Item   Parameter                       Model 1        Model 2

          1      Number of water-collecting trays  1 (Tray C)   3 (Trays A, B, C)
                 installed
          2      Positions of water-collecting trays  Under Circuit 3  Under each
                                                                circuit
          3      Results shown in                Figs. 4.6 and  Figs. 4.8–4.11
                                                 4.7



         tailor-made three-circuit outdoor coil surface was divided into three control volumes,
         respectively, corresponding to the three circuits shown in Fig. 4.1. For each control
         volume, a lumped parameter modeling approach was applied.
            In this section, unlike the models developed in previous studies [11,12,22],
         a defrosting process on the airside of the outdoor coil was chronologically divided
         into four stages: (1) preheating, (2) frost melting without water flowing away from
         a circuit, (3) frost melting with water flowing away from a circuit, and (4) water
         layer vaporizing. Such a way of staging a defrosting process could enable a proper
         account for the flow of the melted frost into, or away from, a control volume
         according to the use of water-collecting trays in the experimental three-circuit
         outdoor coil.
            Under the assumption of four stages of defrosting, a defrosting process began with
         preheating. In this stage, all the melted frost could be held on the finned coil surface
         due to surface tension. When the frost in direct contact with the surface of the tubes
         and fins was melted, a thin water layer was formed. At the end of the first stage, the
         thin water layer covered the entire airside surface of the outdoor coil. However,
         the water layer was not in contact with the ambient air within the entire first stage.
         In the second stage, as the heat was transferred from the warmer water layer to the
         frost, the thickness of the frost layer was decreased and that of the water layer
         increased so that the water layer started to be in contact with the low-temperature
         ambient air. However, there was no melted frost flowing away from a circuit, as
         the mass of the melted frost held did not reach its maximum that could be held by
         surface tension [12]. The third stage began with the start of downward flowing of
         the melted frost, as the force of gravity was larger than the surface tension. In Model
         1, the melted frost flowed downward from an up-control volume into a down-control
         volume due to gravity during this stage. However, in Model 2, the melted frost did
         flow out of a control volume but did not flow into a down-control volume as it
         was taken away by the water-collecting trays installed between the circuits, and
         was then collected by the respective cylinders. Finally, at the beginning of the fourth
         stage, or the water layer vaporizing stage, the entire outdoor coil surface was free of
         frost but covered by the retained water. When the tube surface temperature at the exit
         of the lowest refrigerant circuit (Circuit 3 in this section) in the outdoor coil reached
         24°C [7,9,22], defrosting was terminated.
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