Page 156 - Defrosting for Air Source Heat Pump
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Investigation of effect on uneven defrosting performance          149

           their durations at the ratio of 10.2% and 8.6%, respectively. (3) Experimental results
           show that the total energy used for defrosting was 697.9 kJ in Case 1, but 526.0 kJ in
           Case 2, or 24.6% less. Total energy consumption for defrosting for the two cases was
           344.4 kJ and 323.0 kJ, respectively, or a 6.2% difference. Most energy came from the
           indoor air, and was used on melting frost. Their defrosting efficiencies were calculated
           at 49.4% and 61.4%, with about 12.0% higher in Case 2. (4) As shown in Fig. 5.15A,
           for a vertical three-circuit outdoor coil with separations to install water-collecting
           trays, the total area of the downside surface of the outdoor coil is three times the area
           of Side B, or about 0.264 times the area of Side C shown in Fig. 5.15D. It means that
           the defrosting efficiency could be improved by about 0.264   12.0%, or 3.2%, when
           the remaining melted frost at the downside of each circuit was drained away during
           RCD. (5) For an ASHP unit with a vertical three-circuit outdoor coil, installing water-
           collecting trays between circuits could improve the defrosting efficiency from 43.5%
           to 56.7%, or about 13.2% [11]. Consequently, for an ASHP unit with a vertically
           installed three-circuit outdoor coil, the defrosting efficiency is supposed to be
           improved about 16.4% after downward-flowing melted frost is locally drained by
           water-collecting trays installed between circuits and the remaining water is cleaned
           off by destroying the surface tension.




           5.4   Concluding remarks

           In this chapter, the following conclusions could be reached. (1) The uneven defrosting
           phenomenon could be eliminated by horizontally installing a multicircuit outdoor coil.
           After the uneven defrosting was avoided, the defrosting performance of the ASHP unit
           would be improved with less energy consumption and a shortened defrosting duration.
           (2) It was experimentally demonstrated that the residual water retained on the
           downside of the circuit due to surface tension would have negative effects on
           defrosting performance for an ASHP unit. After the residual water was wiped off man-
           ually, the optimization of the defrosting performance was quantitatively investigated.
           (3) After installing horizontally a vertically installed multicircuit outdoor coil, the
           uneven defrosting problem was alleviated. However, before we consider this modifi-
           cation, the frosting or heating performance of the ASHP unit should be further tested.
           This is because the defrosting period accounts for a smaller proportion of time in a
           frosting-defrosting cycle. (4) As mentioned in Chapter 2, after the circuit number
           was increased from a two circuit to a three circuit for a multicircuit outdoor coil in
           an ASHP unit, the negative effects of the melted frost were increased due to a larger
           increase of defrosting efficiency after the water-collecting trays were installed. How-
           ever, the number of circuits is always limited by the dimension of the structure of an
           outdoor coil. Here, the negative effects of the residual water retained on the downside
           of the circuit due to surface tension also limits the number of circuits for an outdoor
           coil having a fixed heat exchanger area.
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