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10
           Technoeconomic performances




           10.1   Introduction

           To further improve the RCD performance for an ASHP unit, different studies were
           conducted globally, such as heating and/or dehumidifying the inlet air of the outdoor
           coil, structure and dimension adjustments for the outdoor coil, fin type and surface
           treatment, additional defrosting energy supply with a PCM-TES system, FEC
           improvement on the surface of the outdoor coil, control strategy optimization via
           refrigerant distribution adjustment, etc. For an outdoor coil in an ASHP unit, a mul-
           ticircuit structure is usually used in order to enhance its heat transfer and minimize its
           refrigerant pressure loss. To save the floor space, the multicircuit outdoor coil is
           always vertically installed in its practical application.
              For an ASHP unit with a vertically installed multicircuit outdoor coil, it was easy to
           find the uneven defrosting phenomenon in the open literature. When the other circuit
           was waiting for the lowest circuit to terminate its defrosting process, the heat transfer
           between the hot refrigerant tube and fins and the ambient cold air would consume a lot
           of energy [1]. Not only would defrosting efficiency be degraded, but also the
           defrosting duration would be prolonged and the indoor thermal comfort level affected.
           As demonstrated by previous experimental and numerical studies, the downward
           flowing of melted frost along the surface of the outdoor coil was one of the important
           reasons for uneven defrosting [2, 3]. At the same time, a lower FEC would also affect
           RCD. It was reported that when the FEC was increased from 82.6% to 96.6%, the
           defrosting efficiency could increase from 42.0% to 48.7%. After the negative effects
           of melted frost flowing down were eliminated, the defrosting efficiency was increased
           by about 5.7% as the FEC was increased from 79.4% to 96.6%. Furthermore, it was
           proved that frosting COP was increased from 4.10 to 4.26 as the FEC was increased
           from 75.7% to 90.5% [4]. Among all the previous experimental studies, a series of
           valves was used to adjust the refrigerant distribution, according to the tube surface
           temperatures at the circuit exits.
              However, for a new technology or innovation, a technoeconomic analysis is very
           important and should always be carried out before its wide application [5–7]. The total
           cost of technoeconomic proposed new ASHP unit is increased by the additional
           investment of valves, and a longer payback period is expected. To solve this problem,
           the economy has to be improved based on the characteristics of the ASHP unit.
           Although many methods were used to improve the operating performance of an ASHP
           unit [8, 9], especially to optimize its RCD performance [10, 11], only a few studies
           with a technoeconomic analysis were reported [12]. Horton et al. gave an economic
           analysis when evaluating a high-performance cold-climate heat pump [13].As
           reported, the maximum additional cost of the system changes for the Minneapolis
           location in the United States was $430 for a vapor-injected system and $391 for an
           oil-flooded system. These estimates were based on an assumed 3-year simple payback
           Defrosting for Air Source Heat Pump. https://doi.org/10.1016/B978-0-08-102517-8.00010-2
           © 2019 Elsevier Ltd. All rights reserved.
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