A mathematic model of the scroll expander in the low-temperature waste heat recovery system using R123 as working fluid was established and the effects of suction and discharge
leakage
and heat transfer on its working process were analyzed. The results show that the actual process is different from the theoretic one because of the pressure loss in the suction and discharge processes and the leakage and heat transfer in the entire process. The working fluid mass in the expansion chamber is less than the theoretic value after the suction process
and it decreases at the beginning of expansion and then increases. The actual delivery and power output increase but their increments decrease with the increase of the rotational speed. The volumetric efficiency increases with the rotational speed. In addition
the volumetric efficiency may be enhanced by reducing theradial clearance and axial clearance.
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references
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