One-dimensional analysis of the convergent-divergent motive nozzle for the two-phase ejector: Effect of the operating and design parameters

被引:10
作者
Atmaca, Ayse Ugurcan [1 ]
Erek, Aytunc [1 ]
Ekren, Orhan [2 ]
机构
[1] Dokuz Eylul Univ, Fac Engn, Mech Engn Dept, Tinaztepe Yerlekesi, TR-35390 Izmir, Turkey
[2] Ege Univ, Solar Energy Inst EVKA 3, TR-35100 Izmir, Turkey
关键词
Ejector expansion refrigeration cycle; Two-phase ejector; Motive (primary) nozzle; Converging-diverging nozzle; One-dimensional (1-D) modelling; Homogeneous equilibrium model (HEM); VAPOR COMPRESSION REFRIGERATION; COMPUTATIONAL MODEL; CFD SIMULATION; STEAM EJECTOR; R744; EJECTOR; PERFORMANCE; CYCLE; FLOW; R134A; CO2;
D O I
10.1016/j.applthermaleng.2020.115866
中图分类号
O414.1 [热力学];
学科分类号
摘要
Two-phase ejectors are used in the refrigeration cycles to decrease the throttling losses and improve the performance. The subject of this paper is the motive nozzle which is the critical component of the ejector since the pressure distribution throughout the motive nozzle affects the secondary fluid to be entrained into the ejector. A simplified version of the one of the previously established one-dimensional (1-D) converging-diverging motive nozzle models is developed in this paper to calculate the pressure, temperature, velocity, and Mach number distributions. 1-D model of the nozzle is established based on the conservation equations of mass, momentum, and energy and the equation of state under steady, frictional, and adiabatic flow assumptions with the homogeneous equilibrium condition. Maximum differences of the pressure drop throughout the nozzle between the literature data and the calculated results are around 6% and 8% for CO2 and R134a nozzles, respectively. The main objective is investigating the effects of the subcooling temperature difference, inlet pressure (condenser temperature or pressure), mass flow rate, and motive nozzle outlet diameter for R134a, R1234yf, and R1234ze (E). Parametric comparisons and evaluations are used to lead the motive nozzle designs for the further numerical and experimental studies including these new generation refrigerants for R134a replacement.
引用
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页数:15
相关论文
共 37 条
[1]  
Angielczyk W., 2010, INT REFRIGERATION AI
[2]  
ANSI/ASHRAE, 2010, ANSI/ASHRAEStandard 34-2010
[3]   Impact of the mixing theories on the performance of ejector expansion refrigeration cycles for environmentally-friendly refrigerants [J].
Atmaca, Aye Ugurcan ;
Erek, Aytunc ;
Ekren, Orhan .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2019, 97 :211-225
[4]   Effective property models for homogeneous two-phase flows [J].
Awad, M. M. ;
Muzychka, Y. S. .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2008, 33 (01) :106-113
[5]   Hydrodynamic characteristics of gas-liquid ejectors [J].
Balamurugan, S. ;
Gaikar, V. G. ;
Patwardhan, A. W. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2006, 84 (A12) :1166-1179
[6]   1D Computational model of a two-phase R744 ejector for expansion work recovery [J].
Banasiak, Krzysztof ;
Hafner, Armin .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2011, 50 (11) :2235-2247
[7]   Performance improvement of the vapour compression refrigeration cycle by a two-phase constant area ejector [J].
Bilir, Nagihan ;
Ersoy, H. Kursad .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2009, 33 (05) :469-480
[8]   Effect of throat diameters of the ejector on the performance of the refrigeration cycle using a two-phase ejector as an expansion device [J].
Chaiwongsa, Praitoon ;
Wongwises, Somchai .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2007, 30 (04) :601-608
[9]  
CHURCHILL SW, 1977, CHEM ENG-NEW YORK, V84, P91
[10]   Particular characteristics of transcritical CO2 refrigeration cycle with an ejector [J].
Deng, Jian-qiang ;
Jiang, Pei-xue ;
Lu, Tao ;
Lu, Wei .
APPLIED THERMAL ENGINEERING, 2007, 27 (2-3) :381-388