Experimental Study on Coupling Characteristics of Refrigerant Flow Pattern-Flow Resistance and Two-Phase Pressure Drop Prediction in Horizontal Tube
|更新时间:2025-07-08
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Experimental Study on Coupling Characteristics of Refrigerant Flow Pattern-Flow Resistance and Two-Phase Pressure Drop Prediction in Horizontal Tube
Moren Journal(2025)
作者机构:
1.西安交通大学热流科学与工程教育部重点实验室,陕西省西安市710049
2.广东美的制冷设备有限公司,广东省佛山市528311
3.西安交通大学能源与动力工程学院,陕西省西安市710049
作者简介:
基金信息:
DOI:
CLC:TK124
Received:07 May 2025,
Revised:2025-06-30,
Accepted:07 July 2025,
稿件说明:
移动端阅览
WANG Jianwei, LIU Yantao, ZHOU Chenjie, et al. Experimental Study on Coupling Characteristics of Refrigerant Flow Pattern-Flow Resistance and Two-Phase Pressure Drop Prediction in Horizontal Tube[J/OL]. Moren Journal, 2025.
DOI:
WANG Jianwei, LIU Yantao, ZHOU Chenjie, et al. Experimental Study on Coupling Characteristics of Refrigerant Flow Pattern-Flow Resistance and Two-Phase Pressure Drop Prediction in Horizontal Tube[J/OL]. Moren Journal, 2025.DOI:
Experimental Study on Coupling Characteristics of Refrigerant Flow Pattern-Flow Resistance and Two-Phase Pressure Drop Prediction in Horizontal Tube
The evolution of flow patterns and flow mechanisms of low-dryness R32 and R134a refrigerants are not clear
which constrains the optimal design of high-efficiency air-conditioning systems. In this study
a visual experimental setup was established. The flow pattern distribution and pressure drop characteristics of R134a and R32 in a horizontal circular tube with 7 mm inner diameter were studied with flowrate and dryness ranging between 150~750 kg/(m
2
·s) and 0~0.2
respectively. The OpenCV image feature extraction method was used and the synchronous measurement method is established
while the evolution laws of three typical flow patterns
namely
slug flow
wave flow and annular flow
are obtained. Results show that R32 display a slug flow at low flowrate with small dryness. By increasing the dryness
the flow pattern gradually changes to wave flow with gas-liquid separation. On the other hand
R134a indicates an increased stability of the liquid film at high flowrate and high dryness
and the proportion of annular flow is incre
ased
reaching 13% which is higher than that of R32 on average. Meanwhile
the full liquid-phase friction coefficient reaches the peak at a flowrate of 360 kg/(m
2
·s)
illustrating the minimum mixing density and the maximum gas-liquid-phase velocity ratio. Note that the friction-pressure-drop gradient for R134a is 25%-50% higher than that for R32. Based on the flow pattern division strategy
the pressure drop prediction model incorporating flow pattern parameters (
C
i
) and dimensionless numbers (
Fr
,
We
,
Re
tp
) is proposed. The absolute deviation can be rapidly reduced from -30~-70% to 12.31% compared with existed models
while 89% of the data locating within ±20% error band. Results could provide good theoretical support to their figurant system design.
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