超临界R1234ze(E)在水平螺旋螺旋管内强化传热及新关联的实验研究

Yizhou Jiang, Peng Hu, Qi Chen, Cheng Jia, Pan-Pan Zhao, Lei Jia
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引用次数: 0

摘要

- HFOs制冷剂R1234ze(E)由于ODP为零,GWP极低,近年来在超临界热泵系统和超临界有机朗肯循环(ORC)中得到了广泛应用。本文对超临界HFO-1234ze(E)在水平螺旋盘管(HCT)中的冷却换热性能进行了实验研究。详细分析了质量通量(G)和压力(P)对换热系数(h)、重力浮力效应和离心浮力效应的相对比例(G c Ri / Ri)、HCT的换热增强和二次流速度(V s)分布的影响。P的增加抑制了G对h的影响,而G的增加则增强了P对h的影响。Ri / Ri随g的增大而减小,随P的增大而增大。质量通量越大,离心力对V s截面分布的影响越明显,HCT的换热强化效果越显著。当G分别为240和400 kg/m 2s时,螺旋管中s- r1234ze (E)的h比直管高12.73%和18.69%。P的变化几乎没有改变离心作用对V s分布的影响,因此对HCT的强化传热影响不大。当P分别为4.5 MPa和5 MPa时,螺旋管的h比直管高15.38%和15.12%。在T b > T pc区域,由于没有Ri c项,直线管的相关系数对螺旋管s-R1234ze(E)性能的预测偏差较大。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Experimental Investigation On Heat Transfer Enhancement And New Correlation Of Supercritical R1234ze(E) In Horizontal Helically Coiled Tube
- HFOs refrigerant R1234ze(E) has been widely applied in supercritical heat pump system and supercritical Organic Rankine Cycle (ORC) in recent years due to zero ODP and extremely low GWP. In this paper, experimental research on the cooling heat transfer performances of supercritical HFO-1234ze(E) in horizontal helically coiled tube (HCT) is performed. The impacts of mass flux ( G ) and pressure ( P ) on the heat transfer coefficient ( h ), the relative proportion of gravitational buoyancy effect and centrifugal buoyancy effect ( g c Ri / Ri ), the heat transfer enhancement of HCT and the distribution of secondary flow velocity ( V s ) are detailed analyzed. The increasing P suppresses the impact of G on h , while the increasing G strengthens the influence of P on h . g c Ri / Ri decreases with the enhancement of G , yet increases with the rising P . The higher the mass flux is, the more obvious the influence of centrifugal force on the cross-sectional distribution of V s will be, and the more significant the heat transfer enhancement of HCT will become. When G is 240 and 400 kg/m 2 s respectively, h of s-R1234ze(E) in helical tube is 12.73% and 18.69% higher than that in straight tube. The variation of P hardly changes the centrifugal effect on the distribution of V s , thus having little impact on the heat transfer enhancement of HCT. When P is 4.5 and 5 MPa respectively, h of helical tube is 15.38% and 15.12% higher than that of straight tube. In the region of T b > T pc , the correlation of straight tube has large prediction deviations for the performances of s-R1234ze(E) in helical tube owing to the absence of Ri c term.
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