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Modeling of annular and intermittent flow condensation in micro- and mini- channels with experimental validation

机译:实验验证的微型和迷你通道的环形与间歇流动凝结的建模

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摘要

Mechanistic models for predicting condensation heat transfer in the annular and intermittent flow regimes are presented and compared with data for different working fluids (R134a and R245fa) over a range of mass fluxes, saturation temperatures (30 ≤ T_(sat) ≤ 50 °C), saturation-to-wall temperature differences (1.5 < △T < 2.5 K), and channel geometries. The annular flow model is based on a laminar assumption and is applicable to arbitrarily shaped micro- or minichannels. Model predictions are validated using experiments focusing on low mass fluxes (G ≤ 100 kg m~(-2) s~(-1)), for which there are few analytical models or experimental data. The intermittent model developed here is also validated based on similar experiments. The annular model is found to be applicable for G ≤ 100 kg m~(-2) s~(-1), Re_δ < 61 (square), and Re_δ < 125 (circular), while the intermittent model is applicable for G ≤ 150 kg m~(-2) s~(-1) and 78 < Re_δ < 365.
机译:提出了用于预测环形和间歇性流动制度的冷凝传热的机械模型,并与不同工作流体(R134A和R245FA)的数据进行比较,在一系列质量通量范围内,饱和温度(30≤T_(SAT)≤50°C) ,饱和到壁温差(1.5 <△T<2.5 k)和通道几何形状。 环形流量模型基于层状假设,并且适用于任意形状的微观或迷你录。 使用专注于低质量通量的实验(G≤100kgm〜(-2)S〜(-1)),验证模型预测(G≤100kgm〜(-1)),分析模型或实验数据很少。 这里开发的间歇模型也基于类似的实验验证。 环形模型可用于G≤100kgm〜(-2)s〜(-1),re_Δ<61(正方形)和re_Δ<125(圆形),而间歇模型适用于g≤ 150 kg m〜(-2)s〜(-1)和78

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