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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >An experimental investigation of phase separation of gas-liquid two-phase flow through a small break
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An experimental investigation of phase separation of gas-liquid two-phase flow through a small break

机译:气液两相流小断裂相分离的实验研究

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This paper proposes a specially designed splitting device to study the phase separation of gas-liquid two-phase flow through a small break. The inner pipe diameter of the main test section is 40 mm. A small hole with 2.5 mm diameter was drilled at the main pipe wall to simulate the break. Three break orientation angles were tested, including 0 degrees (side), -45 degrees (inclined) and -90 degrees (bottom) from horizontal orientation. Experiments were conducted in an air-water two-phase flow loop with a horizontal test section. Stratified wavy, annular and slug flows were observed. Experimental results show that phase separation is affected by the break location, flow pattern and gas and liquid superficial velocities. The fraction of liquid taken off of slug flow is observed much larger than that of stratified wavy or annular flows due to its particular flow behavior. A simplified correlation of break pressure difference is proposed in terms of break outlet mass flow rate and gas quality. (C) 2015 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:本文提出了一种专门设计的分流装置,以研究气液两相流小间隙的相分离。主测试部分的内管直径为40毫米。在主管壁上钻了一个直径为2.5 mm的小孔,以模拟断裂。测试了三个断裂取向角,包括与水平取向的0度(侧面),-45度(倾斜)和-90度(底部)。在带有水平测试部分的气水两相流回路中进行实验。观察到分层的波浪状,环形和团状流。实验结果表明,相分离受断裂位置,流型以及气体和液体表面速度的影响。观察到从团状流中取出的液体部分比分层的波浪或环形流大得多,这是由于其特殊的流动特性。根据中断出口质量流量和气体质量,提出了中断压力差的简化关联。 (C)2015化学工程师学会。由Elsevier B.V.发布。保留所有权利。

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