分层气液流动中的多重滞留平衡和水力梯度

0 ENERGY & FUELS
Peter S. Johansson , Zhilin Yang , Dominique Larrey , Roel Belt , Lan Liu
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引用次数: 0

摘要

对 2°、3° 和 2°+3° 直管配置进行了液体负荷极低的两相流升压试验。升压操作产生的液体排放过程可以用多重截留平衡来解释。在实验条件下,多重截留平衡区域一直延伸到气油体积流量比约为 1000 时。如果管道末端的滞留量足够低,则在多重滞留平衡区域内运行的管段流量将获得低滞留平衡。否则,管段的流动将获得高滞留平衡。在低液体负荷的天然气冷凝水系统中,可以通过避免上坡段末端的陡峭倾角来尽量减少液体积聚。在存在多种平衡的情况下,确保整个管道的低滞留平衡可最大限度地减少液体积聚,并降低运行条件下的最小流速限制。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Multiple holdup equilibria and hydraulic gradients in stratified gas–liquid flows
Experimental ramp-up tests for a two-phase flow with very low liquid loading have been conducted for 2°, 3° and 2° + 3° straight pipe configurations. The liquid draining process resulting from the ramp-up operation is explained by multiple holdup equilibria. For the conditions of the experiments, the multiple holdup equilibria region extends down to a gas oil volume flow rate ratio of about 1000. The flow of a pipe segment operating in the multiple holdup equilibria region will obtain the low holdup equilibrium if the holdup at the end of the pipe is sufficiently low. Otherwise, the flow of the pipe segment will obtain the high holdup equilibrium. Liquid accumulation can be minimized by avoiding steep inclination angles at the culmination of uphill sections in low liquid loading gas condensate systems. Ensuring low holdup equilibria throughout the pipeline, where multiple equilibria exist, minimizes liquid accumulation and reduces minimum flow rate limits during operating conditions.
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CiteScore
11.20
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