从天然气凝析液中分离天然气液体和水

Matthew Efe Takerhi
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引用次数: 1

摘要

与干气储层不同,凝析气藏含有相当数量的天然气液体,应将其提取以最大限度地利用能源。本文采用Bryan ProMax建立了天然气液回收和脱水处理装置。模拟的参数是假设含硫气体的气体成分。模拟的结果包括将水含量降至7磅/立方英尺以下,回收甲烷,只回收丙烷和异丁烷。乙二醇脱水装置最大限度地减少了水的杂质,而焦耳-汤姆逊阀和热交换器的冷却有助于甲烷的回收和天然气液体的分离。结果表明,通过控制换热器、闪蒸器、冷分离器、分馏器、稳定器及其再沸器和冷凝器等装置的工况,可以实现天然气液的回收,而天然气液的回收取决于气体成分。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Separation of natural gas liquids and water from gas condensate
Unlike dry gas reservoirs, condensate gas reservoirs contain a considerable amount of natural gas liquids which should be extracted to maximize energy usage. This paper uses Bryan ProMax to set up the processing units for the recovery of natural gas liquids and removal of water. The parameters for the simulation were a gas composition which assumes a sweet gas content. The outcome of the simulation includes reduction of water content below 7 lbm/MMscf, recovery of methane and recovery of propane and isobutane only. The glycol dehydration unit minimized water impurity, while cooling with Joule–Thomson valve and heat exchangers help in methane recovery and separation from natural gas liquids. The results show that natural gas liquid recovery which depends on gas composition can be recovered by controlling the conditions of several units, namely heat exchangers, flash vessels, cold separators, fractionators, stabilizers with their reboilers and condensers. 
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