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method for simultaneous drainage and süßung of natural gas

机译:天然气同时排水和吸收的方法

摘要

Simultaneous dehydration and sweetening of natural gas to produce therefrom a purified natural gas having a low dew point and a low sulfur content suitable for passage in gas transmission lines with concomitant production of hydrogen sulfide gas removed from the natural gas and production of water substantially free of impurities removed from the natural gas involving passing a solvent medium comprising a normally liquid dialkyl ether of a polyalkylene glycol ether containing 2 to 15 percent water by weight in direct contact with the natural gas to reduce its H2S content to less than 10 parts per million and its water content to less than 12 pounds per million standard cubic feet; stripping the hydrogen sulfide from the solvent medium by means of internally generated steam which is generated by externally heating stripped solvent medium; withdrawing a portion of internally generated steam containing a minor amount of solvent; condensing a portion of it together with contained solvent and returning the steam condensate and contained solvent to the stripping zone; condensing and discharging the remaining portion of withdrawn steam and returning lean solvent medium for stripping of natural gas.
机译:同时进行天然气的脱水和脱硫,从而生产出具有低露点和低硫含量的纯化天然气,适合于通过气体传输线,同时生产从天然气中去除的硫化氢气体和生产基本上不含水的水从天然气中除去的杂质,包括使溶剂介质通过,该溶剂介质包含通常为液态的聚亚烷基二醇醚的二烷基醚,其中的聚亚烷基二醇醚含有2至15重量%的水,与天然气直接接触,以将其H2S含量降至百万分之10以下;以及其水含量低于每百万标准立方英尺12磅;借助于内部产生的蒸汽从溶剂介质中汽提硫化氢,该蒸汽是通过外部加热汽提的溶剂介质而产生的;抽取一部分内部产生的含有少量溶剂的蒸汽;将其一部分与所含溶剂一起冷凝,并使蒸汽冷凝物和所含溶剂返回汽提区。冷凝并排放剩余的抽出蒸汽,并返回稀薄的溶剂介质以汽提天然气。

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