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Raw natural gas pretreatment prior to liquefaction - by removing acid gases, drying, expanding, scrubbing and fractionating to give methane, ethane and propane

机译:液化前的原始天然气预处理-通过除去酸性气体,干燥,膨胀,洗涤和分馏得到甲烷,乙烷和丙烷

摘要

Raw natural gas at 800 psig is pretreated prior to liquefaction by a process comprising (a) passing the stream to a sweetening zone for removal of acid gases (CO2 and H2S), (b) passing the stream to a first drying zone to form a dry gas stream having a dew point of -20 degrees F, (c) expanding the stream in an energy recovery means (developing shaft horsepower) to 300 psig, (d) scrubbing the stream with a lean hydrocarbon liq. to remove from it all 2C hydrocarbon and form a CH4-rich gas stream (I) and a rich liq. hydrocarbon stream (II), (e) passing (I) to a solid desiccant drying zone to form a dry gas stream having a dew point of -240 degrees F, (f) fractionating (II) to separate streams rich in methane, ethane and propane respectively and obtain a =4C liq. hydrocarbon stream (III), and (g) dividing (III) into two portions and passing one portion as the lean hydrocarbon liq. to the scrubbing zone in step (d). Liquefaction refrigeration power requirements are reduced by utilising the energy recovered in expanding the raw gas. The volume of gas which must be dried in expensive desiccant beds prior to liquefaction is reduced.
机译:在液化之前,采用以下方法对> 800 psig的粗天然气进行预处理:(a)使气流进入脱硫区,以除去酸性气体(CO2和H2S);(b)使气流进入第一干燥区以形成露点为-20华氏度的干燥气流,(c)在能量回收装置中将气流膨胀(产生竖井马力)至300 psig,(d)用贫烃液洗涤气流。从中除去所有> 2C的烃,并形成富含CH4的气流(I)和浓液。烃物流(II),(e)使(I)进入固体干燥剂干燥区以形成露点为-240华氏度的干燥气流,(f)分馏(II)以分离出富含甲烷,乙烷的物流和丙烷分别得到≥4C的液体。烃料流(III),和(g)将(III)分成两部分,并作为贫烃液体通过一部份。进入步骤(d)中的洗涤区。通过利用在膨胀原料气中回收的能量来降低液化制冷功率的需求。减少了液化之前必须在昂贵的干燥剂床中干燥的气体量。

著录项

  • 公开/公告号FR2414947A1

    专利类型

  • 公开/公告日1979-08-17

    原文格式PDF

  • 申请/专利权人 UOP INC;

    申请/专利号FR19780001510

  • 发明设计人

    申请日1978-01-19

  • 分类号B01D53/00;C07C7/01;C07C9/02;F25J3/08;

  • 国家 FR

  • 入库时间 2022-08-22 19:31:17

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