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Liquefaction of natural gas at supercritical pressure employing a single refrigeration cycle

机译:采用单个制冷循环的超临界压力天然气液化

摘要

1,105,374. Gas liquefication processes. LUMMUS CO. 16 Feb., 1966 [18 Feb., 1965], No. 6788/66. Addition to 1,016,049. Heading F4P. Liquefaction of a hydrocarbon gas, e.g. natural methane, is effected by compressing at 13SP1/SP feed gas to a pressure between 40 atoms. and about 1À5 times its critical pressure, cooling by indirect heat exchange at 18SP1/SP, 19SP1/SP with an expanded refrigerant, e.g. propylene, liquefying by indirect heat exchange at 20SP1/SP, 21SP1/SP with a further expanded refrigerant, e.g. ethylene, expanding at a valve 96 into a drum 95, withdrawing condensate therefrom and sequentially, expanding at valves 29SP1/SP, 33SP1/SP, 37SP1/SP into flash drums 30SP1/SP, 34SP1/SP, 38SP1/SP withdrawing product liquefied gas from drum 38SP1/SP at about atmospheric pressure and feeding it to a storage container 43SP1/SP. Gaseous overheads withdrawn from drums 95, 30SP1/SP, 34SP1/SP, 38SP1/SP are compressed at 461 and recycled to the outlet of compressor 13SP1/SP at a point either up or downstream of heat exchanger 18SP1/SP. A portion of gaseous overhead from drum 95 is withdrawn as fuel gas.
机译:1,105,374。气体液化过程。 LUMMUS CO.1966年2月16日[1965年2月18日],编号6788/66。除1,016,049。标题F4P。烃气的液化,例如天然甲烷是通过在13 1 进料气中压缩至40个原子之间的压力来实现的。并在其临界压力的约1‑5倍下,通过膨胀的制冷剂(例如)在18 1 ,19 1 之间进行间接热交换进行冷却。丙烯,通过与20 1 ,21 1 的间接热交换与进一步膨胀的制冷剂(例如乙烯,在阀96处膨胀成鼓状95,从中抽出冷凝水,然后依次在阀29 1 ,33 1 ,37 1 处膨胀进入闪蒸罐30 1 ,34 1 ,38 1 大约在大气压下从圆筒38 1 抽出产品液化气加压并将其送入存储容器43 1 。从转鼓95、30 1 ,34 1 ,38 1 排出的气态塔顶馏分在461压缩并循环到压缩机13 1 在热交换器18 1 的上方或下游。来自鼓95的塔顶气体的一部分作为燃料气体被抽出。

著录项

  • 公开/公告号US3413817A

    专利类型

  • 公开/公告日1968-12-03

    原文格式PDF

  • 申请/专利权人 THE LUMMUS COMPANY;

    申请/专利号US19670651587

  • 发明设计人 KNIEL LUDWIG;

    申请日1967-07-06

  • 分类号F25J1/02;F25J3/02;

  • 国家 US

  • 入库时间 2022-08-23 11:48:01

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