首页> 外国专利> A method for regasifying liquefied natural gas to use the calorify potential of the same. (Machine-translation by Google Translate, not legally binding)

A method for regasifying liquefied natural gas to use the calorify potential of the same. (Machine-translation by Google Translate, not legally binding)

机译:一种将液化天然气再气化以利用其热势的方法。 (通过Google翻译进行机器翻译,没有法律约束力)

摘要

A method for regasifying liquefied natural gas to utilize the calorific potential thereof, comprising: (a) partially evaporating said liquefied natural gas and recovering the cold potential thereof with a heat exchange medium; (b) introducing said partially evaporated natural gas into a methane separation zone, and separating therein a gaseous overhead fraction containing predominantly methane and a liquid tail fraction containing ethane and heavier components; (c) superheating said gaseous methane fraction up to the distribution temperature and recovering its cold potential with a heat exchange medium and removing said fraction as a product; (d) introducing said liquid fraction of glue into an ethane separation zone and separating therein a gaseous ethane fraction as the head and a glue fraction containing propane and any heavier components; (e) introducing said ethane fraction as feedstock into an ethylene facility; (f) supply the cooling needs of said ethylene facility with the cold potential recovered in operations (a) and (c); (g) removing as separate products from said ethylene facility an ethylene fraction and a lighter gas fraction containing substantially hydrogen, carbon monoxide, methane and the like; and (h) mixing said lighter gas fraction from operation (g) with said propane fraction from operation (d) to produce a gas having approximately the same heat value as the gas withdrawn in operation (c). (Machine-translation by Google Translate, not legally binding)
机译:一种将液化天然气再气化以利用其热势的方法,包括:(a)部分地蒸发所述液化天然气,并用热交换介质回收其冷势; (b)将所述部分蒸发的天然气引入甲烷分离区,并在其中分离出主要含有甲烷的气态塔顶馏分和含有乙烷及较重组分的液体尾馏分; (c)将所述气态甲烷馏分过热至分布温度,并用热交换介质回收其冷势,并除去作为产物的所述馏分; (d)将所述胶水的液体部分引入乙烷分离区,并在其中分离出作为头部的气态乙烷油部分和含有丙烷和任何较重组分的胶水部分; (e)将所述乙烷馏分作为原料引入乙烯设备中; (f)提供上述乙烯设施的冷却需求,并在操作(a)和(c)中回收冷势; (g)从所述乙烯设备中分离出乙烯馏分和基本上包含氢,一氧化碳,甲烷等的较轻的气体馏分作为分离的产物; (h)将操作(g)中的所述较轻的气体馏分与操作(d)中的所述丙烷馏分混合,以产生具有与操作(c)中排出的气体大致相同的热值的气体。 (通过Google翻译进行机器翻译,没有法律约束力)

著录项

  • 公开/公告号ES328242A1

    专利类型

  • 公开/公告日1967-04-01

    原文格式PDF

  • 申请/专利权人 THE LUMMUS COMPANY;

    申请/专利号ES19660328242

  • 发明设计人

    申请日1966-06-22

  • 分类号C07C7/04;C07C11/04;C10G5/06;C10K3;F17C9/04;F25J3/02;

  • 国家 ES

  • 入库时间 2022-08-23 14:23:27

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