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Method of production of ethylene at the basis of liquefied natural gas containing methane and heavier hydrocarbons with regasifying the liquefied natural gas

机译:在含有甲烷和重烃的液化天然气的基础上,通过对液化天然气进行再气化生产乙烯的方法

摘要

Vaporized methane, and ethylene are obtained from liquefied natural gas containing methane and heavier hydrocarbons by fractionating in a first demethanizer to obtain vaporous methane overhead and a heavier hydrocarbon bottoms, cracking the latter to produce a gas mixture containing methane and ethylene, separating the methane in a second demethanizer and passing the liquefied natural gas before fractionation through a heat exchanger to condense reflux for the second demethanizer and subsequently through a heat exchanger to condense reflux for the first demethanizer. Liquefied natural gas from store 10 is pumped by line 11 through heat exchangers 12, 13, 14, 15, 16 and 17 to first demethanizer 20. Vapour may be separated intermediately, e.g. in separator 18. Methane is obtained overhead and partially condensed in heat exchanger 16, vapour being removed by line 29 and liquid being refluxed by line 28. Bottoms may be split into ethane C2 hydrocarbons (line 32), C3 (line 33) and C4 (line 34) by fractionators 21 and 22 for separate cracking in cracking plant 35 or may be cracked without separation. After cooling and drying the combined products are split into two streams in lines 40 and 41 for cooling with methane vapours and liquid respectively before being fed into second demethanizer 23. Overhead is partially condensed in heat exchanger 12 to provide reflux. The bottoms are further separated into ethylene (line 59), ethane/bottoms from fractionator 25) and C3 and higher hydrocarbons (bottoms from fractionator 24). PICT:1011518/C4-C5/1
机译:汽化甲烷和乙烯是通过在第一脱甲烷塔中分馏以获得塔顶气态甲烷和重质烃残渣,将后者裂解生成含甲烷和乙烯的气体混合物,从甲烷中分离出甲烷而从含甲烷和重烃的液化天然气中获得的第二脱甲烷塔,使液化的天然气在分馏之前通过热交换器以冷凝第二脱甲烷塔的回流,随后通过热交换器冷凝第一脱甲烷塔的回流。来自储存器10的液化天然气由管线11通过热交换器12、13、14、15、16和17泵送至第一脱甲烷塔20。蒸气可以在中间进行分离,例如通过蒸汽分离。在分离器18中将甲烷从塔顶获得并在热交换器16中进行部分冷凝。通过管线29除去蒸汽,通过管线28回流液体。塔底馏出物可分为乙烷,C2烃(管线32),C3(管线33)和C4在分馏塔21和22中(管线34),在裂化装置35中分离裂化,或者可以不分离而裂化。在冷却和干燥之后,将合并的产物在管线40和41中分成两股物流,分别用甲烷蒸气和液体冷却,然后将其进料到第二脱甲烷塔23中。塔顶馏出物在热交换器12中部分冷凝以提供回流。将塔底物进一步分离为乙烯(管线59),乙烷/来自分馏塔25的塔底馏分和C3和高级烃(来自分馏塔24的塔底馏分)。 <图片:1011518 / C4-C5 / 1>

著录项

  • 公开/公告号FR1458194A

    专利类型

  • 公开/公告日1966-11-10

    原文格式PDF

  • 申请/专利号FR19650018968

  • 发明设计人

    申请日1965-05-31

  • 分类号C07C11/04;F17C9/04;F25J3/02;

  • 国家 FR

  • 入库时间 2022-08-23 14:48:26

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