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Brief description of the liquefaction of natural gas with a change of phase

机译:相变天然气液化的简述

摘要

Process for liquefying natural gas in a cryogenic heat exchanger by flowing in indirect contact with refrigerant fluid entering heat exchanger at a first inlet at temperature T0 and pressure P1, and flowing through the exchanger as co-current with the natural gas stream, leaving the heat exchanger in the liquid state, then being expanded at the cold end of the exchanger to return to gaseous state at a pressure P1 P1 and temperature T1 T0, before leaving the hot end of exchanger by outlet orifice in gaseous state T0. The fluid is then reliquefied to the inlet of the exchanger via compression followed by partial condensation and phase separation, a first liquid phase taken to the first inlet, a first gaseous portion compressed by a second compressor and cooled in desuperheater by contact with portion of the first liquid phase, prior to condensing in a second condenser.
机译:通过与在第一入口以温度T0和压力P1进入热交换器的制冷剂流体间接接触流动并与天然气流并流流经热交换器而离开热量的方法,在低温热交换器中使天然气液化处于液态的换热器,然后在压力为P1 P1且温度为T1 T0的情况下,在换热器的冷端膨胀,返回到气态,然后由出口孔以气态T0离开换热器的热端。然后,通过压缩将流体重新液化到交换器的入口,然后进行部分冷凝和相分离,将第一液相带到第一入口,将第一气态部分通过第二压缩机压缩,并通过与部分热交换器接触的方式在减温器中冷却。第一液相,然后在第二冷凝器中冷凝。

著录项

  • 公开/公告号FR2993643B1

    专利类型

  • 公开/公告日2014-08-22

    原文格式PDF

  • 申请/专利权人 SAIPEM S.A.;

    申请/专利号FR20120056888

  • 申请日2012-07-17

  • 分类号F25J1/02;

  • 国家 FR

  • 入库时间 2022-08-21 15:36:35

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