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    • 5. 发明申请
    • PROCESS FOR THE SEPARATION OF AIR BY CRYOGENIC DISTILLATION
    • 通过低温蒸馏分离空气的方法
    • WO2013148799A3
    • 2015-06-25
    • PCT/US2013034042
    • 2013-03-27
    • AIR LIQUIDEHA BAOBRUGEROLLE JEAN-RENAUD
    • HA BAOBRUGEROLLE JEAN-RENAUD
    • F25J3/00
    • F25J3/04054F25J3/0409F25J3/04175F25J3/04296F25J3/04303F25J3/04393F25J3/04412F25J2290/10
    • A process for separation of air by cryogenic distillation, including cooling a first purified feed air stream in a heat exchanger, thereby producing a cooled first feed stream, removing a first portion from the heat exchanger at a first intermediate temperature, and compressing the cooled first portion in a first booster compressor, cooling the compressed first portion in the heat exchanger, thereby producing a cooled first portion, removing a second portion from the heat exchanger at a second intermediate temperature, and compressing the cooled second portion in a second booster compressor, cooling the compressed second portion in the heat exchanger, thereby producing a cooled second portion, and vaporizing a pressurized liquid stream from the column system in the heat exchanger at a vaporization temperature to form a pressurized gaseous product stream, wherein, both the first discharge temperature and said second discharge temperature are below - 55°C.
    • 一种通过低温蒸馏分离空气的方法,包括冷却热交换器中的第一纯化进料空气流,从而产生冷却的第一进料流,在第一中间温度下从热交换器中除去第一部分,并将冷却的第一 冷却第一增压压缩机中的压缩的第一部分,从而产生冷却的第一部分,在第二中间温度下从热交换器中除去第二部分,并在第二增压压缩机中压缩冷却的第二部分, 冷却热交换器中的压缩的第二部分,从而产生冷却的第二部分,并且在蒸发温度下将来自热交换器中的塔系统的加压液体流蒸发以形成加压的气态产物流,其中,第一排出温度 并且所述第二排出温度低于-55℃。
    • 6. 发明申请
    • PROCESS AND APPARATUS FOR THE SEPARATION OF AIR BY CRYOGENIC DISTILLATION
    • 用于通过低温蒸馏分离空气的方法和装置
    • WO2005057112A1
    • 2005-06-23
    • PCT/IB2004/003925
    • 2004-11-30
    • L'AIR LIQUIDE, SOCIETE ANONYME A DIRECTOIRE ET CONSEIL DE SURVEILLANCE POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDEHA, BaoBRUGEROLLE, Jean-Renaud
    • HA, BaoBRUGEROLLE, Jean-Renaud
    • F25J3/04
    • F25J3/04175F25J3/04024F25J3/04054F25J3/04084F25J3/0409F25J3/04133F25J3/04278F25J3/04296F25J3/04303F25J3/04309F25J3/04315F25J3/04375F25J3/04381F25J3/04393F25J3/04412F25J2205/04F25J2230/20F25J2270/90
    • A process for separating air by cryogenic distillation in a column system comprising a high pressure column and a low pressure column comprises compressing all the feed air in a first compressor (1) to a first outlet pressure, sending a first part of the air at the first outlet pressure to a second compressor (3) and compressing the air to a second outlet pressure, cooling at least part of the air at the second outlet pressure in a heat exchanger (5) to form cooled compressed air at the second outlet pressure, sending at least part (7) of the cooled compressed air at the second outlet pressure to a third compressor (8) and compressing the at least part of the cooled compressed air at the second outlet pressure to a third outlet pressure, liquefying at least part of the air at the third outlet pressure and sending the liquefied air (10) to at least one column of the column system wherein at least 50% of the liquefied air sent to the column system has been compressed in the third compressor (8), cooling a second part of the air (12) at the first outlet pressure in the heat exchanger and expanding at least part of the second part of the air in an expander (13) from the first outlet pressure to the pressure of a column (30, 31) of column system and sending the expanded air to that column, removing liquid (20) from a column of the column system and vaporizing the liquid by heat exchange in the heat exchanger.
    • 在包括高压塔和低压塔的塔系统中通过低温蒸馏分离空气的方法包括将第一压缩机(1)中的所有进料空气压缩至第一出口压力,将第一部分空气在 对第二压缩机(3)的第一出口压力并将空气压缩到第二出口压力,在热交换器(5)中在第二出口压力下冷却至少部分空气以在第二出口压力下形成冷却的压缩空气, 将处于第二出口压力的冷却的压缩空气的至少一部分(7)送至第三压缩机(8),并将第二出口压力下的冷却的压缩空气的至少一部分压缩至第三出口压力, 的第三出口压力的空气,并将液化空气(10)送入塔系统的至少一列,其中送至塔系统的至少50%的液化空气在第三压缩机中被压缩 (8),在热交换器中以第一出口压力冷却空气(12)的第二部分,并将膨胀器(13)中的空气的至少部分的第二部分从第一出口压力膨胀到压力 的柱系统的塔(30,31),并将膨胀的空气送入该塔,从塔系统的塔中除去液体(20),并通过热交换器中的热交换来蒸发液体。