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    • 3. 发明授权
    • Cryogenic distillation method and system for air separation
    • 低温蒸馏法和空气分离系统
    • US07464568B2
    • 2008-12-16
    • US10555765
    • 2004-03-24
    • Patrick Le BotOlivier De Cayeux
    • Patrick Le BotOlivier De Cayeux
    • F25J3/00
    • F25J3/04175F25J3/04054F25J3/0409F25J3/04296F25J3/04381F25J3/04393F25J3/04412F25J2240/04
    • Methods and apparatus for air separation by cryogenic distillation in a double or triple air separation column. The column in the system with the highest operating pressure is said to be operating at medium pressure. All the air to be distilled is pressurized to a high pressure, which is about 5 bar greater than the medium pressure. The air is purified at this high pressure, and a portion of the purified air is cooled in a heat exchange line, while another portion is expanded in a turbine. Part of the cooled air is drawn from the exchange line with a cold booster, which is mechanically coupled to at least one turbine. An energy dissipation device is also provided which is coupled to the turbine not coupled to the cold booster. The energy dissipation device is either another booster, an oil break system, or an electrical generator.
    • 在双层或三层空气分离柱中通过低温蒸馏进行空气分离的方法和装置。 具有最高工作压力的系统中的色谱柱据说在中等压力下运行。 所有待蒸馏的空气被加压至高于中压约5巴的高压。 空气在该高压下被净化,并且一部分净化空气在热交换管线中冷却,而另一部分在涡轮机中膨胀。 冷却的空气的一部分从具有机械地耦合到至少一个涡轮机的冷增压器的交换管线中抽出。 还提供了一种能量耗散装置,其耦合到未联接到冷增压器的涡轮机。 能量消耗装置是另一个增压器,断油系统或发电机。
    • 4. 发明申请
    • Cryogenic Distillation Method and System for Air Separation
    • 低温蒸馏法和空气分离系统
    • US20090078001A1
    • 2009-03-26
    • US12252444
    • 2008-10-16
    • Patrick Le BotOlivier De Cayeux
    • Patrick Le BotOlivier De Cayeux
    • F25J3/04
    • F25J3/04175F25J3/04054F25J3/0409F25J3/04296F25J3/04381F25J3/04393F25J3/04412F25J2240/04
    • Methods and apparatus for air separation by cryogenic distillation in a double or triple air separation column. The column in the system with the highest operating pressure is said to be operating at medium pressure. All the air to be distilled is pressurized to a high pressure, which is about 5 bar greater than the medium pressure. The air is purified at this high pressure, and a portion of the purified air is cooled in a heat exchange line, while another portion is expanded in a turbine. Part of the cooled air is drawn from the exchange line with a cold booster, which is mechanically coupled to at least one turbine. An energy dissipation device is also provided which is coupled to the turbine not coupled to the cold booster. The energy dissipation device is either another booster, an oil break system, or an electrical generator.
    • 在双层或三层空气分离柱中通过低温蒸馏进行空气分离的方法和装置。 具有最高工作压力的系统中的色谱柱据说在中等压力下运行。 所有待蒸馏的空气被加压至高于中压约5巴的高压。 空气在该高压下被净化,并且一部分净化空气在热交换管线中冷却,而另一部分在涡轮机中膨胀。 冷却的空气的一部分从具有机械地耦合到至少一个涡轮机的冷增压器的交换管线中抽出。 还提供了一种能量耗散装置,其耦合到未联接到冷增压器的涡轮机。 能量消耗装置是另一个增压器,断油系统或发电机。
    • 7. 发明授权
    • Method and apparatus for separating air by cryogenic distillation
    • 通过低温蒸馏分离空气的方法和装置
    • US09091478B2
    • 2015-07-28
    • US13384432
    • 2010-07-16
    • Frederic JudasHerve Le BihanPatrick Le Bot
    • Frederic JudasHerve Le BihanPatrick Le Bot
    • F25J3/00F25J3/04
    • F25J3/04781F25J3/04018F25J3/04024F25J3/04054F25J3/0409F25J3/04175F25J3/04296F25J3/04393F25J3/04412F25J3/04448F25J3/04454F25J3/04775F25J3/04824F25J2230/08F25J2230/30F25J2230/40F25J2240/04F25J2240/10F25J2240/42F25J2245/40
    • The invention relates to equipment for separating air by cryogenic distillation, including: a double air separation column; an exchange line (91); a hot air supercharger (CI) and a cold air supercharger (C2); a first turbine (TI) and a second turbine (T2), each of which is coupled to one of the superchargers; means for bringing all the air to a high pressure that is greater than the mean pressure; means for purifying the air at said high pressure; means for dividing the purified air into two fractions and sending one fraction thereof to the hot air supercharger and one fraction to the cold air supercharger after cooling in the exchange line; means for feeding the second air fraction from the cold air supercharger back into the exchange line; means for sending at least one pressurized liquid from one of the columns into the exchange line; a valve (4, 5); means for sending the non-supercharged air, purified at a high pressure, to the exchange line, so as to be cooled therein, and then to the valve; and means for sending the air, expanded in the valve, to be distilled and/or to the atmosphere.
    • 本发明涉及通过低温蒸馏分离空气的设备,包括:双空气分离塔; 交换线(91); 热空气增压器(CI)和冷气增压器(C2); 第一涡轮机(TI)和第二涡轮机(T2),其中每一个联接到增压器之一; 使所有空气达到高于平均压力的高压的装置; 用于在所述高压下净化空气的装置; 用于将净化空气分成两部分并将其一部分分配到热空气增压器中的装置,以及在交换管线中冷却之后的一部分到冷空气增压器的装置; 用于将来自冷空气增压器的第二空气部分进入交换线的装置; 用于将至少一个加压液体从所述列中的一个送入所述交换管线的装置; 阀(4,5); 用于将在高压下净化的非增压空气送到交换管路的装置,以便在其中冷却,然后到达阀门; 以及用于将在阀中膨胀并被蒸馏和/或向大气传播的空气的装置。
    • 8. 发明申请
    • METHOD AND APPARATUS FOR SEPARATING AIR BY CRYOGENIC DISTILLATION
    • 通过低温蒸馏分离空气的方法和装置
    • US20120118006A1
    • 2012-05-17
    • US13384432
    • 2010-07-16
    • Frederic JudasHerve Le BihanPatrick Le Bot
    • Frederic JudasHerve Le BihanPatrick Le Bot
    • F25J1/00
    • F25J3/04781F25J3/04018F25J3/04024F25J3/04054F25J3/0409F25J3/04175F25J3/04296F25J3/04393F25J3/04412F25J3/04448F25J3/04454F25J3/04775F25J3/04824F25J2230/08F25J2230/30F25J2230/40F25J2240/04F25J2240/10F25J2240/42F25J2245/40
    • The invention relates to equipment for separating air by cryogenic distillation, including: a double air separation column; an exchange line (91); a hot air supercharger (CI) and a cold air supercharger (C2); a first turbine (TI) and a second turbine (T2), each of which is coupled to one of the superchargers; means for bringing all the air to a high pressure that is greater than the mean pressure; means for purifying the air at said high pressure; means for dividing the purified air into two fractions and sending one fraction thereof to the hot air supercharger and one fraction to the cold air supercharger after cooling in the exchange line; means for feeding the second air fraction from the cold air supercharger back into the exchange line; means for sending at least one pressurized liquid from one of the columns into the exchange line; a valve (4, 5); means for sending the non-supercharged air, purified at a high pressure, to the exchange line, so as to be cooled therein, and then to the valve; and means for sending the air, expanded in the valve, to be distilled and/or to the atmosphere.
    • 本发明涉及通过低温蒸馏分离空气的设备,包括:双空气分离塔; 交换线(91); 热空气增压器(CI)和冷气增压器(C2); 第一涡轮机(TI)和第二涡轮机(T2),其中每一个联接到增压器之一; 使所有空气达到高于平均压力的高压的装置; 用于在所述高压下净化空气的装置; 用于将净化空气分成两部分并将其一部分分配到热空气增压器中的装置,以及在交换管线中冷却之后的一部分到冷空气增压器的装置; 用于将来自冷空气增压器的第二空气部分进入交换线的装置; 用于将至少一个加压液体从所述列中的一个送入所述交换管线的装置; 阀(4,5); 用于将在高压下净化的非增压空气送到交换管路的装置,以便在其中冷却,然后到达阀门; 以及用于将在阀中膨胀并被蒸馏和/或向大气传播的空气的装置。