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1.
公开(公告)号:US06662595B2
公开(公告)日:2003-12-16
申请号:US10217329
申请日:2002-08-13
申请人: Horst Corduan , Dietrich Rottmann , Christian Kunz
发明人: Horst Corduan , Dietrich Rottmann , Christian Kunz
IPC分类号: F25J304
CPC分类号: F25J3/04218 , F25J3/04084 , F25J3/0409 , F25J3/042 , F25J3/04303 , F25J3/0446 , F25J3/04672 , F25J2200/06 , F25J2200/94 , F25J2215/50 , F25J2235/50
摘要: The process and device are used to obtain a compressed product by low temperature separation of air in a rectification system which has a pressure column and a low pressure column. A first flow of compressed and purified feedstock air is cooled in a main heat exchanger system and is fed into the pressure column. At least one fraction from the pressure column is expanded and fed into the low pressure column. An oxygen-rich fraction from the low pressure column is liquid-pressurized and delivered to a mixing column. A heat exchange medium is fed into the lower area of the mixing column and is brought into countercurrent contact with the oxygen-rich fraction. A gaseous top product is removed from the upper area of the mixing column. A product fraction is removed from the rectification system, liquid-pressurized, vaporized in indirect heat exchange with the gaseous top product of the mixing column and is withdrawn as the compressed product. Indirect heat exchange is carried out for vaporization of the liquid-pressurized product fraction in the main heat exchanger system.
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公开(公告)号:US06196023B1
公开(公告)日:2001-03-06
申请号:US09297380
申请日:1999-04-30
IPC分类号: F25J100
CPC分类号: F25J3/04212 , F25J3/04084 , F25J3/0409 , F25J3/04103 , F25J3/04224 , F25J3/0423 , F25J3/04236 , F25J3/04284 , F25J3/04303 , F25J3/04321 , F25J3/04412 , F25J3/04418 , F25J3/04424 , F25J3/04872 , F25J3/04878 , F25J3/04884 , F25J2200/52 , F25J2200/54 , F25J2200/90 , F25J2235/02 , F25J2235/42 , F25J2245/42 , F25J2245/50 , F25J2250/04 , F25J2250/10 , F25J2250/20 , F25J2250/42 , F25J2250/50 , F25J2250/52
摘要: The process and the apparatus serve to produce pressurized nitrogen by low-temperature fractionation of air in a rectification system which has a pressure column (4) and a low-pressure column (5). Feed air (1, 3) is passed into the pressure column (4). An oxygen-containing liquid fraction (11) is taken off from the pressure column (4) and fed into the low-pressure column (5). Gaseous nitrogen (18) from the low-pressure column (5) is at least partially condensed in a top condenser (17) by indirect heat exchange with an evaporating liquid (13). Nitrogen from the low-pressure column is produced as gaseous pressurized nitrogen product (24, 25, 29) at a pressure which is higher than the operating pressure of the low-pressure column (5). Liquid nitrogen (20) withdrawn from the low-pressure column is brought (21) in the liquid state to a pressure which exceeds the pressure of the low-pressure column (5). The pressurized liquid (22) is evaporated in a product evaporator (23) by indirect heat exchange with a heat-transfer medium (35) and is subsequently produced as gaseous pressurized nitrogen product (24, 25, 29). (FIG. 1)
摘要翻译: 该方法和装置用于在具有压力塔(4)和低压塔(5)的精馏系统中通过空气低温分馏产生加压氮气。 进料空气(1,3)通入压力塔(4)。 将含氧液体馏分(11)从压力塔(4)中取出并进料到低压塔(5)中。 来自低压塔(5)的气态氮(18)通过与蒸发液体(13)的间接热交换在顶部冷凝器(17)中至少部分地冷凝。 来自低压塔的氮气以高于低压塔(5)的操作压力的压力产生为气态加压氮气产物(24,25,29)。 从低压塔排出的液氮(20)使(21)处于液态,压力超过低压塔(5)的压力。 加压液体(22)通过与传热介质(35)的间接热交换在产物蒸发器(23)中蒸发,随后被产生为气态加压氮气产物(24,25,29)。 (图。1)
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公开(公告)号:US06560992B2
公开(公告)日:2003-05-13
申请号:US09957469
申请日:2001-09-21
申请人: Horst Corduan , Dietrich Rottmann
发明人: Horst Corduan , Dietrich Rottmann
IPC分类号: F25J3100
CPC分类号: F25J3/04793 , F25J3/04303 , F25J3/04412 , F25J3/04678 , F25J3/048 , F25J2235/58
摘要: For adjusting the capacity of a low-temperature rectification unit having a high pressure column and a low pressure column in which a fluid is introduced into the high pressure column (1) and in which liquid from the bottom of the high pressure column is directed into the low pressure column (2), the amount of liquid that is removed from the bottom of high pressure and fed to the low pressure column (2) is controlled via flow adjustment (4), wherein a nominal value for flow adjustment (4) is set to a desired amount of flow, and the liquid level of the liquid at the bottom of column (1) that operates at higher pressure is fixed without a set nominal value corresponding to the amount of liquid that is removed.
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公开(公告)号:US07188492B2
公开(公告)日:2007-03-13
申请号:US10612287
申请日:2003-07-03
申请人: Horst Corduan , Dietrich Rottmann
发明人: Horst Corduan , Dietrich Rottmann
CPC分类号: F25J5/002 , F25J3/04296 , F25J3/04345 , F25J3/04393 , F25J3/04412 , F25J2205/04 , F25J2290/32 , F25J2290/42 , F28D9/0093 , Y10S62/903
摘要: A plate heat exchanger for indirect heat exchange of several fluid flows (30, 40, 50) with a heat transfer medium/cooling medium (10, 20) in a heat exchanger core (9) has a plurality of heat exchange passages within the core for the heat transfer medium/cooling medium (10, 20), a first fluid flow (30, 40, 50) and a second fluid flow (30, 40, 50). All heat exchange passages for the first fluid flow (40) are located In a first component area, and all heat exchange passages for the second fluid flow (30) are located in a second component area. The first and the second component areas do not intersect and each extend over the entire height of the heat exchanger core (9). The heat exchanger is particularly suitable for use in air-separation processes.
摘要翻译: 用于在热交换器芯(9)中具有传热介质/冷却介质(10,20)的若干流体流(30,40,50)的间接热交换的板式热交换器具有在所述芯部内的多个热交换通道 用于传热介质/冷却介质(10,20),第一流体流(30,40,50)和第二流体流(30,40,50)。 用于第一流体流(40)的所有热交换通道位于第一组分区域中,并且用于第二流体流(30)的所有热交换通道位于第二组分区域中。 第一和第二组分区域不相交并且各自延伸在热交换器芯(9)的整个高度上。 热交换器特别适用于空气分离过程。
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公开(公告)号:US07152432B2
公开(公告)日:2006-12-26
申请号:US10296883
申请日:2001-05-31
CPC分类号: F25J5/005 , F25J2250/02 , F25J2250/10 , F25J2250/20 , F25J2290/32 , Y10S62/903
摘要: The invention relates to a bath condenser with a condenser block (1) that has evaporation passages (8) for a liquid and liquefaction passages (2) for a heating medium and at least two circulation sections (7) that are located vertically on top of one another. The evaporation passages (8) each have on the lower end of a circulation section (7) at least one entry opening (9) for the liquid and on the upper end of a circulation section (7) at least one exit opening (10), for each circulation section (7) there being a liquid storage tank (15) that is flow-connected to the entry opening (9) and the exit opening (10) of the circulation section (7) and that has a gas offtake (18). The inlet into the gas offtake (18) is not located in the area in front of the side (12) of the circulation section (7) in which the exit opening (10) of the circulation section (7) is located.
摘要翻译: 本发明涉及一种具有冷凝器块(1)的浴冷凝器,其具有用于液体的液体和液化通道(2)和用于加热介质的至少两个循环部分(7)的蒸发通道(8),所述循环部分垂直地位于 另一个。 蒸发通道(8)各自在循环部分(7)的下端具有用于液体的至少一个入口(9)和循环段(7)的上端,至少一个出口(10) 对于每个循环部分(7),存在流体连接到循环部分(7)的入口(9)和出口(10)并且具有气体排出口(7)的液体储存罐(15) 18)。 进入气体出口(18)的入口不位于循环部分(7)的出口(10)所在的循环部分(7)的侧面(12)的前面区域。
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公开(公告)号:US06629433B2
公开(公告)日:2003-10-07
申请号:US09844254
申请日:2001-04-30
申请人: Horst Corduan , Dietrich Rottmann , Karl Leibl
发明人: Horst Corduan , Dietrich Rottmann , Karl Leibl
IPC分类号: F25J300
CPC分类号: F25J3/04218 , F25J3/04084 , F25J3/0409 , F25J3/04193 , F25J3/04224 , F25J3/04303 , F25J3/04351 , F25J3/04357 , F25J3/04393 , F25J3/04412 , F25J3/04672 , F25J3/04787 , F25J5/002 , F25J2215/54 , F25J2290/32 , F25J2290/42 , Y10S62/903
摘要: For the indirect heat-exchange of a plurality of gas streams (14, 15, 16) with a heat-cold carrier (2, 7) in heat-exchange blocks (23a, b, c, d, e) in which the gas streams (14, 15, 16) are passed through a multiplicity of heat-exchange passages, only one of the gas streams (14, 15, 16) is passed in this case through at least one heat-exchange block (23a, b, c, d, e). The heat-exchange passages of the heat-exchange block (23a, b, c, d, e), through which this gas stream (14, 15, 16) flows end at two end surfaces of the heat-exchange block (23a, b, c, d, e). The gas stream (23a, b, c, d, e) is fed to an taken off from these heat-exchange passages via in each case a collector/distributor (41) connected to the heat-exchange block (23a, b, c, d, e), which collector/distributor extends in each case over the entire end surface of the heat-exchange block (23a, b, c, d, e).
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公开(公告)号:US4824453A
公开(公告)日:1989-04-25
申请号:US217516
申请日:1988-07-11
申请人: Dietrich Rottmann , Horst Corduan
发明人: Dietrich Rottmann , Horst Corduan
IPC分类号: F25J3/04
CPC分类号: F25J3/04303 , F25J3/04212 , F25J3/04412 , F25J3/04678 , F25J3/04715 , F25J2200/06 , F25J2200/32 , F25J2200/34 , F25J2200/94 , F25J2205/02 , F25J2215/44 , F25J2215/52 , F25J2215/56 , F25J2220/42 , F25J2220/50 , F25J2250/20 , F25J2250/42 , Y10S62/924
摘要: In a process and apparatus for air separation by rectification air 1 is preliminarily separated in a first rectification stage 2 of a two-stage rectification column to obtain a nitrogen-rich fraction 4 and an oxygen-rich fraction 8. These two fractions are fed to the second rectification stage 6 and separated into oxygen and nitrogen fractions. An argon-enriched fraction, containing essentially oxygen and argon, is removed from the second rectification stage at an intermediate point and is separated in a raw argon column 10 by rectification into an argon-rich fraction 18 and a liquid fraction 19 containing essentially oxygen. The liquid fraction 19 is fed back into the second rectification stage. Another fraction 22 is removed from the raw argon column above the bottom thereof and is separated in a high-purity oxygen column 23 to produce a high-purity oxygen fraction 25, 26 and a lighter residual fraction 24. An additional nitrogen-rich fraction is removed from the head of the first rectification stage and separated in a high-purity nitrogen column 31 producing a bottom liquid fraction 29, which is fed back to the head of the first rectification stage, and a residual gas fraction 33. A high-purity nitrogen fraction 34 is removed at a point several plates below the head of the first rectification stage.
摘要翻译: 在二级精馏塔的第一精馏阶段2中,通过精馏空气1进行空气分离的方法和装置预先分离,得到富氮馏分4和富氧馏分8.将这两个馏分进料至 第二精馏段6并分离成氧和氮馏分。 在中间点从第二精馏阶段除去基本上含有氧和氩的富氩馏分,并通过精馏将其在原氩塔10中分离成富氩馏分18和基本上含氧的液体馏分19。 液体馏分19反馈回第二精馏段。 另一部分22从其底部的原氩塔中除去,并在高纯氧塔23中分离,以产生高纯氧分数25,26和较轻的残余馏分24.另外的富氮馏分为 从第一精馏段的头部除去,并在高纯氮塔31中分离,产生反馈到第一精馏段的头部的底部液体馏分29和残余气体馏分33.高纯度 氮馏分34在第一整流段的头部下方的几个板上被去除。
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公开(公告)号:US07134297B2
公开(公告)日:2006-11-14
申请号:US10365610
申请日:2003-02-13
申请人: Horst Corduan , Dietrich Rottmann
发明人: Horst Corduan , Dietrich Rottmann
IPC分类号: F25J3/00
CPC分类号: F25J3/04878 , F25J3/04412 , F25J3/04884 , F25J2235/50 , F25J2245/50 , F25J2250/04 , F25J2250/10 , F25J2250/20 , Y10S62/903
摘要: The invention relates to a process for the low-temperature fractionation of air in a rectification unit, which comprises a pressure column (1) a low-pressure column (2) and a condenser-evaporator system having at least two falling-film evaporators (203, 204). Oxygen-rich liquid from the low-pressure column (2) is introduced into the evaporation passages of the first and second falling-film evaporators (203, 204) and is partially evaporated. Unevaporated oxygen-rich liquid from the first falling-film evaporator (203) is transferred into the evaporation passages of the second falling-film evaporator (204).
摘要翻译: 本发明涉及一种精馏单元中空气的低温分馏方法,该方法包括一个压力塔(1),一个低压塔(2)和一个具有至少两个降膜蒸发器的冷凝器 - 蒸发器系统( 203,204)。 来自低压塔(2)的富氧液体被引入到第一和第二降膜蒸发器(203,204)的蒸发通道中并被部分蒸发。 来自第一降膜蒸发器(203)的未蒸发的富氧液体被转移到第二降膜蒸发器(204)的蒸发通道中。
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公开(公告)号:US20050028554A1
公开(公告)日:2005-02-10
申请号:US10296883
申请日:2001-05-31
CPC分类号: F25J5/005 , F25J2250/02 , F25J2250/10 , F25J2250/20 , F25J2290/32 , Y10S62/903
摘要: The invention relates to a bath condenser with a condenser block (1) that has evaporation passages (8) for a liquid and liquefaction passages (2) for a heating medium and at least two circulation sections (7) that are located vertically on top of one another. The evaporation passages (8) each have on the lower end of a circulation section (7) at least one entry opening (9) for the liquid and on the upper end of a circulation section (7) at least one exit opening (10), for each circulation section (7) there being a liquid storage tank (15) that is flow-connected to the entry opening (9) and the exit opening (10) of the circulation section (7) and that has a gas offtake (18). The inlet into the gas offtake (18) is not located in the area in front of the side (12) of the circulation section (7) in which the exit opening (10) of the circulation section (7) is located.
摘要翻译: 本发明涉及一种具有冷凝器块(1)的浴冷凝器,其具有用于液体的液体和液化通道(2)和用于加热介质的至少两个循环部分(7)的蒸发通道(8),所述循环部分垂直地位于 另一个。 蒸发通道(8)各自在循环部分(7)的下端具有用于液体的至少一个入口(9)和循环段(7)的上端,至少一个出口(10) 对于每个循环部分(7),存在流体连接到循环部分(7)的入口(9)和出口(10)并且具有气体排出口(7)的液体储存罐(15) 18)。 进入气体出口(18)的入口不位于循环部分(7)的出口(10)所在的循环部分(7)的侧面(12)的前面区域。
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10.
公开(公告)号:US06776004B2
公开(公告)日:2004-08-17
申请号:US10601875
申请日:2003-06-24
申请人: Dietrich Rottmann , Christian Kunz
发明人: Dietrich Rottmann , Christian Kunz
IPC分类号: F25J302
CPC分类号: F25J3/04745 , C01B13/0248 , C01B2210/0046 , C01B2210/0084 , C01B2210/0085 , F25J3/04303 , F25J3/04466 , F25J3/04872 , F25J3/04969 , F25J2200/06 , F25J2200/34 , F25J2200/92 , F25J2200/94 , F25J2235/50 , F25J2245/50
摘要: A process and apparatus for low-temperature fractionation of air in a distillation column system for nitrogen-oxygen separation (5, 6) introduces into first feed air stream (4) into a distillation column system for nitrogen-oxygen separation. An oxygen-rich fraction (22) from the distillation column system for nitrogen-oxygen separation is pressurized (23) in liquid form and is added (25) to a mixing column (26). A heat transfer medium stream is introduced into the lower region of the mixing column (26) and is brought into countercurrent contact with the oxygen-rich fraction (22, 25). Gaseous top product (260) from the upper region of the mixing column (26) is introduced into an additional column (27). A liquid (38, 39, 40, 41) from the lower or middle region of the mixing column is introduced into the distillation column system. A krypton- and xenon-containing oxygen stream (44, 46, 47, 48) from the distillation column system is introduced into a krypton-xenon enriching column (36) from which a krypton- and xenon-enriched fraction (51) is obtained. A krypton- and xenon-depleted top fraction (28) is obtained from the upper region of the additional column (27).
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