公开(公告)号：US20100206004A1

公开(公告)日：2010-08-19

申请号：US12677335

申请日：2008-09-09

Applicant: Benoit Davidian

Inventor： Benoit Davidian

IPC: F25J3/00 ,  F25B29/00 ,  F28F3/08

CPC classification number: F28D9/0037 ,  F25J3/04193 ,  F25J3/04218 ,  F25J3/044 ,  F25J3/04872 ,  F25J5/002 ,  F25J2200/72 ,  F25J2290/40 ,  F25J2290/42 ,  F28D2021/0033

Abstract: A unit for separating air using cryogenic distillation is provided.

Abstract translation: 提供了使用低温蒸馏分离空气的单元。

公开(公告)号：US20090314031A1

公开(公告)日：2009-12-24

申请号：US12305490

申请日：2007-06-19

Applicant: Benoit Davidian ,  Pierre Bodelin

Inventor： Benoit Davidian ,  Pierre Bodelin

IPC: F25J3/00

CPC classification number: F25J3/044 ,  F25J3/04254 ,  F25J3/04496 ,  F25J3/04793 ,  F25J3/04836 ,  F25J2210/42 ,  F25J2250/42 ,  F25J2290/62

Abstract: An air distillation unit comprises an air distillation column (10) suitable for producing a nominal flow of gaseous nitrogen, the top of said column being connected to a liquid nitrogen source (8), and operates by carrying out the following steps: a flow of compressed, cooled and purified air is sent to an exchanger (11) and then to the column, a flow of gaseous nitrogen is withdrawn from the column, the level of liquid at the bottom of the column is controlled; and injection liquid (20), sent from the source to the column, is no longer sent if the required production reduces to at most the nominal production. Application to the separation of air by cryogenic distillation.

Abstract translation: 空气蒸馏单元包括适于产生标称气态氮气的空气蒸馏塔（10），所述塔的顶部连接到液氮源（8），并通过执行以下步骤操作：流动 压缩，冷却和净化的空气被送到交换器（11），然后送到塔中，从塔中取出气态氮气流，控制塔底部的液体水平; 如果所需的生产量减少到最多的标称产量，则从源到塔的进料液体（20）不再发送。 应用于通过低温蒸馏分离空气。

公开(公告)号：US20080271481A1

公开(公告)日：2008-11-06

申请号：US12097641

申请日：2006-12-15

Applicant: Benoit Davidian

Inventor： Benoit Davidian

IPC: F25J3/00

CPC classification number: F25J3/04624 ,  F25J3/04254 ,  F25J3/04284 ,  F25J3/04296 ,  F25J3/04872 ,  F25J5/007 ,  F25J2200/02 ,  F25J2210/42 ,  F25J2290/44

Abstract: The invention relates to an air separating device by means of cryogenic distillation for producing nitrogen, comprising an exchange line (3), a simple distillation column (7) containing plates and/or structured packings, a supply line for delivery of compressed purified air (1) to the exchange line, a supply line for delivery of the compressed purified and cooled air from the exchange line to the distillation column, a line for withdrawal of a liquid (11) enriched in oxygen from the distillation column for delivery to the exchange line, said exchange line having two sections, a rectifying section (3B) and a heat exchange section (3A), the rectifying section being connected to the column and the line for the enriched liquid and the heat exchange section is connected to the air supply line and the rectifying section.

Abstract translation: 本发明涉及一种通过用于生产氮的低温蒸馏的空气分离装置，包括交换管线（3），包含板和/或结构填料的简单蒸馏塔（7），用于输送压缩净化空气的供应管线 1）到交换管线，用于将压缩的净化和冷却的空气从交换管线输送到蒸馏塔的供应管线，用于从蒸馏塔排出富含氧的液体（11）的管线，用于输送到交换器 线路，所述交换线路具有两个部分，整流部分（3B）和热交换部分（3A），所述整流部分连接到所述列，并且所述富集液体和所述热交换部分的所述管线连接到 供气管路和整流段。

公开(公告)号：US08776546B2

公开(公告)日：2014-07-15

申请号：US12305490

申请日：2007-06-19

Applicant: Benoit Davidian ,  Pierre Bodelin

Inventor： Benoit Davidian ,  Pierre Bodelin

IPC: F25J3/00 ,  F17C9/02

CPC classification number: F25J3/044 ,  F25J3/04254 ,  F25J3/04496 ,  F25J3/04793 ,  F25J3/04836 ,  F25J2210/42 ,  F25J2250/42 ,  F25J2290/62

Abstract: An air distillation unit comprises an air distillation column (10) suitable for producing a nominal flow of gaseous nitrogen, the top of said column being connected to a liquid nitrogen source (8), and operates by carrying out the following steps: a flow of compressed, cooled and purified air is sent to an exchanger (11) and then to the column, a flow of gaseous nitrogen is withdrawn from the column, the level of liquid at the bottom of the column is controlled; and injection liquid (20), sent from the source to the column, is no longer sent if the required production reduces to at most the nominal production. Application to the separation of air by cryogenic distillation.

Abstract translation: 空气蒸馏单元包括适于产生标称气态氮气的空气蒸馏塔（10），所述塔的顶部连接到液氮源（8），并通过执行以下步骤操作：流动 压缩，冷却和净化的空气被送到交换器（11），然后送到塔中，从塔中取出气态氮气流，控制塔底部的液体水平; 如果所需的生产量减少到最多的标称产量，则从源到塔的进料液体（20）不再发送。 应用于通过低温蒸馏分离空气。

公开(公告)号：US20130133364A1

公开(公告)日：2013-05-30

申请号：US13805367

申请日：2011-07-05

Applicant: Benoit Davidian

Inventor： Benoit Davidian

IPC: F25J3/04

CPC classification number: F25J3/04 ,  F25J3/0204 ,  F25J3/0409 ,  F25J3/04206 ,  F25J3/04303 ,  F25J3/04412 ,  F25J3/04824 ,  F25J3/04836 ,  F25J3/0486 ,  F25J2215/02 ,  F25J2215/54 ,  F25J2245/50 ,  F25J2250/50 ,  F25J2290/62

Abstract: In a process for delivering pressurized gas from an apparatus for separating air by cryogenic distillation, a stream of oxygen-rich liquid or gas having a nominal flow rate is withdrawn from a low-pressure column, an oxygen-rich liquid purge stream is withdrawn as bottoms from the low-pressure column and the oxygen-rich liquid purge stream is sent to a storage tank, in the event of a reduction in the production by the column system or an increase in the demand by a customer, a back-up stream is withdrawn from the storage tank and vaporized in a back-up reboiler and only if the liquid level in the storage tank exceeds a given threshold, a liquid stream is withdrawn from the storage tank constituting at most 2% of the nominal production output of the oxygen-rich stream and is sent to the back-up reboiler.

Abstract translation: 在通过低温蒸馏从用于分离空气的装置输送加压气体的方法中，从低压塔中取出具有标称流量的富氧液体或气体流，将富氧液体吹扫流作为 来自低压塔的底部物质和富氧液体吹扫流被送到储罐中，在塔系统的生产减少或客户的需求增加的情况下，备用流 从储罐中取出并在备用再沸器中蒸发，只有当储罐中的液位超过给定的阈值时，液体流从存储罐中取出，占储罐的标称产量的2％ 富氧流，并被送到备用再沸器。

公开(公告)号：US20130055891A1

公开(公告)日：2013-03-07

申请号：US13634276

申请日：2011-02-25

Applicant: Bruno Alban ,  Philippe Arpentinier ,  Alain Briglia ,  Serge Moreau ,  Fabrice Del Corso ,  Benoit Davidian

Inventor： Bruno Alban ,  Philippe Arpentinier ,  Alain Briglia ,  Serge Moreau ,  Fabrice Del Corso ,  Benoit Davidian

IPC: B01D53/14 ,  B01D53/02

CPC classification number: B01D53/263 ,  B01D47/00 ,  B01D53/002 ,  B01D53/62 ,  B01D53/64 ,  B01D53/75 ,  B01D2251/302 ,  B01D2251/404 ,  B01D2256/22 ,  B01D2257/102 ,  B01D2257/104 ,  B01D2257/11 ,  B01D2257/302 ,  B01D2257/404 ,  B01D2257/602 ,  B01D2258/00 ,  C01B32/50 ,  F23J15/02 ,  F23J2215/50 ,  F23J2215/60 ,  F23J2219/40 ,  F23J2219/70 ,  F25J3/0266 ,  F25J3/04533 ,  F25J3/04563 ,  F25J3/067 ,  F25J2205/32 ,  F25J2205/34 ,  F25J2210/70 ,  F25J2220/80 ,  F25J2230/08 ,  F25J2230/30 ,  F25J2260/44 ,  F25J2270/90 ,  Y02C10/04 ,  Y02C10/12 ,  Y02E20/326 ,  Y02E20/344 ,  Y02P20/152

Abstract: The invention relates to a method for treating a gas stream comprising combustion fumes containing CO2 in an initial proportion, water vapor, one or more volatile acid compounds, and one or more additional impurities selected from among oxygen, nitrogen and argon, comprising the steps of: i) compressing the gas stream to a final pressure of 1 bar to 74 bar absolute; ii) cooling the gas stream to a temperature of around −10° C. to around −130° C. and eliminating at least one additional impurity; and iii) recovering a CO2-enriched gas stream containing a final proportion of CO2 greater than the initial proportion of CO2 in the stream to be treated. In addition, the method comprises, prior to step i), a step of pre-drying the stream for removing therefrom at least a portion of the water vapor which it contains.

Abstract translation: 本发明涉及一种用于处理气流的方法，其包括初始比例含有CO 2的燃烧烟雾，水蒸气，一种或多种挥发性酸化合物和一种或多种选自氧，氮和氩的附加杂质，其包括以下步骤： ：i）将气流压缩至1巴至74巴绝对压力的最终压力; ii）将气流冷却至约-10℃至约-130℃的温度，并除去至少一种另外的杂质; 和iii）回收含CO 2的最终比例的CO 2的CO 2的流量大于待处理流中CO 2的初始比例。 此外，该方法在步骤i）之前包括预干燥流以从其中除去其中含有的至少一部分水蒸气的步骤。

公开(公告)号：US20120279255A1

公开(公告)日：2012-11-08

申请号：US13511423

申请日：2010-11-22

Applicant: Benoit Davidian

Inventor： Benoit Davidian

IPC: F25J3/08

CPC classification number: F25J3/04157 ,  F25J3/04018 ,  F25J3/04236 ,  F25J2205/04 ,  F25J2205/34 ,  F25J2230/04 ,  F25J2230/06 ,  F25J2245/02

Abstract: The invention relates to a method for compressing and cooling air upstream from a facility for cryogenic separation of air, with no means for exchange by indirect heat, in which humid air is compressed in a compressor, the air compressed in the compressor is cooled in a first exchanger having indirect heat exchange, water is recovered from the air upstream and/or downstream from cooling in the first exchanger, the air cooled in the first exchanger is sent to a purification unit in order to produce air purified of carbon dioxide and/or water, the purified air is sent to the cryogenic separation facility, and at least one gas is recovered from the cryogenic separation facility.

Abstract translation: 本发明涉及一种用于压缩和冷却用于空气低温分离的设备上游的空气的方法，没有任何通过间接热量进行交换的装置，其中湿空气在压缩机中被压缩，在压缩机中压缩的空气被冷却 第一交换器具有间接热交换，在第一交换器中从上游和/或下游冷却回收水，将第一交换器中冷却的空气送至净化单元，以产生纯化的二氧化碳和/或 净化后的空气被送到低温分离设备，从低温分离设备回收至少一种气体。

公开(公告)号：US20110132035A1

公开(公告)日：2011-06-09

申请号：US12528713

申请日：2008-02-18

Applicant: Pierre Bodelin ,  Benoit Davidian ,  Eric Masliah

Inventor： Pierre Bodelin ,  Benoit Davidian ,  Eric Masliah

IPC: F25J3/04 ,  F25J3/00

CPC classification number: F25J3/044 ,  F25J3/04254 ,  F25J3/04836 ,  F25J2210/42 ,  F25J2245/42 ,  F25J2250/42 ,  F25J2290/10 ,  F25J2290/62

Abstract: A method and apparatus for providing nitrogen is provided.

Abstract translation: 提供了一种提供氮气的方法和装置。

公开(公告)号：US20110067445A1

公开(公告)日：2011-03-24

申请号：US12937608

申请日：2009-04-08

Applicant: Benoit Davidian

Inventor： Benoit Davidian

IPC: F25J3/00

CPC classification number: F25J3/04181 ,  F25J3/0406 ,  F25J3/0409 ,  F25J3/04103 ,  F25J3/04187 ,  F25J3/04206 ,  F25J3/04303 ,  F25J3/04309 ,  F25J3/04351 ,  F25J3/04393 ,  F25J3/04418 ,  F25J2200/34 ,  F25J2200/54 ,  F25J2250/40 ,  F25J2250/42 ,  F25J2250/50

Abstract: A method and to an apparatus for producing oxygen by separating air using cryogenic distillation is presented.

Abstract translation: 提出了一种通过使用低温蒸馏分离空气来生产氧气的方法和装置。