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1. 发明公开

EP3395428A2 METHOD OF OBTAINING CARBON DIOXIDE FROM A CARBON DIOXIDE-CONTAINING GAS MIXTURE 审中-公开
公开(公告)号：EP3395428A2
公开(公告)日：2018-10-31
申请号：EP18170442.0
申请日：2010-12-15
申请人： L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE
发明人： HASSE, David J. , KULKARNI, Sudhir S. , SANDERS, JR., Edgar S. , TRANIER, Jean-Pierre , TERRIEN, Paul
IPC分类号： B01D53/22 , B01D53/00 , B01D71/64 , F25J3/06
CPC分类号： B01D53/228 , B01D53/002 , B01D53/229 , B01D71/50 , B01D71/52 , B01D71/64 , B01D71/68 , B01D71/82 , B01D2257/504 , F25J3/067 , F25J2205/20 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2230/08 , F25J2230/30 , F25J2230/80 , F25J2235/80 , F25J2240/80 , F25J2240/90 , F25J2245/02 , F25J2270/02 , F25J2270/06 , Y02C10/10 , Y02C10/12
摘要： Disclosed are methods of obtaining carbon dioxide from a CO 2 -containing gas mixture. The methods combine the benefits of gas membrane separation with cryogenic temperatures.

2. 发明公开

EP2234694A4 CARBON DIOXIDE CAPTURE FROM FLUE GAS 有权转让
标题翻译：截留二氧化碳的烟
公开(公告)号：EP2234694A4
公开(公告)日：2016-12-07
申请号：EP08855143
申请日：2008-11-28
申请人： SUSTAINABLE ENERGY SOLUTIONS LLC
发明人： BAXTER LARRY L
IPC分类号： B01D53/00 , B01D53/62 , F25J3/06
CPC分类号： F25J3/067 , B01D53/002 , B01D2257/504 , F01D15/005 , F01K13/00 , F02C1/02 , F02C1/04 , F02C6/16 , F22B37/008 , F23J15/06 , F23J2900/15061 , F25J3/066 , F25J2205/20 , F25J2205/24 , F25J2210/70 , F25J2220/82 , F25J2220/84 , F25J2230/04 , F25J2230/20 , F25J2230/30 , F25J2240/02 , F25J2240/40 , F25J2240/90 , F25J2260/02 , F25J2260/30 , F25J2260/80 , F25J2270/02 , F25J2270/04 , F25J2270/90 , F25J2280/02 , F25J2290/44 , F25J2290/62 , F25J2290/80 , Y02C10/04 , Y02C10/12 , Y02E20/326 , Y02E20/363 , Y02E60/15
摘要： A method for capturing carbon dioxide from a flue gas includes (i) removing moisture from a flue gas to yield a dried flue gas; (ii) compressing the dried flue gas to yield a compressed gas stream; (iii) reducing the temperature of the compressed gas stream to a temperature T1 using a first heat exchanger; (iv) reducing the temperature of the compressed gas stream to a second temperarature T2 using a second heat exchanger stream, where T2

3. 发明授权

EP2512622B1 METHOD OF OBTAINING CARBON DIOXIDE FROM A CARBON DIOXIDE-CONTAINING GAS MIXTURE BY MEANS OF A MEMBRANE WITH A SWEEP STREAM 有权
标题翻译：一种获得的二氧化碳含有二氧化碳气体混合物，使用膜WITH清洗流
公开(公告)号：EP2512622B1
公开(公告)日：2016-11-02
申请号：EP10799188.7
申请日：2010-12-15
申请人： L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude
发明人： HASSE, David, J. , KULKARNI, Sudhir, S. , SANDERS, Edgar, S., Jr. , TRANIER, Jean-Pierre , TERRIEN, Paul
IPC分类号： B01D53/00 , B01D53/22 , C01B31/20 , F23J15/00 , F25J3/06 , F23J15/06
CPC分类号： B01D53/229 , B01D53/002 , B01D2256/22 , B01D2257/504 , F23J15/06 , F23J2215/50 , F23J2900/15061 , F25J3/067 , F25J2205/20 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2230/08 , F25J2230/30 , F25J2230/80 , F25J2235/80 , F25J2240/80 , F25J2240/90 , F25J2245/02 , F25J2270/02 , F25J2270/06 , Y02C10/10 , Y02C10/12 , Y02C20/20 , Y02E20/326 , Y02E20/363
摘要： Disclosed are methods of obtaining carbon dioxide from a CO2-containing gas mixture. The methods combine the benefits of gas membrane separation with cryogenic temperatures.

4. 发明公开

EP2997320A2 ANLAGE ZUR VERRINGERUNG EINES KOHLENDIOXIDGEHALTS EINES KOHLENDIOXIDHALTIGEN UND KOHLENWASSERSTOFFREICHEN GASSTROMS UND ENTSPRECHENDES VERFAHREN 审中-公开
标题翻译：附录A，以减少含有二氧化碳和富含碳氢化合物的气体流量和相应的方法二氧化碳水平
公开(公告)号：EP2997320A2
公开(公告)日：2016-03-23
申请号：EP14879279.9
申请日：2014-05-08
申请人： Linde Aktiengesellschaft
发明人： ADLER, Robert , DORNER, Sascha , KLEIN, Ekkehardt , NAGL, Christoph
IPC分类号： F25J3/06 , B01D53/00 , C10L3/10
CPC分类号： F25J3/067 , B01D53/002 , B01D2256/24 , B01D2256/245 , B01D2257/504 , B01D2258/05 , C10L3/104 , F25J3/061 , F25J3/0635 , F25J2205/20 , F25J2205/24 , F25J2210/42 , F25J2210/62 , F25J2270/904 , Y02C10/12 , Y02E50/346
摘要： The invention relates to an installation (1) configured to reduce a carbon dioxide content of a gas flow (A) that contains carbon dioxide and is rich in hydrocarbons, comprising a first and a second segregating unit (10, 20) each of which has a cryogenic condenser (11, 21) that is arranged in a segregation chamber (12, 22) and can be supplied with a coolant (C), and means (30, 40) being provided that are configured, in a first operating mode, to guide the coolant (C) through the cryogenic condenser (11) of only the first segregating unit (10) and to guide the carbon dioxide-containing, hydrocarbon-rich gas flow (A) through the segregation chamber (12) of only the first segregating unit (10), and to heat the second segregating unit (20) and remove a carbon dioxide-rich flow (D) from said second segregating unit (20); and being configured, in a second operating mode, to guide the coolant (C) through the cryogenic condenser (21) of only the second segregating unit (20) and to guide the carbon dioxide-containing, hydrocarbon-rich gas flow (A) through the segregation chamber (22) of only the second segregating unit (20), and to heat the first segregating unit (10) and remove a carbon dioxide-rich flow (D) therefrom. The invention also relates to a corresponding method.

5. 发明公开

EP1867940A3 Apparatus for the liquefaction of natural gas and methods relating to same 审中-公开
标题翻译：天然气液化装置及其相关方法
公开(公告)号：EP1867940A3
公开(公告)日：2016-03-09
申请号：EP07017307.5
申请日：2002-07-01
申请人： Bechtel BWXT Idaho, LLC
发明人： Wilding, Bruce, M. , Bingham, Dennis, N. , McKellar, Michael G. , Turner, Terry D. , Raterman, Kevin T. , Palmer, Gary, L. , Klingler, Kerry, M. , Vranicar, John, J.
IPC分类号： F25J1/02 , F25J3/00 , F25J3/08 , B01D53/52 , F28D7/04 , F28F27/02
CPC分类号： F25J1/0259 , F25J1/0022 , F25J1/0037 , F25J1/004 , F25J1/0045 , F25J1/0201 , F25J1/0232 , F25J1/0244 , F25J1/0247 , F25J1/0262 , F25J1/0275 , F25J5/002 , F25J2205/20 , F25J2205/60 , F25J2205/84 , F25J2210/06 , F25J2220/62 , F25J2220/66 , F25J2220/68 , F25J2230/30 , F25J2240/60 , F25J2245/90 , F25J2290/44 , F25J2290/62 , F28D7/04 , Y10S62/904 , Y10S62/929
摘要： A liquefaction plant (102) comprising:
a plant inlet (112) configured to be sealingly and fluidly coupled with a source of unpurified natural gas;
a turbo expander (156) positioned and configured to receive a first stream of natural gas drawn through the plant inlet and produce and expanded cooling stream therefrom;
a compressor (158) mechanically coupled to the turbo expander and positioned and configured to receive a second stream of natural gas drawn through the plant inlet and
produce a compresses process stream therefrom;
a first heat exchanger (166) positioned and configured to receive the compressed process stream and the expanded cooling stream in a countercurrent flow arrangement to cool the compressed process stream;
a first plant outlet (132) positioned and configured to be sealingly and fluidly coupled with the source of unpurified gas and to discharge the expanded cooling stream thereinto subsequent to passage thereof through the heat exchanger;
a first expansion valve (174) positioned and configured to receive and expand a first portion of the cooled compressed process stream to form an additional cooling stream, the plant further including conduit structure to combine additional cooling stream with the expanded cooling stream to the expanded cooling stream entering the first heat exchanger;
a second expansion valve (176) positioned and configured to receive and expand a second portion of the cooled compressed process stream to form gas-solid-liquid mixture therefrom;
a first gas-liquid separator (180) positioned and configured to receive the gas-solid-liquid mixture; and
a second plant outlet (114) positioned to be sealingly and fluidly coupled with a storage vessel, the first gas-liquid separator being positioned and configured to deliver a liquid contained therein to the second plant outlet.
摘要翻译： 1。一种液化设备（102），包括：植物入口（112），其被配置为与未纯化的天然气源密封且流体地连接; 涡轮膨胀机（156），所述涡轮膨胀机（156）定位并构造成接收通过所述设备入口抽出的第一天然气流并且由此产生并膨胀冷却流; 压缩机（158），其机械地连接到所述涡轮膨胀机并且被定位和构造成接收通过所述设备入口抽取的第二天然气流并且由此产生压缩过程流; 第一热交换器（166），所述第一热交换器（166）定位并构造成以逆流流动布置接收所述压缩的工艺物流和所述膨胀的冷却物流以冷却所述压缩的工艺物流; 第一设备出口（132），所述第一设备出口（132）被定位和构造成密封地且流体地与所述未净化气体源耦合，并且在所述膨胀冷却流通过所述热交换器之后排出所述第一设备出口; 第一膨胀阀（174），所述第一膨胀阀（174）定位并构造成接收和膨胀所述冷却的压缩过程流的第一部分以形成额外的冷却流，所述设备还包括管道结构以将额外的冷却流与所述膨胀的冷却流结合到所述膨胀的冷却流进入第一换热器; 第二膨胀阀（176），所述第二膨胀阀（176）定位并构造成接收和膨胀所述冷却的压缩过程流的第二部分以从其中形成气 - 固 - 液混合物; 第一气液分离器（180），所述第一气液分离器（180）定位和构造成接收所述气固液混合物; 和定位成与储存容器密封并流体连接的第二植物出口（114），所述第一气液分离器被定位和构造成将容纳在其中的液体输送到所述第二植物出口。

6. 发明授权

EP2253911B1 Refiner for a circulation type liquid helium recondensation device with a contaminant purging function 有权
标题翻译：清洁装置用于氦Rückverflüssiger与杂质冲洗功能
公开(公告)号：EP2253911B1
公开(公告)日：2015-06-24
申请号：EP10008867.3
申请日：2003-09-18
申请人： Japan Science and Technology Agency
发明人： Takeda, Tsunehiro
IPC分类号： F25J3/08
CPC分类号： F25J1/025 , F17C2221/017 , F17C2223/0161 , F17C2223/033 , F17C2250/0443 , F17C2260/044 , F17C2265/015 , F17C2265/033 , F17C2265/034 , F17C2265/036 , F17C2265/037 , F25J1/0065 , F25J1/0276 , F25J3/08 , F25J2205/20 , F25J2215/30 , F25J2245/90 , F25J2270/90 , F25J2270/912 , F25J2280/30 , F25J2290/62

7. 发明授权

EP2475747B1 A METHOD AND AN APPARATUS FOR NGL/GPL RECOVERY FROM A HYDROCARBON GAS, IN PARTICULAR FROM NATURAL GAS 有权
标题翻译：方法和装置NGL / LPG回收率为烃类气体，特别是天然气
公开(公告)号：EP2475747B1
公开(公告)日：2014-11-19
申请号：EP11751930.6
申请日：2011-03-30
申请人： Sime S.r.l.
发明人： FAVILLI, Stefano , LEITEMPERGHER, Giacinto , SCIBOLA, Luciano
IPC分类号： C10G5/06 , F25J3/06 , C10L3/10 , B01D53/00 , B01D53/26
CPC分类号： B01D53/002 , B01D53/265 , B01D2256/24 , B01D2257/702 , B01D2257/80 , C10G5/06 , C10G2300/1025 , C10L3/106 , C10L3/12 , F25J3/061 , F25J3/0635 , F25J3/064 , F25J2205/20 , F25J2230/08 , F25J2230/20 , F25J2230/32 , F25J2235/60 , F25J2240/02 , F25J2240/40 , F25J2245/02 , F25J2270/90 , F25J2290/42

8. 发明公开

EP2598817A1 CRYOGENIC SYSTEMS FOR REMOVING ACID GASES FROM A HYDROCARBON GAS STREAM USING CO-CURRENT SEPARATION DEVICES 无效转让
标题翻译：低温系统用于酸性气体从烃气流与跟踪末端切割设备中移除
公开(公告)号：EP2598817A1
公开(公告)日：2013-06-05
申请号：EP11812917.0
申请日：2011-06-28
申请人： ExxonMobil Upstream Research Company
发明人： NORTHROP, Paul, Scott
IPC分类号： F25J3/00
CPC分类号： F25J3/0266 , C10L3/102 , C10L3/106 , F25J3/02 , F25J3/0209 , F25J3/0233 , F25J2200/02 , F25J2200/40 , F25J2200/74 , F25J2200/76 , F25J2205/02 , F25J2205/04 , F25J2205/20 , F25J2210/62 , F25J2210/80 , F25J2215/04 , F25J2220/66 , F25J2220/68 , F25J2240/60 , F25J2260/80 , F25J2270/12 , F25J2270/60 , F25J2280/10 , F25J2280/40 , F25J2290/42 , Y02C10/12
摘要： A system for removing acid gases from a raw gas stream is provided. The system includes a cryogenic distillation column. The cryogenic distillation column receives a dehydrated and chilled sour gas stream, and separates the sour gas stream into an overhead gas stream comprised primarily of methane, and a bottom acid gas stream comprised primarily of carbon dioxide. The system also includes a series of co-current contactors. The co-current contactors may be placed in series to receive the bottom acid gas stream and recapture any entrained methane gas. Alternatively or in addition, the co-current contactors may be placed in series to receive the overhead gas stream, and sweeten it using a reflux liquid such as methane. In this instance, the sweetened gas is optionally liquefied and delivered for commercial sale, or is used as fuel gas on-site.

9. 发明公开

EP2304359A1 METHOD AND SYSTEM FOR EXTRACTING CARBON DIOXIDE BY ANTI-SUBLIMATION AT RAISED PRESSURE 审中-公开
标题翻译：方法和系统在高压凝华BY二氧化碳萃取
公开(公告)号：EP2304359A1
公开(公告)日：2011-04-06
申请号：EP09781042.8
申请日：2009-07-24
申请人： Alstom Technology Ltd
发明人： HEES, Wolfgang, Georg , MONROE, Charles, Malcolm
IPC分类号： F25J3/02 , C01B31/22 , B01D53/00 , B01D7/02 , F17C9/00
CPC分类号： B01D53/002 , B01D7/02 , B01D2257/504 , F25J3/066 , F25J3/067 , F25J2205/20 , F25J2205/24 , F25J2205/32 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2230/08 , F25J2230/30 , F25J2240/40 , F25J2270/04 , F25J2270/90 , Y02C10/12 , Y02P70/34
摘要： A method for removal of CO2 from a gas stream by anti-sublimation, comprising the steps of: a) introducing a gas stream containing CO2 into a frosting vessel; b) reducing the temperature of at least a portion of the gas stream in said frosting vessel to a temperature at which solid CO2 is deposited by anti-sublimation; c) discharging the gas stream depleted of CO2 from the frosting vessel; and d) recovering the deposited solid CO2; wherein the pressure of the gas stream in step b) is higher than atmospheric pressure. An anti-sublimation system for removal of CO2 from a gas stream, comprising: a frosting vessel configured to receive the gas stream, said frosting vessel comprising a low temperature refrigeration device configured for reducing the temperature of at least a portion of a gas stream in said frosting vessel to a temperature at which solid CO2 is deposited by anti-sublimation; and a compressor configured to increase the gas pressure of the gas stream which is fed to the frosting vessel.

10. 发明公开

EP2277614A1 Verfahren zum Reinigen und Verflüssigen von Biogas 审中-公开
标题翻译： Verfahren zum Reinigen undVerflüssigenvon Biogas
公开(公告)号：EP2277614A1
公开(公告)日：2011-01-26
申请号：EP10007608.2
申请日：2010-07-22
申请人： LO Solutions GmbH
发明人： Hermeling, Werner
IPC分类号： B01D53/00 , B01D53/26 , C10L3/08 , F25J3/06
CPC分类号： B01D53/002 , B01D53/265 , B01D2256/24 , B01D2257/504 , C10L3/10 , C10L3/102 , F25J1/0022 , F25J1/004 , F25J1/0052 , F25J1/0072 , F25J1/0204 , F25J2205/20 , F25J2210/66 , F25J2220/62 , F25J2220/66 , F25J2220/68
摘要： Ein Verfahren zum Reinigen und Verflüssigen von Biogas zeichnet sich dadurch aus, dass das Biogas fraktioniert verflüssigt wird, wobei eine Abkühlung in einer ersten Stufe mit einem Wärmetauscher auf die Taupunkttemperatur von Wasser vorgenommen wird, dass in einer anschließenden mechanischen Trennung, wie z.B in einer Zyklonstufe, im Schwebezustand gebildete Feststoffe abgetrennt werden, so dass ein Anhaften an der Wandung nicht oder nur sehr beschränkt möglich ist und in wenigstens einer Kühlstufe unter Zusatz von kaltem CH 4 vorzugsweise im Anschluss an die Zyklonstufe der Druck zur Unterbindung der CO 2 -Schneebildung auf ≥ 5,6 bar eingestellt wird und die Temperatur über Wärmetauscher weiter abgesenkt wird, sodass CO 2 an verbleibenden Kondensationskeimen, wie z.B. Eiskristallen, kondensiert, worauf das verflüssigte CO 2 ausgetragen wird, das Biogas unter Verflüssigung weiter gekühlt wird und ein Teilstrom des Biogases zur Kühlung des Biogasstroms verwendet wird.
摘要翻译：用于净化和液化沼气的分馏过程包括（a）冷却至水的露点，（b）机械地除去悬浮固体而没有堵塞形成的沉积物，（c）加压至至少5.6巴，加入冷甲烷进行冷却，以防止固体二氧化碳的形成，（d）进一步冷却任何核上的CO 2，并且（e）通过进一步冷却来除去液体CO 2并液化沼气。净化和液化沼气的方法包括通过（a）用热交换器冷却到水的露点进行分馏，（b）通过机械分离除去悬浮固体，例如，在旋风分离器中，固体几乎不粘附到分隔壁上，（c）在加入冷甲烷的至少一个冷却阶段将压力调节至至少5.6巴，以防止形成固体二氧化碳，（d）通过热交换器进一步降低温度，使得CO在任何剩余的核（例如冰晶）上沉积，以及（e）通过进一步冷却来脱除液化的二氧化碳并液化沼气，同时使用一部分沼气来冷却主要沼气流。

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