公开(公告)号：EP3292363A2

公开(公告)日：2018-03-14

申请号：EP16724489.6

申请日：2016-04-08

申请人： GE Oil and Gas Inc.

发明人： KENNEDY, David, Allen ,  SALAMON, Mark, Mulherin ,  YOUNT, Christopher, Scott

IPC分类号： F25J3/02 ,  F25J3/08

CPC分类号： F25J3/0214 ,  F25J3/0219 ,  F25J3/0233 ,  F25J3/0238 ,  F25J3/08 ,  F25J2200/74 ,  F25J2205/04 ,  F25J2215/04 ,  F25J2215/62 ,  F25J2240/40 ,  F25J2245/02 ,  F25J2245/90 ,  F25J2270/12 ,  F25J2270/60

摘要： A system and process that are configured to prepare incoming hydrocarbon feedstocks for storage. For incoming ethane gas, the embodiments can utilize a plurality of vessels to distill the incoming feedstock to vapor and liquid ethane that is suitable for storage. The embodiments can direct the vapor to a demethanizer column that is downstream of the vessels and other components. The process can include stages for distilling an incoming feedstock at a plurality of vessels to form a vapor and a liquid for storage; directing the vapor to a demethanizer column; and circulating liquid from the demethanizer column back to the plurality of vessels.

公开(公告)号：EP2910298B1

公开(公告)日：2017-11-29

申请号：EP13847246.9

申请日：2013-10-01

申请人： Taiyo Nippon Sanso Corporation

发明人： KAMBE, Takashi ,  HAYASHIDA, Shigeru ,  IGARASHI, Takehiro

IPC分类号： B01D59/04 ,  B01D3/14 ,  C01B13/02 ,  F25J3/02 ,  H01M8/06 ,  B01D59/32 ,  B01D59/50

CPC分类号： B01D59/04 ,  B01D3/14 ,  B01D3/143 ,  B01D59/32 ,  B01D59/50 ,  C01B5/00 ,  C01B5/02 ,  C01B13/02 ,  C01B21/24 ,  F25J3/02 ,  F25J3/08 ,  H01M8/04156 ,  H01M8/0662

摘要： The present invention provides a method for enriching an oxygen isotope which, when distilling a large amount of a nitric oxide raw material, enables the oxygen isotope to be enriched without requiring regular replenishment of large amounts of the nitric oxide raw material and with a small liquid NO hold-up volume, without reducing the separation efficiency for the oxygen isotope. By performing a chemical exchange between a water acquired by adding hydrogen to an oxygen having a crudely enriched oxygen isotope produced by a first distillation device (11), and a nitric oxide discharged from a second distillation device (12), a nitric oxide having an enriched concentration of the oxygen isotope and a water having a reduced concentration of the oxygen isotope are obtained, and the nitric oxide having an enriched concentration of the oxygen isotope is supplied to the second distillation device (12), while an oxygen obtained by electrolysis of the water having a reduced concentration of the oxygen isotope is returned to the first distillation device (11).

公开(公告)号：EP3149418A2

公开(公告)日：2017-04-05

申请号：EP15729883.7

申请日：2015-05-28

申请人： Highview Enterprises Limited

发明人： CASTELUCCI, Nicola ,  RILEY, Richard

IPC分类号： F25J1/00 ,  F25J1/02 ,  B01D53/02 ,  F01K21/00

CPC分类号： F25J3/04387 ,  B01D53/02 ,  B01D53/0462 ,  B01D53/047 ,  B01D2259/403 ,  B01D2259/404 ,  B01D2259/41 ,  F01K5/00 ,  F01K21/00 ,  F01K25/00 ,  F16D31/02 ,  F25J1/0012 ,  F25J1/0045 ,  F25J1/02 ,  F25J1/0242 ,  F25J1/0251 ,  F25J3/08 ,  F25J2205/24 ,  F25J2205/60 ,  F25J2205/64 ,  F25J2205/66 ,  F25J2205/68 ,  F25J2230/04 ,  F25J2230/30 ,  F25J2230/40 ,  F25J2235/02 ,  F25J2240/10 ,  F25J2240/90 ,  F25J2245/40 ,  F25J2245/90

摘要： A liquid air energy storage system comprises an air liquefier, a liquid air storage facility for storing the liquefied air, and a power recovery unit coupled to the liquid air storage facility. The air liquefier comprises an air input, an adsorption air purification unit for purifying the input air, and a cold box for liquefying the purified air. The power recovery unit comprise a pump for pressurizing the liquefied air from the liquid air storage facility; an evaporator for transforming the high-pressure liquefied air into high-pressure gaseous air; an expansion turbine capable of being driven by the high-pressure gaseous air; a generator for generating electricity from the expansion turbine; and an exhaust for exhausting low-pressure gaseous air from the expansion turbine. The exhaust is coupled to the adsorption air purification unit such that at least a portion of the low-pressure gaseous air exhausted from the expansion turbine is usable to regenerate the adsorption air purification unit.

摘要翻译： 液体空气能量储存系统（LAES）包括空气液化器100,110,120，用于储存液化空气的液体空气存储设备130和耦合到液体空气存储设备的动力回收单元。 空气液化器包括空气输入口，用于净化输入空气的吸附空气净化单元（APU）110和用于液化净化空气的冷箱120。 动力回收单元包括用于对来自液体空气存储设备的液化空气加压的泵; 用于将高压液化空气转化成高压气态空气的蒸发器; 能够由高压气体空气驱动的膨胀涡轮机; 用于从膨胀涡轮发电的发电机; 以及用于从膨胀涡轮机排出低压气态空气的废气。 排气与吸附空气净化单元联接，使得从膨胀涡轮排出的低压气体空气的至少一部分可用于再生吸附空气净化单元。 还要求保护的是一种操作这种系统和空气净化单元的方法。

公开(公告)号：EP1647321B1

公开(公告)日：2017-02-08

申请号：EP05022669.5

申请日：2005-10-18

申请人： L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude ,  Air Liquide Deutschland GmbH

发明人： Kutz, Thomas ,  Stahl, Manfred ,  Schulte, Martin ,  Terkatz, Stefan

IPC分类号： B01D53/00

CPC分类号： F25J3/06 ,  B01D53/002 ,  F25J3/08 ,  F25J2210/42 ,  F25J2215/40 ,  F25J2270/904

公开(公告)号：EP2495517A4

公开(公告)日：2016-06-01

申请号：EP10837077

申请日：2010-09-28

申请人： CONSEJO SUPERIOR INVESTIGACION ,  UNIV ZARAGOZA ,  GWR INSTR INC

发明人： RILLO MILLÁN CONRADO ,  TOCADO MARTÍNEZ LETICIA

IPC分类号： F25J1/02 ,  F25J3/02

CPC分类号： F25J1/0007 ,  F25J1/0065 ,  F25J1/0225 ,  F25J1/025 ,  F25J1/0269 ,  F25J1/027 ,  F25J1/0271 ,  F25J1/0276 ,  F25J3/08 ,  F25J2220/02 ,  F25J2270/908 ,  F25J2270/912 ,  F25J2290/60 ,  F25J2290/62

摘要： A plant to recover helium without loss is described, which allows either a continuous supply of helium to equipment that require said element for refrigeration or storage of said element in a liquid state when it is not needed.

公开(公告)号：EP2781250B1

公开(公告)日：2016-05-18

申请号：EP14166817.8

申请日：2013-02-28

申请人： Kabushiki Kaisha Toshiba

发明人： KITAMURA, Hideo ,  SAITO, Satoshi ,  UDATSU, Mitsuru

IPC分类号： B01D53/14 ,  F23J15/02 ,  F25J3/08

CPC分类号： B01D53/96 ,  B01D53/1425 ,  B01D53/1475 ,  B01D53/62 ,  B01D53/78 ,  B01D2252/204 ,  B01D2252/20478 ,  B01D2257/504 ,  B01D2258/0283 ,  B01D2259/65 ,  F23J15/02 ,  F23J2215/50 ,  F23J2219/40 ,  F25D3/08 ,  F25J3/08 ,  Y02C10/06 ,  Y02E20/326

摘要： In one embodiment, a carbon dioxide recovery apparatus includes a heat exchanger which heats a first rich liquid, a flow divider which divides the first rich liquid heated by the heat exchanger into a second rich liquid and a third rich liquid, a first release device which heats the second rich liquid and discharges a first semi-lean liquid, a second release device which heats the third rich liquid and discharges a second semi-lean liquid, and a regeneration tower which heats the first and second semi-lean liquids to generate a lean liquid. The first release device heats the second rich liquid, using the lean liquid. The second release device heats the third rich liquid, using a carbon dioxide-containing steam discharged at the regeneration tower. The heat exchanger heats the first rich liquid, using the lean liquid which has passed through the first release device.

公开(公告)号：EP2867582A4

公开(公告)日：2015-12-02

申请号：EP13809797

申请日：2013-06-28

申请人： BABCOCK & WILCOX CO

发明人： MCDONALD DENNIS K ,  DARDE ARTHUR EO ,  DUBETTIER-GRENIER RICHARD

IPC分类号： F23C5/00 ,  F23L7/00

CPC分类号： B01D53/1431 ,  B01D53/002 ,  B01D53/40 ,  B01D53/75 ,  B01D2251/304 ,  B01D2251/404 ,  B01D2257/302 ,  B01D2257/404 ,  B01D2257/504 ,  B01D2257/602 ,  B01D2258/0283 ,  F23J15/02 ,  F23J15/06 ,  F23J2219/20 ,  F23J2219/70 ,  F23J2900/15061 ,  F23L7/007 ,  F25J3/067 ,  F25J3/08 ,  Y02C20/30 ,  Y02E20/326 ,  Y02E20/344

摘要： The present invention relates generally to the field of emissions control and, in particular to a new and useful method and/or system by which to control, treat and/or mitigate various liquid-based acidic compounds that are produced during oxy-combustion (e.g., during a compression step and/or cooling step) from various gaseous acid compounds and/or gaseous acid precursor compounds (e.g., SOx, NOx, etc.). In one embodiment, the present invention relates to a method and/or system by which such one or more liquid-based acid compounds are recycled into the flue gases and/or into one or more of the emissions control and/or flue gas treatment equipment of an oxy-combustion power generation system.

公开(公告)号：EP2818447A1

公开(公告)日：2014-12-31

申请号：EP13173741.3

申请日：2013-06-26

申请人： Ammonia Casale S.A.

发明人： Filippi, Ermanno ,  Ostuni, Raffaele ,  Marzari Chiesa, Damiano

IPC分类号： C01B3/02 ,  C01B3/50 ,  C01B3/58

CPC分类号： F25J3/08 ,  C01B3/025 ,  C01B3/506 ,  C01B3/586 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/0445 ,  C01B2203/046 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/0495 ,  C01B2203/068 ,  C01B2203/1235 ,  C01B2203/147 ,  F25J3/0223 ,  F25J2220/40

摘要： A process for purification of a current of hydrogen synthesis gas (100), particularly in the front-end of an ammonia plant, wherein said gas contains hydrogen and minor amounts of carbon monoxide, carbon dioxide, water and impurities, said process including steps of methanation (13) of said current (100), converting residual amounts of carbon monoxide and carbon dioxide to methane and water, dehydration (14) of the gas to remove water, and then a cryogenic purification such as liquid nitrogen wash (15), to remove methane and Argon; a corresponding plant and method for revamping an ammonia plant are also disclosed.

摘要翻译： 一种用于净化氢合成气（100）的电流的方法，特别是在氨装置的前端，其中所述气体含有氢气和少量一氧化碳，二氧化碳，水和杂质，所述方法包括以下步骤： 将所述电流（100）的甲烷化（13），将一氧化碳和二氧化碳的残余量转化为甲烷和水，将气体脱水（14）以除去水，然后进行低温纯化如液氮洗涤（15）， 去除甲烷和氩气; 还公开了用于改造氨厂的相应设备和方法。

公开(公告)号：EP2789957A1

公开(公告)日：2014-10-15

申请号：EP13163349.7

申请日：2013-04-11

申请人： Shell Internationale Research Maatschappij B.V.

发明人： Van Aken, Michiel Gijsbert ,  Wolters-Den Breejen, Mariska

IPC分类号： F25J1/00 ,  F25J1/02 ,  F25J3/06 ,  F25J3/08

CPC分类号： F25J1/0022 ,  F25J1/0035 ,  F25J1/0037 ,  F25J1/004 ,  F25J1/0042 ,  F25J1/0202 ,  F25J1/0267 ,  F25J3/061 ,  F25J3/0635 ,  F25J3/065 ,  F25J3/067 ,  F25J3/08 ,  F25J2205/02 ,  F25J2205/10 ,  F25J2205/20 ,  F25J2220/64 ,  F25J2220/66 ,  F25J2230/30 ,  F25J2235/60 ,  F25J2245/90 ,  Y02C10/12

摘要： The present invention provides a method of liquefying a contaminated hydrocarbon-containing gas stream, the method comprising at least the steps of:
(a) providing a contaminated hydrocarbon-containing gas stream (20);
(b) cooling the contaminated hydrocarbon-containing gas stream (20) in a first heat exchanger (3) thereby obtaining a cooled contaminated hydrocarbon-containing stream (40);
(c) cooling the cooled contaminated hydrocarbon-containing stream (40) in an expander (4) thereby obtaining a partially liquefied stream (70);
(d) separating the partially liquefied stream (70) in a separator (5) thereby obtaining a gaseous stream (80) and a liquid stream (90);
(e) expanding the liquid steam (90) obtained in step (d) thereby obtaining a multiphase stream (100);
(f) separating the multiphase stream (100) in a separator (7) thereby obtaining a gaseous stream (110) and a slurry stream (120);
(g) separating the slurry stream (120) in a solid/liquid separator (9) thereby obtaining a liquid hydrocarbon stream (170) and a concentrated slurry stream (140);
(h) passing the gaseous stream (80) obtained in step (d) through the first heat exchanger (3) thereby obtaining a heated gaseous stream (270); and
(i) compressing the heated gaseous stream (270) thereby obtaining a compressed gas stream (220); and
(j) combining the compressed gas stream (220) obtained in step (i) with the contaminated hydrocarbon-containing gas stream (20) provided in step (a).

摘要翻译： 本发明提供一种液化含污染烃的气流的方法，该方法至少包括以下步骤：（a）提供污染的含烃气流（20）; （b）在第一热交换器（3）中冷却被污染的含烃气流（20），从而获得冷却的含污染烃类流（40）; （c）在膨胀器（4）中冷却被冷却的含有污染烃的料流（40），由此获得部分液化物流（70）; （d）将分离器（5）中的部分液化物流（70）分离，从而获得气流（80）和液体流（90）; （e）使步骤（d）中获得的液体蒸汽（90）膨胀，从而获得多相流（100）; （f）在分离器（7）中分离多相流（100），从而获得气流（110）和浆料流（120）; （g）在固/液分离器（9）中分离浆料流（120），从而获得液态烃流（170）和浓缩浆液流（140）; （h）使步骤（d）中获得的气流（80）通过第一热交换器（3），从而获得加热的气流（270）; 和（i）压缩加热的气流（270），从而获得压缩气流（220）; 和（j）将步骤（i）中获得的压缩气流（220）与步骤（a）中提供的污染的含烃气流（20）组合。

公开(公告)号：EP2402417B1

公开(公告)日：2014-07-30

申请号：EP10745949.7

申请日：2010-02-22

申请人： Japan Oil, Gas and Metals National Corporation ,  INPEX Corporation ,  JX Nippon Oil & Energy Corporation ,  Japan Petroleum Exploration Co., Ltd. ,  Cosmo Oil Co., Ltd. ,  Nippon Steel Engineering Co., Ltd

发明人： TASAKA, Kazuhiko

IPC分类号： C10G5/06 ,  C10G2/00 ,  C10G31/06

CPC分类号： F25J3/08 ,  C10G2/30 ,  C10G31/06 ,  C10G2300/1022 ,  C10G2300/4081