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91. 发明公开

EP0913180A3 Distillation process to separate mixtures containing three or more components 有权
标题翻译：对于三个或更多个组分的混合物分离蒸馏过程
公开(公告)号：EP0913180A3
公开(公告)日：2002-04-03
申请号：EP98308686.9
申请日：1998-10-23
申请人： AIR PRODUCTS AND CHEMICALS, INC.
发明人： Agrawal, Rakesh , Fidkowski, Zbigniew Tadeusz
IPC分类号： B01D3/14
CPC分类号： B01D3/146 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J3/0247 , F25J3/0257 , F25J3/0261 , F25J3/0295 , F25J3/044 , F25J3/0466 , F25J3/04709 , F25J3/04793 , F25J2200/02 , F25J2200/30 , F25J2200/38 , F25J2200/50 , F25J2200/72 , F25J2210/12 , F25J2215/62 , F25J2215/64 , F25J2215/66 , F25J2290/40 , Y10S62/924 , Y10S62/927
摘要： The heat requirement of conventional distillation processes which separate feed mixtures containing three or more components is reduced by sending a liquid bottoms stream 20 (or gaseous overhead stream 230) containing two or more components from an earlier column to a subsequent column and returning a vapor stream 227 (or liquid stream 337) between the same locations in the two columns. A portion 24 (234) of the liquid bottoms stream 20 (overhead vapor stream 230) is at least partially vaporized (condensed) prior to feeding to the second column or heat is added (removed) from the second column between the feed location of the entire liquid stream 20 (gaseous stream 230) and the bottom (top) of the second column.

92. 发明公开

EP1189000A2 Dephlegmator system and process 有权
标题翻译：装置和方法与分馏塔
公开(公告)号：EP1189000A2
公开(公告)日：2002-03-20
申请号：EP01120800.6
申请日：2001-09-11
申请人： AIR PRODUCTS AND CHEMICALS, INC.
发明人： Howard, Lee Jarvis , Rowles, Howard Charles , Nickel, Randy James , Lucadamo, Gene Anthony , Hill, Bruce Moodie
IPC分类号： F25J3/02
CPC分类号： F25J3/0238 , F25J3/0209 , F25J3/0219 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J3/0257 , F25J3/0261 , F25J3/0295 , F25J5/007 , F25J2200/80 , F25J2210/12 , F25J2250/10 , F25J2250/20 , F25J2270/12 , F25J2270/66 , F25J2290/30 , F25J2290/50 , F28D9/0068 , Y10S62/903
摘要： Dephlegmator system without headers, collectors, or distributors at the bottom end of feed circuits in plate and fin exchangers operating in condensing or rectifying service. Each dephlegmator is installed within a pressure vessel, thereby eliminating the need for headers, collectors, or distributors at the bottom end of the feed circuits. In an alternative embodiment of the invention, upper and lower segments of the pressure vessel are isolated by a mid-vessel seal between the vessel and dephlegmator walls, and headers or collectors are not required at the upper and lower ends of the feed circuits.

93. 发明公开

EP1118827A1 Procédé de liquéfaction partielle d'un fluide contenant des hydrocarbures tel que du gaz naturel 有权
标题翻译： Verfahren zur partiellenVerflüssigungeiner kohlenwasserstoffreichen Fraktion wie Erdgas
公开(公告)号：EP1118827A1
公开(公告)日：2001-07-25
申请号：EP01400050.9
申请日：2001-01-10
申请人： INSTITUT FRANCAIS DU PETROLE
发明人： Fischer, Béatrice
IPC分类号： F25J1/02
CPC分类号： F25J3/0242 , F25J1/0022 , F25J1/0035 , F25J1/004 , F25J1/0042 , F25J1/0045 , F25J1/0052 , F25J1/0212 , F25J1/0219 , F25J1/023 , F25J1/0231 , F25J1/0237 , F25J1/0241 , F25J1/025 , F25J1/0255 , F25J1/0284 , F25J1/0291 , F25J1/0292 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J2200/04 , F25J2200/70 , F25J2200/74 , F25J2205/02 , F25J2210/04 , F25J2210/06 , F25J2215/62 , F25J2215/64 , F25J2220/60 , F25J2220/62 , F25J2220/68 , F25J2230/08 , F25J2230/32 , F25J2235/60 , F25J2240/30 , F25J2240/40 , F25J2240/80 , F25J2245/02 , F25J2270/12 , F25J2270/66 , F25J2290/34
摘要： Procédé de liquéfaction partielle d'un fluide G formé au moins en partie d'hydrocarbures, produisant simultanément :

une fraction liquide après détente
une fraction gazeuse représentant au moins 10 % poids, qui pourra être soit réinjectée, soit utilisée pour produire de l'électricité.
et comportant au moins deux étapes de réfrigération au cours desquelles :

dans la première étape a) on refroidit le fluide G essentiellement gazeux à l'aide d'un réfrigérant externe M pour qu'à l'issue de cette première étape il soit au moins partiellement liquide à la pression opératoire et
dans la deuxième étape b) on termine si nécessaire la liquéfaction dudit fluide G et on sous refroidit ledit fluide G, à l'aide d'une partie du même fluide G, ladite partie étant ainsi détendue et vaporisée de manière à produire le froid nécessaire pour récupérer l'autre partie dudit fluide G totalement liquide à la pression du stockage.
摘要翻译：在两个制冷阶段部分液化烃的气体混合物液化混合物的≤90wt％。一些残余气体用于发电。第一个制冷阶段使用外部制冷剂。在第二阶段，通过膨胀和蒸发一些冷却的流体产生冷却。包括如上所述的用于部分液化天然气的另外的方法的独立权利要求。在第一阶段结束时，气体被冷却到-40℃以下。优选的特征：20-80重量％的混合物被液化。在第一阶段结束时产生的液体是单一或密相。将残余气体注入气井，以改善井的产量。来自第二阶段的膨胀和蒸发的流体仍然被充分加压，用于驱动发电机的燃气轮机或冷却并送到两个分馏塔中的第一台的底部。

94. 发明公开

EP1114808A1 Hydrocarbon separation process and apparatus 有权
标题翻译： Verfahren und Vorrichtung zur Trennung von Kohlenwasserstoffen
公开(公告)号：EP1114808A1
公开(公告)日：2001-07-11
申请号：EP01300132.6
申请日：2001-01-08
申请人： Costain Oil, Gas & Process Limited
发明人： Finn, Adrian Joseph , Johnson, Grant Leigh
IPC分类号： C07C7/00 , F25J3/02
CPC分类号： C10G5/06 , C07C7/005 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2200/04 , F25J2200/74 , F25J2200/76 , F25J2200/78 , F25J2205/04 , F25J2210/12 , F25J2230/60 , F25J2240/02 , F25J2245/02 , F25J2270/02 , F25J2270/90
摘要： A process is described for separating the heavier hydrocarbons from a gaseous hydrocarbon feed wherein a first separator is employed to separate partially condensed gaseous feed and wherein the vapour portion undergoes work expansion and is fed to a fractionation column. The liquid portion is subcooled in heat exchange with the overhead vapour from the fractionation column, expanded, evaporated to provide refrigeration at a low temperature level, and fed to the fractionation column. The rewarmed residual vapour is subsequently compressed to a pressure suitable for export, with a portion of the compressed gas being cooled, condensed and recycled back to reflux the top section of the fractionation column.
Also described is a process wherein a first separator is employed to separate partially condensed gaseous feed and wherein the vapour portion undergoes work expansion and is fed to a high pressure wash column. The liquid portion is expanded and fed to the base of the high pressure wash column. Bottoms liquid from the wash column is subcooled in heat exchange with the overhead vapour from a fractionation column, expanded, evaporated to provide refrigeration at a low temperature level, and fed to the fractionation column. Vapour from the high pressure wash column is partially condensed, with the liquid portion used to provide reflux to the high pressure wash column and the fractionation column.
The processes are especially applicable to recovery of ethane and heavier components from natural gas. Overall process power requirements are reduced, recovery of the desired heavy hydrocarbons is increased or both of these effects are realised.
摘要翻译：描述了用于从气态烃进料分离较重烃的方法，其中使用第一分离器分离部分冷凝的气态进料，并且其中蒸气部分经历工作膨胀并进料至分馏塔。液体部分与来自分馏塔的塔顶蒸气热交换过冷，膨胀，蒸发以在低温水平提供制冷，并进料至分馏塔。随后将再热的残余蒸气压缩至适于出口的压力，一部分压缩气体被冷却，冷凝并再循环回到分馏塔的顶部部分。还描述了一种方法，其中使用第一分离器来分离部分冷凝的气态进料，并且其中蒸气部分经历工作膨胀并进料到高压洗涤塔。液体部分膨胀并进料到高压洗涤塔的底部。来自洗涤塔的底部液体与来自分馏塔的塔顶蒸气热交换过冷，膨胀，蒸发以在低温水平提供制冷，并进料至分馏塔。来自高压洗涤塔的蒸汽部分冷凝，液体部分用于向高压洗涤塔和分馏塔提供回流。该方法特别适用于从天然气中回收乙烷和较重的组分。总体处理能力要求降低，期望的重质烃的回收率增加或者这两种效应都实现。

95. 发明授权

EP0748765B1 Installation de production de monoxyde de carbone incorporant une unité de séparation cryogénique 失效
标题翻译：植物用于生产一氧化碳，具有深冷分离装置
公开(公告)号：EP0748765B1
公开(公告)日：1999-08-11
申请号：EP96401278.5
申请日：1996-06-12
申请人： L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE
发明人： Billy, Jean
IPC分类号： C01B31/18 , F25J3/08
CPC分类号： F25J3/0261 , C01B32/40 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J2205/60 , F25J2280/02 , Y10S62/908 , Y10S62/92

96. 发明公开

EP0875486A3 Process producing ammonia and recovering argon using low purity oxygen 失效
标题翻译：一种用于生产氨和氩的回收过程中，所使用的低纯度氧
公开(公告)号：EP0875486A3
公开(公告)日：1999-05-26
申请号：EP98107966.8
申请日：1998-04-30
申请人： PRAXAIR TECHNOLOGY, INC.
发明人： Drnevich, Raymond Francis , Fisher, Theodore Fringelin
IPC分类号： C01B3/02 , C01B23/00
CPC分类号： F25J3/04587 , C01B3/025 , F25J3/0223 , F25J3/0233 , F25J3/0276 , F25J3/0285 , F25J3/04539 , F25J3/04545 , F25J2200/06 , F25J2200/74 , F25J2200/78 , F25J2205/02 , F25J2205/30 , F25J2205/82 , F25J2210/42 , F25J2270/904 , Y10S62/924 , Y10S62/934
摘要： A process for producing ammonia synthesis gas and recovering argon in conjunction with a low-purity oxygen separating unit.

97. 发明公开

EP0895961A1 Process and apparatus for separating a gaseous mixture 失效
标题翻译： Verfahren und Vorrichtung zur Trennung einer Gasmischung
公开(公告)号：EP0895961A1
公开(公告)日：1999-02-10
申请号：EP98305916.3
申请日：1998-07-24
申请人： AIR PRODUCTS AND CHEMICALS, INC.
发明人： McNeil, Brian Alfred , Truscott, Alan Geoffrey
IPC分类号： C01B3/50 , F25J3/02 , C01B31/18
CPC分类号： C01B3/506 , C01B32/40 , C01B2203/047 , C01B2203/048 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J3/0261 , F25J2200/76 , F25J2200/78 , F25J2200/94 , F25J2205/30 , Y10S62/92 , Y10S62/932
摘要： Hydrogen (4), and carbon monoxide (21) are separated from a gaseous mixture thereof, typically a mixture of essentially hydrogen, carbon monoxide and methane (1) using liquid methane (3) to dissolve carbon monoxide in a methane wash column (2), removing (8) residual hydrogen (15) from the loaded methane wash (6), and separating (18) the residual loaded methane into carbon monoxide and methane fractions (21,22). The residual hydrogen (15) is removed in a hydrogen stripping column (8), said column being refluxed with a methane rich scrubbing liquid stream (13) withdrawn from an intermediate location of the methane wash column (2).
摘要翻译：氢气（4）和一氧化碳（21）与其气体混合物（通常为基本上为氢气，一氧化碳和甲烷的混合物）（1）分离，使用液体甲烷（3）将一氧化碳溶解在甲烷洗涤塔（2 ），从负载的甲烷洗涤（6）中除去（8）残余氢气（15），并将残余的负载甲烷分离成（18）为一氧化碳和甲烷馏分（21,22）。在氢汽提塔（8）中除去残余氢（15），所述塔与从甲烷洗涤塔（2）的中间位置排出的富含甲烷的洗涤液流（13）一起回流。

98. 发明公开

EP0883786A1 REDUCING THE AMOUNT OF COMPONENTS HAVING LOW BOILING POINTS IN LIQUEFIED NATURAL GAS 失效
标题翻译：在液体SPAN GAS减少光沸点组分
公开(公告)号：EP0883786A1
公开(公告)日：1998-12-16
申请号：EP97905128.0
申请日：1997-02-27
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
发明人： ELION, Wiveka, Jacoba , KLEIN NAGELVOORT, Robert , VINK, Kornelis, Jan
IPC分类号： F25J3
CPC分类号： F25J3/029 , F25J3/0209 , F25J3/0233 , F25J3/0257 , F25J2200/02 , F25J2200/40 , F25J2200/70 , F25J2200/90 , F25J2205/04 , F25J2215/04 , F25J2240/30 , F25J2240/40 , F25J2270/02
摘要： Method of reducing the amount of components having low boiling points in liquefied natural gas (1) comprising passing the liquefied natural gas at liquefaction pressure through the hot side (2) of an external heat exchanger (3) to obtain cooled liquefied natural gas (6), allowing the cooled liquefied natural gas to expand dynamically (9) to an intermediate pressure and statically (10) to a low pressure to obtain expanded fluid (15), and introducing expanded fluid into the upper part of a fractionation column (20) provided with a contacting section (25) arranged between the upper part and the lower part of the fractionation column; passing a direct side stream (32) at low pressure through the cold side (30) of the external heat exchanger (3) to obtain heated two-phase fluid (36); introducing the heated two-phase fluid into the lower part (28) of the fractionation column (20) and allowing the vapour to flow upwards through the contacting section (25); allowing the liquid of the expanded fluid to flow downwards through the contacting section (25); and withdrawing from the lower part of the fractionation column (20) a liquid product stream (45) having a reduced content of components having low boiling points, and from the upper part of the fractionation column a gas stream (47) which is enriched in components having low boiling points.

99. 发明公开

EP0875486A2 Process producing ammonia and recovering argon using low purity oxygen 失效
标题翻译：一种用于生产氨和氩的回收过程中，所使用的低纯度氧
公开(公告)号：EP0875486A2
公开(公告)日：1998-11-04
申请号：EP98107966.8
申请日：1998-04-30
申请人： PRAXAIR TECHNOLOGY, INC.
发明人： Drnevich, Raymond Francis , Fisher, Theodore Fringelin
IPC分类号： C01B3/02 , C01B23/00
CPC分类号： F25J3/04587 , C01B3/025 , F25J3/0223 , F25J3/0233 , F25J3/0276 , F25J3/0285 , F25J3/04539 , F25J3/04545 , F25J2200/06 , F25J2200/74 , F25J2200/78 , F25J2205/02 , F25J2205/30 , F25J2205/82 , F25J2210/42 , F25J2270/904 , Y10S62/924 , Y10S62/934
摘要： A process for producing ammonia synthesis gas and recovering argon in conjunction with a low-purity oxygen separating unit.

100. 发明授权

EP0677483B1 Procédé et installation de séparation d'un mélange gazeux 失效
标题翻译：用于气体混合物的分离方法和装置
公开(公告)号：EP0677483B1
公开(公告)日：1998-09-02
申请号：EP95400753.0
申请日：1995-04-04
申请人： L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE
发明人： Billy, Jean , Granier, François , Victor, Pascal
IPC分类号： C01B3/50 , F25J3/02 , C01B31/18
CPC分类号： F25J3/0261 , C01B3/506 , C01B32/40 , C01B2203/047 , C01B2203/048 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J2200/70 , F25J2200/74 , F25J2205/04 , F25J2270/12 , F25J2270/14 , F25J2270/40 , F25J2270/42 , F25J2270/50 , F25J2270/58 , F25J2270/60

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