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1. 发明申请

US20100243549A1 Pervaporation Assembly 有权
标题翻译：渗透汽化装置
公开(公告)号：US20100243549A1
公开(公告)日：2010-09-30
申请号：US12794445
申请日：2010-06-04
申请人： Nicholas P. Wynn , Yu Huang , Tiem Aldajani , Donald A. Fulton
发明人： Nicholas P. Wynn , Yu Huang , Tiem Aldajani , Donald A. Fulton
IPC分类号： B01D61/36
CPC分类号： B01D61/362 , B01D1/22 , B01D1/26 , B01D3/001 , B01D3/145 , B01D63/12 , B01D2311/08 , B01D2311/12 , B01D2313/38 , B01D2319/022
摘要： The invention is a pervaporation process and pervaporation equipment, using a series of membrane modules, and including inter-module reheating of the feed solution under treatment. The inter-module heating is achieved within the tube or vessel in which the modules are housed, thereby avoiding the need to repeatedly extract the feed solution from the membrane module train.
摘要翻译：本发明是一种渗透蒸发过程和渗透蒸发设备，使用一系列膜模块，并且包括处理进料溶液的模块间再加热。模块内加热是在容纳模块的管或容器中实现的，从而避免了从膜模块列反复提取进料溶液的需要。

2. 发明申请

US20080164207A1 Pervaporation process and assembly 有权
标题翻译：渗透蒸发过程和装配
公开(公告)号：US20080164207A1
公开(公告)日：2008-07-10
申请号：US11651303
申请日：2007-01-09
申请人： Nicholas P. Wynn , Yu Huang , Tiem Aldajani , Donald A. Fulton
发明人： Nicholas P. Wynn , Yu Huang , Tiem Aldajani , Donald A. Fulton
IPC分类号： B01D1/00
CPC分类号： B01D61/362 , B01D1/22 , B01D1/26 , B01D3/001 , B01D3/145 , B01D63/12 , B01D2311/08 , B01D2311/12 , B01D2313/38 , B01D2319/022
摘要： The invention is a pervaporation process and pervaporation equipment, using a series of membrane modules, and including inter-module reheating of the feed solution under treatment. The inter-module heating is achieved within the tube or vessel in which the modules are housed, thereby avoiding the need to repeatedly extract the feed solution from the membrane module train.
摘要翻译：本发明是一种渗透蒸发过程和渗透蒸发设备，使用一系列膜模块，并且包括处理进料溶液的模块间再加热。模块内加热是在容纳模块的管或容器中实现的，从而避免了从膜模块列反复提取进料溶液的需要。

3. 发明授权

US07758754B2 Pervaporation process and assembly 有权
标题翻译：渗透蒸发过程和装配
公开(公告)号：US07758754B2
公开(公告)日：2010-07-20
申请号：US11651303
申请日：2007-01-09
申请人： Nicholas P. Wynn , Yu Huang , Tiem Aldajani , Donald A. Fulton
发明人： Nicholas P. Wynn , Yu Huang , Tiem Aldajani , Donald A. Fulton
IPC分类号： B01D15/00 , C02F1/44
CPC分类号： B01D61/362 , B01D1/22 , B01D1/26 , B01D3/001 , B01D3/145 , B01D63/12 , B01D2311/08 , B01D2311/12 , B01D2313/38 , B01D2319/022
摘要： The invention is a pervaporation process and pervaporation equipment, using a series of membrane modules, and including inter-module reheating of the feed solution under treatment. The inter-module heating is achieved within the tube or vessel in which the modules are housed, thereby avoiding the need to repeatedly extract the feed solution from the membrane module train.
摘要翻译：本发明是一种渗透蒸发过程和渗透蒸发设备，使用一系列膜模块，并且包括处理进料溶液的模块间再加热。模块内加热是在容纳模块的管或容器中实现的，从而避免了从膜模块列反复提取进料溶液的需要。

4. 发明申请

US20080011157A1 Four-port gas separation membrane module assembly 有权
标题翻译：四口气体分离膜组件
公开(公告)号：US20080011157A1
公开(公告)日：2008-01-17
申请号：US11484547
申请日：2006-07-11
申请人： Nicholas P. Wynn , Donald A. Fulton , Kaaeid A. Lokhandwala , Jurgen Kaschemekat
发明人： Nicholas P. Wynn , Donald A. Fulton , Kaaeid A. Lokhandwala , Jurgen Kaschemekat
IPC分类号： B01D53/22
CPC分类号： B01D53/22 , B01D63/12 , B01D2313/12 , B01D2319/022 , B01D2319/04 , Y02C10/10
摘要： A gas-separation membrane assembly, and a gas-separation process using the assembly. The assembly incorporates multiple gas-separation membranes in an array within a single vessel or housing, and is equipped with two permeate ports, enabling permeate gas to be withdrawn from both ends of the membrane module permeate pipes.
摘要翻译：气体分离膜组件和使用该组件的气体分离方法。该组件将单个容器或壳体内的阵列中的多个气体分离膜并入，并且配备有两个渗透物口，使渗透气体能够从膜组件渗透管的两端排出。

5. 发明授权

US07758670B2 Four-port gas separation membrane module assembly 有权
标题翻译：四口气体分离膜组件
公开(公告)号：US07758670B2
公开(公告)日：2010-07-20
申请号：US11484547
申请日：2006-07-11
申请人： Nicholas P. Wynn , Donald A. Fulton , Kaaeid A. Lokhandwala , Jurgen Kaschemekat
发明人： Nicholas P. Wynn , Donald A. Fulton , Kaaeid A. Lokhandwala , Jurgen Kaschemekat
IPC分类号： B01D53/22
CPC分类号： B01D53/22 , B01D63/12 , B01D2313/12 , B01D2319/022 , B01D2319/04 , Y02C10/10
摘要： A gas-separation membrane assembly, and a gas-separation process using the assembly. The assembly incorporates multiple gas-separation membranes in an array within a single vessel or housing, and is equipped with two permeate ports, enabling permeate gas to be withdrawn from both ends of the membrane module permeate pipes.
摘要翻译：气体分离膜组件和使用该组件的气体分离方法。该组件将单个容器或壳体内的阵列中的多个气体分离膜并入，并且配备有两个渗透物口，使渗透气体能从膜组件渗透管的两端排出。

6. 发明授权

US08128787B2 Membrane-augmented distillation with pressure change to separate solvents from water 有权
标题翻译：增压蒸馏，压力变化，以将溶剂与水分离
公开(公告)号：US08128787B2
公开(公告)日：2012-03-06
申请号：US12229790
申请日：2008-08-27
申请人： Nicholas P. Wynn , Yu Huang , Masakatsu Urairi , Richard W Baker
发明人： Nicholas P. Wynn , Yu Huang , Masakatsu Urairi , Richard W Baker
IPC分类号： B01D3/00 , C07C45/82 , C07C29/80 , C07C51/44
CPC分类号： B01D61/362 , B01D53/228 , B01D71/32 , B01D71/44 , C07C29/76 , C07C51/47 , Y02E50/17 , Y10S203/08 , Y10S203/09 , Y10S203/14 , C07C31/10 , C07C31/08 , C07C31/12 , C07C53/08
摘要： Processes for removing water from organic solvents, such as ethanol. The processes include distillation in two columns operated at sequentially higher pressure, followed by treatment of the overhead vapor by one or two membrane separation steps.
摘要翻译：从有机溶剂如乙醇中除去水的方法。这些方法包括在连续较高压力下运行的两塔中进行蒸馏，然后通过一个或两个膜分离步骤处理塔顶蒸气。

7. 发明申请

US20090004713A1 Membrane-augmented distillation with pressure change to separate solvents from water 有权
标题翻译：增压蒸馏，压力变化，以将溶剂与水分离
公开(公告)号：US20090004713A1
公开(公告)日：2009-01-01
申请号：US12229790
申请日：2008-08-27
申请人： Nicholas P. Wynn , Yu Huang , Masakatsu Urairi , Richard W. Baker
发明人： Nicholas P. Wynn , Yu Huang , Masakatsu Urairi , Richard W. Baker
IPC分类号： C12P7/06 , C07C29/80 , C07C31/08 , C12P7/02
CPC分类号： B01D61/362 , B01D53/228 , B01D71/32 , B01D71/44 , C07C29/76 , C07C51/47 , Y02E50/17 , Y10S203/08 , Y10S203/09 , Y10S203/14 , C07C31/10 , C07C31/08 , C07C31/12 , C07C53/08
摘要： Processes for removing water from organic solvents, such as ethanol. The processes include distillation in two columns operated at sequentially higher pressure, followed by treatment of the overhead vapor by one or two membrane separation steps.
摘要翻译：从有机溶剂如乙醇中除去水的方法。该方法包括在连续较高压力下运行的两个塔中进行蒸馏，然后通过一个或两个膜分离步骤处理塔顶蒸气。

8. 发明授权

US08771637B2 Gas separation process for production of hydrogen by autothermal reforming of natural gas, with carbon dioxide recovery 有权
标题翻译：通过天然气自热重整生产氢气的二氧化碳回收气体分离过程
公开(公告)号：US08771637B2
公开(公告)日：2014-07-08
申请号：US13370942
申请日：2012-02-10
申请人： Nicholas P. Wynn , Douglas E Gottschlich , Haiqing Lin
发明人： Nicholas P. Wynn , Douglas E Gottschlich , Haiqing Lin
IPC分类号： C01B3/24 , C01B3/26 , C01B31/20
CPC分类号： C01B3/382 , C01B3/501 , C01B3/56 , C01B32/40 , C01B32/50 , C01B2203/0244 , C01B2203/0405 , C01B2203/043 , C01B2203/0495 , C01B2203/1241 , C01B2203/146 , C01B2203/148 , C01B2203/86 , Y02P30/30
摘要： Disclosed herein is a process for the production of hydrogen by autothermal reforming of natural gas, with simultaneous recovery of carbon dioxide using carbon dioxide-selective membrane separation. Residual gas from the hydrogen and carbon dioxide recovery is recycled back to the autothermal reformer.
摘要翻译：本文公开了一种通过天然气的自热重整生产氢的方法，同时使用二氧化碳选择性膜分离回收二氧化碳。来自氢气和二氧化碳回收的残余气体被循环回到自热重整器。

9. 发明授权

US4587111A Method of liquid-liquid extraction of gallium from a basic aqueous solution 失效
标题翻译：从碱性水溶液中液 - 液萃取镓的方法
公开(公告)号：US4587111A
公开(公告)日：1986-05-06
申请号：US669065
申请日：1984-11-07
申请人： Nicholas P. Wynn
发明人： Nicholas P. Wynn
IPC分类号： C01G15/00 , C22B3/36
CPC分类号： C01G15/003 , C22B3/0037 , C22B3/0039 , Y02P10/234
摘要： The process of liquid-liquid extraction of gallium from sodium aluminate liquor used in the Bayer alumina process, uses an organic extractant comprising a diluent and a substituted hydroxyquinoline such that gallium and some aluminum are extracted into the organic phase.In five successive steps, the organic extractant solution loaded with gallium and aluminum is first contacted with an aqueous mineral acid solution, during which the acid solution strips the loaded solution of gallium and aluminum. Next, the phases are separated and a chloride salt or hydrochloric acid is dissolved in the acidic solution of gallium and aluminum which is then contacted with an organic solvent, e.g. n-butyl acetate. Aluminum remains in the aqueous acid solution whereas the organic solvent becomes loaded with gallium.After the phases have been separated, the organic solvent is separated from gallium chloride, which forms the feed for producing pure gallium.
摘要翻译：在拜尔氧化铝工艺中使用的铝酸钠液体液体液体萃取镓的方法使用包含稀释剂和取代的羟基喹啉的有机萃取剂，使得镓和一些铝被萃取到有机相中。在连续五个步骤中，首先将装载有镓和铝的有机萃取剂溶液与无机酸水溶液接触，在此期间酸溶液将负载的镓和铝溶液剥离。接下来，将相分离，并将氯化物盐或盐酸溶解在镓和铝的酸性溶液中，然后与有机溶剂例如乙酸乙酯接触。乙酸正丁酯铝保留在酸性水溶液中，而有机溶剂装载有镓。相分离后，有机溶剂与氯化镓分离，形成纯镓的原料。

10. 发明授权

US08829059B2 Processes for the production of methanol using sweep-based membrane separation steps 有权
标题翻译：使用基于扫描的膜分离步骤生产甲醇的方法
公开(公告)号：US08829059B2
公开(公告)日：2014-09-09
申请号：US13826682
申请日：2013-03-14
申请人： Nicholas P. Wynn
发明人： Nicholas P. Wynn
IPC分类号： C07C27/10
CPC分类号： C07C29/151 , C07C29/76 , C07C31/04
摘要： Disclosed herein are methanol production processes that include a sweep-based membrane separation step using a membrane that is selective to carbon dioxide over hydrogen. Using the processes of the invention, the efficiency of methanol production from syngas is increased by reducing the compression requirements of the process and/or improving the methanol product yield. In certain embodiments, a hydrogen-rich stream is generated; this hydrogen-rich stream can be sent for other uses. An additional benefit is that the processes of the invention may debottleneck existing methanol plants if more syngas or carbon dioxide is available, allowing for feed of imported carbon dioxide into the synthesis loop. This is a way of sequestering carbon dioxide.
摘要翻译：本文公开了甲醇生产方法，其包括使用对二氧化碳对氢气有选择性的膜的基于扫描的膜分离步骤。使用本发明的方法，通过降低该方法的压缩需求和/或提高甲醇产物产率来提高合成气生产甲醇的效率。在某些实施方案中，产生富氢流; 这种富氢流可以发送用于其他用途。另外的好处是，如果更多的合成气或二氧化碳可用，本发明的方法可以对现有甲醇装置进行脱瓶，从而允许将进口的二氧化碳进料到合成循环中。这是一种隔离二氧化碳的方式。

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