CL2012003512A1 - Un proceso y reactor para la remoción selectiva de un producto gaseoso de un sistema gaseoso, que comprende dicho producto y otros componentes, donde el sistema gaseoso se admite a un primer ambiente el cual esta separado de un segundo ambiente por una pared limite y una membrana de permeabilidad, un campo electrico espacialmente no uniforme se genera entre un primer electrodo y un segundo electrodo, donde las lineas de campo cruzan dicha membrana. - Google Patents
Un proceso y reactor para la remoción selectiva de un producto gaseoso de un sistema gaseoso, que comprende dicho producto y otros componentes, donde el sistema gaseoso se admite a un primer ambiente el cual esta separado de un segundo ambiente por una pared limite y una membrana de permeabilidad, un campo electrico espacialmente no uniforme se genera entre un primer electrodo y un segundo electrodo, donde las lineas de campo cruzan dicha membrana.Info
- Publication number
- CL2012003512A1 CL2012003512A1 CL2012003512A CL2012003512A CL2012003512A1 CL 2012003512 A1 CL2012003512 A1 CL 2012003512A1 CL 2012003512 A CL2012003512 A CL 2012003512A CL 2012003512 A CL2012003512 A CL 2012003512A CL 2012003512 A1 CL2012003512 A1 CL 2012003512A1
- Authority
- CL
- Chile
- Prior art keywords
- gaseous
- membrane
- electrode
- environment
- product
- Prior art date
Links
- 239000012528 membrane Substances 0.000 title abstract 4
- 230000005684 electric field Effects 0.000 title abstract 2
- 230000035699 permeability Effects 0.000 title abstract 2
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
- B01D53/323—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00 by electrostatic effects or by high-voltage electric fields
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
- B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
- B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0242—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical
- B01J8/0257—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical in a cylindrical annular shaped bed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0403—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal
- B01J8/0407—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds
- B01J8/0415—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds the beds being superimposed one above the other
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0417—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor
- C01C1/0441—Reactors with the catalyst arranged in tubes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0458—Separation of NH3
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/42—Catalysts within the flow path
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0001—Separation or purification processing
- C01B2210/0009—Physical processing
- C01B2210/001—Physical processing by making use of membranes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0001—Separation or purification processing
- C01B2210/0009—Physical processing
- C01B2210/001—Physical processing by making use of membranes
- C01B2210/0012—Physical processing by making use of membranes characterised by the membrane
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0046—Nitrogen
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0053—Hydrogen
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Inorganic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Un proceso y reactor para la remoción selectiva de un producto gaseoso de un sistema gaseoso, que comprende dicho producto y otros componentes, donde el sistema gaseoso se admite a un primer ambiente el cual está separado de un segundo ambiente por una pared límite y una membrana de permeabilidad, un campo eléctrico espacialmente no uniforme se genera entre un primer electrodo y un segundo electrodo, donde las líneas de campo cruzan dicha membrana.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP10168010A EP2402074A1 (en) | 2010-06-30 | 2010-06-30 | A process for selective removal of reaction products from a gaseous system |
Publications (1)
Publication Number | Publication Date |
---|---|
CL2012003512A1 true CL2012003512A1 (es) | 2013-05-17 |
Family
ID=43244959
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CL2012003512A CL2012003512A1 (es) | 2010-06-30 | 2012-12-12 | Un proceso y reactor para la remoción selectiva de un producto gaseoso de un sistema gaseoso, que comprende dicho producto y otros componentes, donde el sistema gaseoso se admite a un primer ambiente el cual esta separado de un segundo ambiente por una pared limite y una membrana de permeabilidad, un campo electrico espacialmente no uniforme se genera entre un primer electrodo y un segundo electrodo, donde las lineas de campo cruzan dicha membrana. |
Country Status (12)
Country | Link |
---|---|
US (1) | US8871063B2 (es) |
EP (2) | EP2402074A1 (es) |
CN (1) | CN102958594B (es) |
AU (1) | AU2011273749B2 (es) |
BR (1) | BR112013000060B1 (es) |
CA (1) | CA2800437C (es) |
CL (1) | CL2012003512A1 (es) |
MX (1) | MX2012014026A (es) |
MY (1) | MY164017A (es) |
RU (1) | RU2597921C2 (es) |
UA (1) | UA111943C2 (es) |
WO (1) | WO2012000771A1 (es) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103463984B (zh) * | 2013-09-10 | 2015-05-13 | 内蒙古天一环境技术有限公司 | 一种介电电泳中空纤维膜组件 |
CN103480277B (zh) * | 2013-10-09 | 2015-07-01 | 内蒙古天一环境技术有限公司 | 一种介电电泳平板渗透膜组件 |
CN104165079B (zh) * | 2014-08-22 | 2017-11-21 | 阮海生 | 一种汽车尾气净化系统 |
US20160251228A1 (en) * | 2015-02-26 | 2016-09-01 | Khalid T. Alkusayer | Ammonia synthesis for fertilizer production |
FR3033266B1 (fr) * | 2015-03-05 | 2017-03-03 | Ifp Energies Now | Ensemble de collecte d'un fluide gazeux pour reacteur radial |
CN112619565A (zh) * | 2019-10-09 | 2021-04-09 | 中国科学院大连化学物理研究所 | 低温等离子体结合催化剂诱导甲烷/天然气直接制低碳烃类的装置及方法 |
CN111111429A (zh) * | 2019-12-16 | 2020-05-08 | 山东金城柯瑞化学有限公司 | 一种利用单活性中心多相催化剂技术治理乙酰呋喃氧化尾气的方法 |
CN110976093B (zh) * | 2019-12-20 | 2021-12-07 | 付聪 | 基于非匀强电场的静电集尘装置 |
CN113277598B (zh) * | 2021-06-28 | 2022-07-12 | 重庆工商大学 | 一种电场联合波纹板聚结处理含油废水的方法和装置 |
CN115155332B (zh) * | 2022-07-07 | 2023-12-19 | 南京大学 | 一种低压电场耦合导电超滤膜原位抗膜污染的方法 |
CN115524411B (zh) * | 2022-08-18 | 2024-07-26 | 张述新 | 气体组分鉴定装置和方法 |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3489670A (en) * | 1964-07-29 | 1970-01-13 | Gen Electric | Process for gas purification |
US4795617A (en) * | 1984-01-16 | 1989-01-03 | Hare Louis R O | Electroluminescent chemical activation system |
US4735780A (en) | 1986-07-15 | 1988-04-05 | The M. W. Kellogg Company | Ammonia synthesis converter |
US4762535A (en) * | 1987-06-02 | 1988-08-09 | Air Products And Chemicals, Inc. | Ammonia separation using semipermeable membranes |
JPH022819A (ja) * | 1988-03-04 | 1990-01-08 | Matsushita Electric Works Ltd | 気体の膜分離法 |
JPH026817A (ja) | 1988-06-24 | 1990-01-11 | Matsushita Electric Works Ltd | 気体の膜分離法 |
US4999998A (en) * | 1989-01-17 | 1991-03-19 | E-Quad, Inc. | Method and apparatus for elimination of toxic oxides from exhaust gases |
US5609736A (en) * | 1995-09-26 | 1997-03-11 | Research Triangle Institute | Methods and apparatus for controlling toxic compounds using catalysis-assisted non-thermal plasma |
DE69829549T2 (de) | 1998-01-16 | 2006-03-23 | Ammonia Casale S.A. | Verfahren zur in-situ Modernisierung eines heterogenen Synthesereaktors |
US6296686B1 (en) * | 1998-06-03 | 2001-10-02 | Praxair Technology, Inc. | Ceramic membrane for endothermic reactions |
GB0015952D0 (en) * | 2000-06-30 | 2000-08-23 | Aea Technology Plc | Plasma assisted reactor |
DE10111560C1 (de) * | 2001-03-10 | 2002-06-06 | Xcellsis Gmbh | Verfahren und Vorrichtung zur Entfernung von Kohlenmonoxid aus einem Gasstrom |
GB0502227D0 (en) * | 2005-02-03 | 2005-03-09 | Thermal Energy Systems Ltd | Gas separation and compresssion device |
US20080029395A1 (en) * | 2006-08-01 | 2008-02-07 | Gas Technology Institute | Multi-functional filtration and ultra-pure water generator |
SE530266C2 (sv) * | 2006-06-16 | 2008-04-15 | Morphic Technologies Ab Publ | Förfarande och reaktor för framställning av metanol |
JP5037877B2 (ja) | 2006-08-25 | 2012-10-03 | 日本碍子株式会社 | 選択透過膜型反応器及び水素ガスの製造方法 |
WO2009025835A1 (en) | 2007-08-21 | 2009-02-26 | Regents Of The University Of Minnesota | Non-thermal plasma synthesis of ammonia |
WO2010088579A2 (en) | 2009-01-30 | 2010-08-05 | The Ohio State University Research Foundation | Selective ultrafiltration memberanes for renal replacement therapies |
-
2010
- 2010-06-30 EP EP10168010A patent/EP2402074A1/en not_active Withdrawn
-
2011
- 2011-06-10 BR BR112013000060-0A patent/BR112013000060B1/pt active IP Right Grant
- 2011-06-10 CN CN201180032948.XA patent/CN102958594B/zh active Active
- 2011-06-10 MY MYPI2012005017A patent/MY164017A/en unknown
- 2011-06-10 AU AU2011273749A patent/AU2011273749B2/en active Active
- 2011-06-10 WO PCT/EP2011/059655 patent/WO2012000771A1/en active Application Filing
- 2011-06-10 MX MX2012014026A patent/MX2012014026A/es active IP Right Grant
- 2011-06-10 EP EP11726111.5A patent/EP2588225B1/en active Active
- 2011-06-10 RU RU2013103744/05A patent/RU2597921C2/ru active
- 2011-06-10 CA CA2800437A patent/CA2800437C/en active Active
- 2011-06-10 US US13/697,724 patent/US8871063B2/en active Active
- 2011-10-06 UA UAA201300943A patent/UA111943C2/uk unknown
-
2012
- 2012-12-12 CL CL2012003512A patent/CL2012003512A1/es unknown
Also Published As
Publication number | Publication date |
---|---|
UA111943C2 (uk) | 2016-07-11 |
AU2011273749B2 (en) | 2015-07-02 |
US20130087444A1 (en) | 2013-04-11 |
EP2588225A1 (en) | 2013-05-08 |
RU2013103744A (ru) | 2014-08-10 |
BR112013000060B1 (pt) | 2019-02-12 |
CN102958594B (zh) | 2016-11-16 |
AU2011273749A1 (en) | 2012-12-06 |
CA2800437A1 (en) | 2012-01-05 |
BR112013000060A2 (pt) | 2016-05-10 |
MY164017A (en) | 2017-11-15 |
US8871063B2 (en) | 2014-10-28 |
MX2012014026A (es) | 2013-02-12 |
CN102958594A (zh) | 2013-03-06 |
WO2012000771A1 (en) | 2012-01-05 |
RU2597921C2 (ru) | 2016-09-20 |
EP2588225B1 (en) | 2018-02-28 |
CA2800437C (en) | 2018-08-28 |
EP2402074A1 (en) | 2012-01-04 |
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