ATE317965T1 - Mehrkomponenten-fluid-destillationsverfahren zur herstellung eines argon-angereicherten stroms in einem tieftemperaturluftzerlegungsverfahren - Google Patents
Mehrkomponenten-fluid-destillationsverfahren zur herstellung eines argon-angereicherten stroms in einem tieftemperaturluftzerlegungsverfahrenInfo
- Publication number
- ATE317965T1 ATE317965T1 AT00310946T AT00310946T ATE317965T1 AT E317965 T1 ATE317965 T1 AT E317965T1 AT 00310946 T AT00310946 T AT 00310946T AT 00310946 T AT00310946 T AT 00310946T AT E317965 T1 ATE317965 T1 AT E317965T1
- Authority
- AT
- Austria
- Prior art keywords
- argon
- enriched
- stream
- air separation
- producing
- Prior art date
Links
- 238000004821 distillation Methods 0.000 title abstract 5
- 238000000926 separation method Methods 0.000 title abstract 2
- 239000012530 fluid Substances 0.000 title 1
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 abstract 2
- 229910052786 argon Inorganic materials 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04654—Producing crude argon in a crude argon column
- F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
- F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
- F25J3/04703—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser being arranged in more than one vessel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/141—Fractional distillation or use of a fractionation or rectification column where at least one distillation column contains at least one dividing wall
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
- B01D3/146—Multiple effect distillation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04406—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system
- F25J3/04412—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04654—Producing crude argon in a crude argon column
- F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04654—Producing crude argon in a crude argon column
- F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
- F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
- F25J3/04678—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser cooled by oxygen enriched liquid from high pressure column bottoms
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04721—Producing pure argon, e.g. recovered from a crude argon column
- F25J3/04733—Producing pure argon, e.g. recovered from a crude argon column using a hybrid system, e.g. using adsorption, permeation or catalytic reaction
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04763—Start-up or control of the process; Details of the apparatus used
- F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
- F25J3/04896—Details of columns, e.g. internals, inlet/outlet devices
- F25J3/04933—Partitioning walls or sheets
- F25J3/04939—Vertical, e.g. dividing wall columns
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/80—Processes or apparatus using other separation and/or other processing means using membrane, i.e. including a permeation step
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/82—Processes or apparatus using other separation and/or other processing means using a reactor with combustion or catalytic reaction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/58—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being argon or crude argon
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/58—Processes or apparatus involving steps for recycling of process streams the recycled stream being argon or crude argon
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S62/00—Refrigeration
- Y10S62/902—Apparatus
- Y10S62/905—Column
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S62/00—Refrigeration
- Y10S62/923—Inert gas
- Y10S62/924—Argon
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/459,561 US6240744B1 (en) | 1999-12-13 | 1999-12-13 | Process for distillation of multicomponent fluid and production of an argon-enriched stream from a cryogenic air separation process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ATE317965T1 true ATE317965T1 (de) | 2006-03-15 |
Family
ID=23825285
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT00310946T ATE317965T1 (de) | 1999-12-13 | 2000-12-08 | Mehrkomponenten-fluid-destillationsverfahren zur herstellung eines argon-angereicherten stroms in einem tieftemperaturluftzerlegungsverfahren |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US6240744B1 (de) |
| EP (1) | EP1108965B1 (de) |
| JP (1) | JP3495329B2 (de) |
| CN (1) | CN1175234C (de) |
| AT (1) | ATE317965T1 (de) |
| CA (1) | CA2327751C (de) |
| DE (1) | DE60026000T2 (de) |
| ES (1) | ES2254110T3 (de) |
Families Citing this family (71)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10028866A1 (de) * | 2000-06-10 | 2001-12-20 | Messer Ags Gmbh | Verfahren und Vorrichtung zur Gewinnung von Argon |
| JP2003039960A (ja) | 2001-07-25 | 2003-02-13 | Jatco Ltd | 手動変速機及びその変速制御装置 |
| US6550274B1 (en) | 2001-12-05 | 2003-04-22 | Air Products And Chemicals, Inc. | Batch distillation |
| CN1646869A (zh) * | 2002-04-12 | 2005-07-27 | 林德股份公司 | 用于通过低温空气分离获取氩的方法 |
| US7691239B2 (en) * | 2002-12-04 | 2010-04-06 | Fluor Technologies Corporation | Distillation systems |
| US7501009B2 (en) * | 2006-03-10 | 2009-03-10 | Air Products And Chemicals, Inc. | Combined cryogenic distillation and PSA for argon production |
| CN101528665B (zh) * | 2006-09-28 | 2012-09-19 | 巴斯夫欧洲公司 | 制备电子级2-(2-氨基乙氧基)乙醇的方法 |
| US20100018248A1 (en) * | 2007-01-19 | 2010-01-28 | Eleanor R Fieler | Controlled Freeze Zone Tower |
| CA2674618C (en) * | 2007-01-19 | 2015-02-10 | Exxonmobil Upstream Research Company | Integrated controlled freeze zone (cfz) tower and dividing wall (dwc) for enhanced hydrocarbon recovery |
| US20090288939A1 (en) * | 2008-05-20 | 2009-11-26 | Smith Michael R | Distillation Apparatus |
| US20090288940A1 (en) * | 2008-05-20 | 2009-11-26 | Smith Michael R | Distillation Process |
| US8480860B2 (en) * | 2008-10-22 | 2013-07-09 | Air Products And Chemicals, Inc. | Divided wall columns for smaller sized plants |
| US8246816B2 (en) * | 2009-03-04 | 2012-08-21 | Uop Llc | Zone or system for providing one or more streams |
| JP5027173B2 (ja) * | 2009-03-06 | 2012-09-19 | 大陽日酸株式会社 | アルゴン製造方法およびその装置 |
| MY155414A (en) | 2009-04-20 | 2015-10-15 | Exxonmobil Upstream Res Co | Cryogenic system for removing acid gases from a hydrocarbon gas stream, and method of removing acid gases |
| MY161120A (en) | 2009-09-09 | 2017-04-14 | Exxonmobil Upstream Res Co | Cryogenic system for removing acid gases from a hydrocarbon gas stream |
| BR112012009104B1 (pt) * | 2009-10-20 | 2021-08-31 | Dow Global Technologies Llc | Processo para sintetizar pelo menos um nitroalcano, processo para a recuperação de nitroalcano e aparelho para sintetizar pelo menos um nitroalcano |
| BR112012017599A2 (pt) | 2010-01-22 | 2016-08-16 | Exxonmobil Upstream Res Co | remoção de gases ácidos de um fluxo de gás, com captura e sequestro de co2 |
| SG182399A1 (en) | 2010-02-03 | 2012-08-30 | Exxonmobil Upstream Res Co | Systems and methods for using cold liquid to remove solidifiable gas components from process gas streams |
| MX362706B (es) | 2010-07-30 | 2019-02-01 | Exxonmobil Upstream Res Company Star | Sistemas criogenicos para remover gases acidos de una corriente de gas de hidrocarburo que usan dispositivos de separacion de co-corriente. |
| WO2013070042A1 (ko) * | 2011-11-11 | 2013-05-16 | 주식회사 엘지화학 | 트리할로실란의 정제 장치 |
| WO2013070044A1 (ko) * | 2011-11-11 | 2013-05-16 | 주식회사 엘지화학 | 트리할로실란의 정제 장치 |
| KR101372617B1 (ko) * | 2011-11-11 | 2014-03-11 | 주식회사 엘지화학 | 트리할로실란의 정제 장치 |
| JP5956772B2 (ja) * | 2012-02-20 | 2016-07-27 | 東洋エンジニアリング株式会社 | 熱交換型蒸留装置 |
| ES2585062T3 (es) * | 2012-03-06 | 2016-10-03 | Air Products And Chemicals, Inc. | Relleno estructurado |
| CA2867287C (en) | 2012-03-21 | 2019-06-11 | Exxonmobil Upstream Research Company | Separating carbon dioxide and ethane from a mixed stream |
| TW201402188A (zh) * | 2012-06-11 | 2014-01-16 | Universiti Tunku Abdul Rahman | 從龍腦樹滲出物萃取龍腦的方法 |
| US9644890B2 (en) | 2013-03-01 | 2017-05-09 | Praxair Technology, Inc. | Argon production method and apparatus |
| US9302955B2 (en) | 2013-09-27 | 2016-04-05 | Uop Llc | Systems and methods for separating xylene isomers using selective adsorption |
| US9829247B2 (en) | 2013-12-06 | 2017-11-28 | Exxonmobil Upstream Reseach Company | Method and device for separating a feed stream using radiation detectors |
| WO2015084495A2 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of maintaining a liquid level in a distillation tower |
| WO2015084494A2 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and device for separating hydrocarbons and contaminants with a spray assembly |
| MY177768A (en) | 2013-12-06 | 2020-09-23 | Exxonmobil Upstream Res Co | Method and device for separating hydrocarbons and contaminants with a heating mechanism to destabilize and/or prevent adhesion of solids |
| US10139158B2 (en) | 2013-12-06 | 2018-11-27 | Exxonmobil Upstream Research Company | Method and system for separating a feed stream with a feed stream distribution mechanism |
| WO2015084497A2 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of dehydrating a feed stream processed in a distillation tower |
| MY176633A (en) | 2013-12-06 | 2020-08-19 | Exxonmobil Upstream Res Co | Method and system of modifiying a liquid level during start-up operations |
| US9874395B2 (en) | 2013-12-06 | 2018-01-23 | Exxonmobil Upstream Research Company | Method and system for preventing accumulation of solids in a distillation tower |
| US9562719B2 (en) | 2013-12-06 | 2017-02-07 | Exxonmobil Upstream Research Company | Method of removing solids by modifying a liquid level in a distillation tower |
| CA2933493A1 (en) * | 2013-12-17 | 2015-06-25 | Bp Corporation North America Inc. | Enhanced heat recovery in paraxylene plant |
| FR3017698B1 (fr) * | 2014-02-14 | 2019-03-29 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Colonne de separation d'air par distillation cryogenique, appareil de separation d'air comportant une telle colonne et procede de fabrication d'une telle colonne |
| JP6204231B2 (ja) * | 2014-03-11 | 2017-09-27 | 大陽日酸株式会社 | 空気液化分離装置及び方法 |
| US10337792B2 (en) | 2014-05-01 | 2019-07-02 | Praxair Technology, Inc. | System and method for production of argon by cryogenic rectification of air |
| US9291389B2 (en) * | 2014-05-01 | 2016-03-22 | Praxair Technology, Inc. | System and method for production of argon by cryogenic rectification of air |
| US10082333B2 (en) | 2014-07-02 | 2018-09-25 | Praxair Technology, Inc. | Argon condensation system and method |
| FR3032889A1 (fr) * | 2015-02-20 | 2016-08-26 | Air Liquide | Procede et appareil de separation a temperature subambiante |
| EA201791687A1 (ru) | 2015-02-27 | 2017-12-29 | Эксонмобил Апстрим Рисерч Компани | Снижение тепловой нагрузки и нагрузки по дегидратации подаваемого потока, поступающего в процесс криогенной перегонки |
| WO2016146238A1 (de) * | 2015-03-13 | 2016-09-22 | Linde Aktiengesellschaft | Destillationssäulen-system, anlage und verfahren zur erzeugung von sauerstoff durch tieftemperaturzerlegung von luft |
| WO2016146246A1 (de) * | 2015-03-13 | 2016-09-22 | Linde Aktiengesellschaft | Anlage zur erzeugung von sauerstoff durch tieftemperaturzerlegung von luft |
| EP3067648A1 (de) * | 2015-03-13 | 2016-09-14 | Linde Aktiengesellschaft | Destillationssäulen-system und verfahren zur erzeugung von sauerstoff durch tieftemperaturzerlegung von luft |
| US9676629B2 (en) | 2015-06-09 | 2017-06-13 | Praxair Technology, Inc. | Helium enhanced heat transfer in adsorptive liquid or gas phase argon purification processes |
| US10012438B2 (en) * | 2015-07-31 | 2018-07-03 | Praxair Technology, Inc. | Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system |
| US10066871B2 (en) * | 2015-07-31 | 2018-09-04 | Praxair Technology, Inc. | Method and apparatus for argon rejection and recovery |
| US10012437B2 (en) | 2015-07-31 | 2018-07-03 | Praxair Technology, Inc. | Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system |
| US10024596B2 (en) * | 2015-07-31 | 2018-07-17 | Praxair Technology, Inc. | Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system |
| EP3133361B1 (de) | 2015-08-20 | 2018-06-13 | Linde Aktiengesellschaft | Destillationssäulen-system und anlage zur erzeugung von sauerstoff durch tieftemperaturzerlegung von luft |
| CA2994812C (en) | 2015-09-18 | 2020-03-10 | Exxonmobil Upstream Research Company | Heating component to reduce solidification in a cryogenic distillation system |
| CA2998466C (en) | 2015-09-24 | 2021-06-29 | Exxonmobil Upstream Research Company | Treatment plant for hydrocarbon gas having variable contaminant levels |
| DE102015014676A1 (de) * | 2015-11-16 | 2017-06-01 | Julius Montz Gmbh | Kolonne mit zylindrischer Trennwand |
| US9925514B2 (en) | 2016-02-22 | 2018-03-27 | Air Products And Chemicals, Inc. | Modified chabazite adsorbent compositions, methods of making and using them |
| US9669349B1 (en) | 2016-02-22 | 2017-06-06 | Air Products And Chemicals, Inc. | Modified chabazite adsorbent compositions, methods of making and using them |
| US9708188B1 (en) | 2016-02-22 | 2017-07-18 | Air Products And Chemicals, Inc. | Method for argon production via cold pressure swing adsorption |
| EP3423170B1 (de) * | 2016-03-01 | 2021-05-26 | Praxair Technology, Inc. | Verfahren und vorrichtung zur argonrückgewinnung in einer mit einem druckwechseladsorptionssystem integrierten kryogenen lufttrennungsanlage |
| CA3024545C (en) | 2016-03-30 | 2020-08-25 | Exxonmobile Upstream Research Company | Self-sourced reservoir fluid for enhanced oil recovery |
| CN107080965A (zh) * | 2017-04-26 | 2017-08-22 | 华东理工大学 | 一种分壁精馏塔 |
| US10684071B2 (en) | 2017-08-25 | 2020-06-16 | Praxair Technology, Inc. | Annular divided wall column for an air separation unit |
| US10578357B2 (en) * | 2017-08-25 | 2020-03-03 | Praxair Technology, Inc. | Annular divided wall column with ring shaped collectors and distributers for an air separation unit |
| US11262125B2 (en) | 2018-01-02 | 2022-03-01 | Praxair Technology, Inc. | System and method for flexible recovery of argon from a cryogenic air separation unit |
| WO2020005553A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company (Emhc-N1.4A.607) | Mixing and heat integration of melt tray liquids in a cryogenic distillation tower |
| WO2020005552A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company | Hybrid tray for introducing a low co2 feed stream into a distillation tower |
| FR3102548B1 (fr) * | 2019-10-24 | 2023-03-10 | Air Liquide | Procédé et appareil de séparation d’air par distillation cryogénique |
| WO2022106685A1 (de) * | 2020-11-23 | 2022-05-27 | Covestro Deutschland Ag | Destillationseinheit und verfahren zur trennung eines flüssigen stoffgemisches in 2 bis 6 flüssige produktströme unterschiedlicher zusammensetzung |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2471134A (en) | 1946-07-17 | 1949-05-24 | Standard Oil Dev Co | Fractionation apparatus |
| US3100697A (en) * | 1960-08-01 | 1963-08-13 | Gas Proc Inc | Apparatus for treatment of natural gas |
| US3844898A (en) * | 1973-01-02 | 1974-10-29 | Universal Oil Prod Co | Fractionation apparatus having plural, integral and concentric fractionating units |
| DE3327952A1 (de) * | 1983-08-03 | 1985-02-14 | Basf Ag, 6700 Ludwigshafen | Verfahren zur destillativen zerlegung eines azeotropen stoffgemisches - analog einer extraktivdestillation - mittels einer destillationskolonne |
| US5339648A (en) * | 1993-08-05 | 1994-08-23 | Praxair Technology, Inc. | Distillation system with partitioned column |
| DE4418488A1 (de) * | 1994-05-27 | 1995-11-30 | Basf Ag | Verfahren und Vorrichtung zur destillativen Trennung von Stoffgemischen |
| US5755933A (en) * | 1995-07-24 | 1998-05-26 | The M. W. Kellogg Company | Partitioned distillation column |
| US5946942A (en) * | 1998-08-05 | 1999-09-07 | Praxair Technology, Inc. | Annular column for cryogenic rectification |
| DE19849651C2 (de) * | 1998-10-29 | 2003-01-16 | Krupp Uhde Gmbh | Rektifizierkolonne für die Extraktivdestillation von eng- oder azeotrop siedenden Gemischen |
| JP3329750B2 (ja) | 1998-11-05 | 2002-09-30 | 住友重機械工業株式会社 | 蒸留装置及びその蒸留方法 |
-
1999
- 1999-12-13 US US09/459,561 patent/US6240744B1/en not_active Expired - Lifetime
-
2000
- 2000-12-07 CA CA002327751A patent/CA2327751C/en not_active Expired - Fee Related
- 2000-12-08 AT AT00310946T patent/ATE317965T1/de not_active IP Right Cessation
- 2000-12-08 ES ES00310946T patent/ES2254110T3/es not_active Expired - Lifetime
- 2000-12-08 DE DE60026000T patent/DE60026000T2/de not_active Expired - Lifetime
- 2000-12-08 EP EP00310946A patent/EP1108965B1/de not_active Expired - Lifetime
- 2000-12-13 JP JP2000378598A patent/JP3495329B2/ja not_active Expired - Fee Related
- 2000-12-13 CN CNB001349570A patent/CN1175234C/zh not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| CN1300930A (zh) | 2001-06-27 |
| CN1175234C (zh) | 2004-11-10 |
| JP3495329B2 (ja) | 2004-02-09 |
| EP1108965B1 (de) | 2006-02-15 |
| DE60026000D1 (de) | 2006-04-20 |
| US6240744B1 (en) | 2001-06-05 |
| EP1108965A1 (de) | 2001-06-20 |
| CA2327751A1 (en) | 2001-06-13 |
| CA2327751C (en) | 2003-12-30 |
| DE60026000T2 (de) | 2006-10-26 |
| ES2254110T3 (es) | 2006-06-16 |
| JP2001224901A (ja) | 2001-08-21 |
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