NO312857B1 - Fremgangsmåte ved separasjon av en flerkomponent gasström inneholdende minst en frysbar komponent - Google Patents
Fremgangsmåte ved separasjon av en flerkomponent gasström inneholdende minst en frysbar komponent Download PDFInfo
- Publication number
- NO312857B1 NO312857B1 NO19996556A NO996556A NO312857B1 NO 312857 B1 NO312857 B1 NO 312857B1 NO 19996556 A NO19996556 A NO 19996556A NO 996556 A NO996556 A NO 996556A NO 312857 B1 NO312857 B1 NO 312857B1
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- Norway
- Prior art keywords
- stream
- separation system
- cooling
- distillation
- compressed
- Prior art date
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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
- F25J3/0228—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 characterised by the separated product stream
- F25J3/0247—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 characterised by the separated product stream separation of CnHm with 4 carbon atoms or more
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- 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
- F25J3/0204—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 characterised by the feed stream
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- F25J3/0228—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 characterised by the separated product stream
- F25J3/0233—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 characterised by the separated product stream separation of CnHm with 1 carbon atom or more
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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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/62—Details of storing a fluid in a tank
-
- 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
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)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Gas Separation By Absorption (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US5146097P | 1997-07-01 | 1997-07-01 | |
| PCT/US1998/013343 WO1999001707A1 (en) | 1997-07-01 | 1998-06-26 | Process for separating a multi-component gas stream containing at least one freezable component |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| NO996556D0 NO996556D0 (no) | 1999-12-29 |
| NO996556L NO996556L (no) | 2000-02-24 |
| NO312857B1 true NO312857B1 (no) | 2002-07-08 |
Family
ID=21971442
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO19996556A NO312857B1 (no) | 1997-07-01 | 1999-12-29 | Fremgangsmåte ved separasjon av en flerkomponent gasström inneholdende minst en frysbar komponent |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US6053007A (id) |
| CA (1) | CA2294742C (id) |
| GB (1) | GB2344416B (id) |
| ID (1) | ID24280A (id) |
| NO (1) | NO312857B1 (id) |
| WO (1) | WO1999001707A1 (id) |
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| US6742358B2 (en) | 2001-06-08 | 2004-06-01 | Elkcorp | Natural gas liquefaction |
| US20030047492A1 (en) * | 2001-09-04 | 2003-03-13 | Hopewell Richard B. | High ethane recovery from a ryan/holmes additive recovery column |
| WO2003062725A1 (en) * | 2002-01-18 | 2003-07-31 | Curtin University Of Technology | Process and device for production of lng by removal of freezable solids |
| US6945075B2 (en) * | 2002-10-23 | 2005-09-20 | Elkcorp | Natural gas liquefaction |
| AU2003900534A0 (en) * | 2003-02-07 | 2003-02-20 | Shell Internationale Research Maatschappij B.V. | Process and apparatus for removal of a contaminant from a natural gas feed stream |
| KR101120324B1 (ko) * | 2003-02-25 | 2012-06-12 | 오르트로프 엔지니어스, 리미티드 | 탄화수소 가스의 처리방법 |
| US6889523B2 (en) | 2003-03-07 | 2005-05-10 | Elkcorp | LNG production in cryogenic natural gas processing plants |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US4284423A (en) * | 1978-02-15 | 1981-08-18 | Exxon Research & Engineering Co. | Separation of carbon dioxide and other acid gas components from hydrocarbon feeds containing admixtures of methane and hydrogen |
| US4511382A (en) * | 1983-09-15 | 1985-04-16 | Exxon Production Research Co. | Method of separating acid gases, particularly carbon dioxide, from methane by the addition of a light gas such as helium |
| US4889545A (en) * | 1988-11-21 | 1989-12-26 | Elcor Corporation | Hydrocarbon gas processing |
| US4936887A (en) * | 1989-11-02 | 1990-06-26 | Phillips Petroleum Company | Distillation plus membrane processing of gas streams |
| US5062270A (en) * | 1990-08-31 | 1991-11-05 | Exxon Production Research Company | Method and apparatus to start-up controlled freezing zone process and purify the product stream |
| US5120338A (en) * | 1991-03-14 | 1992-06-09 | Exxon Production Research Company | Method for separating a multi-component feed stream using distillation and controlled freezing zone |
| US5335504A (en) * | 1993-03-05 | 1994-08-09 | The M. W. Kellogg Company | Carbon dioxide recovery process |
| US5345772A (en) * | 1993-05-14 | 1994-09-13 | Process Systems International, Inc. | Single column distillative separation employing bottom additives |
-
1998
- 1998-06-26 ID IDW20000195A patent/ID24280A/id unknown
- 1998-06-26 GB GB9930545A patent/GB2344416B/en not_active Expired - Fee Related
- 1998-06-26 CA CA002294742A patent/CA2294742C/en not_active Expired - Lifetime
- 1998-06-26 WO PCT/US1998/013343 patent/WO1999001707A1/en not_active Ceased
- 1998-06-29 US US09/106,152 patent/US6053007A/en not_active Expired - Lifetime
-
1999
- 1999-12-29 NO NO19996556A patent/NO312857B1/no not_active IP Right Cessation
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| Publication number | Publication date |
|---|---|
| ID24280A (id) | 2000-07-13 |
| GB2344416A (en) | 2000-06-07 |
| GB9930545D0 (en) | 2000-02-16 |
| NO996556L (no) | 2000-02-24 |
| WO1999001707A1 (en) | 1999-01-14 |
| CA2294742C (en) | 2005-04-05 |
| GB2344416B (en) | 2001-09-12 |
| US6053007A (en) | 2000-04-25 |
| GB2344416A8 (en) | 2000-06-19 |
| NO996556D0 (no) | 1999-12-29 |
| CA2294742A1 (en) | 1999-01-14 |
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| MK1K | Patent expired |