TW323962B - Separation process of a multi-component stream using a distillation system with multiple towers - Google Patents
Separation process of a multi-component stream using a distillation system with multiple towersInfo
- Publication number
- TW323962B TW323962B TW082101534A TW82101534A TW323962B TW 323962 B TW323962 B TW 323962B TW 082101534 A TW082101534 A TW 082101534A TW 82101534 A TW82101534 A TW 82101534A TW 323962 B TW323962 B TW 323962B
- Authority
- TW
- Taiwan
- Prior art keywords
- component
- tower
- main distillation
- vapor
- recycling
- Prior art date
Links
Classifications
-
- 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
- F25J3/04248—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
- F25J3/04284—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
- F25J3/0429—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
- F25J3/04303—Lachmann expansion, i.e. expanded into oxygen producing or low pressure column
-
- 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
-
- 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
- F25J3/04709—Producing crude argon in a crude argon column as an auxiliary column system in at least 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/50—Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column
-
- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/50—Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column
- F25J2200/54—Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column in the low pressure column of a double 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
-
- 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
- F25J2245/02—Recycle of a stream in general, e.g. a by-pass stream
-
- 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)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Separation By Low-Temperature Treatments (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/885,580 US5230217A (en) | 1992-05-19 | 1992-05-19 | Inter-column heat integration for multi-column distillation system |
Publications (1)
Publication Number | Publication Date |
---|---|
TW323962B true TW323962B (en) | 1998-01-01 |
Family
ID=25387243
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW082101534A TW323962B (en) | 1992-05-19 | 1993-03-02 | Separation process of a multi-component stream using a distillation system with multiple towers |
Country Status (7)
Country | Link |
---|---|
US (1) | US5230217A (zh) |
EP (1) | EP0573176B1 (zh) |
JP (1) | JPH074486B2 (zh) |
KR (1) | KR960010365B1 (zh) |
CA (1) | CA2096064A1 (zh) |
DE (1) | DE69307399T2 (zh) |
TW (1) | TW323962B (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI786250B (zh) * | 2018-03-15 | 2022-12-11 | 日商東洋工程股份有限公司 | 非絕熱型蒸餾塔 |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5341646A (en) * | 1993-07-15 | 1994-08-30 | Air Products And Chemicals, Inc. | Triple column distillation system for oxygen and pressurized nitrogen production |
US5513497A (en) * | 1995-01-20 | 1996-05-07 | Air Products And Chemicals, Inc. | Separation of fluid mixtures in multiple distillation columns |
US5634356A (en) * | 1995-11-28 | 1997-06-03 | Air Products And Chemicals, Inc. | Process for introducing a multicomponent liquid feed stream at pressure P2 into a distillation column operating at lower pressure P1 |
US6605190B1 (en) | 1997-02-14 | 2003-08-12 | San Diego State University Foundation | Staged optimal externally-controlled systems and method thereof |
US5970742A (en) * | 1998-04-08 | 1999-10-26 | Air Products And Chemicals, Inc. | Distillation schemes for multicomponent separations |
US6106674A (en) * | 1998-05-26 | 2000-08-22 | Air Products And Chemicals, Inc. | Operable and efficient distillation schemes for multicomponent separations |
JP3505503B2 (ja) * | 2000-11-22 | 2004-03-08 | 康一 浅野 | 分離係数が1に近い混合物の蒸留による分離濃縮方法および装置 |
WO2005005357A1 (en) * | 2003-07-04 | 2005-01-20 | Ineos Phenol Gmbh & Co. Kg | Process for the preparation of phenolic compounds, for separating phenol from cleavage product mixtures, and an apparatus |
US7626060B2 (en) * | 2003-07-11 | 2009-12-01 | INEOS Phenol GmbH & Co., KG | Process for the preparation of phenolic compounds, for separating phenol from cleavage product mixtures, and an apparatus |
US7249469B2 (en) * | 2004-11-18 | 2007-07-31 | Exxonmobil Chemical Patents Inc. | Method for separating a multicomponent stream |
US8574425B2 (en) | 2010-12-14 | 2013-11-05 | Uop Llc | Process for removing heavy polynuclear aromatic compounds from a hydroprocessed stream |
US8852404B2 (en) | 2010-12-14 | 2014-10-07 | Uop Llc | Apparatus for removing heavy polynuclear aromatic compounds from a hydroprocessed stream |
US8877040B2 (en) | 2012-08-20 | 2014-11-04 | Uop Llc | Hydrotreating process and apparatus relating thereto |
US8877014B2 (en) * | 2012-12-14 | 2014-11-04 | Uop Llc | Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons |
US10408536B2 (en) * | 2017-09-05 | 2019-09-10 | Praxair Technology, Inc. | System and method for recovery of neon and helium from an air separation unit |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1508603A (en) * | 1974-04-11 | 1978-04-26 | Haselden G | Distillation processes and apparatus |
US4234391A (en) * | 1978-10-13 | 1980-11-18 | University Of Utah | Continuous distillation apparatus and method |
US4605247A (en) * | 1982-04-21 | 1986-08-12 | Spetsialnoe Konstruktorskoe Bjuro "Transprogress" | Device for sealing the detachable joints of tubing elements in pneumatic transport facilities |
GB8524598D0 (en) * | 1985-10-04 | 1985-11-06 | Boc Group Plc | Liquid-vapour contact |
US4756731A (en) * | 1986-02-20 | 1988-07-12 | Erickson Donald C | Oxygen and argon by back-pressured distillation |
GB8622055D0 (en) * | 1986-09-12 | 1986-10-22 | Boc Group Plc | Air separation |
US4762542A (en) * | 1987-03-20 | 1988-08-09 | The Boc Group, Inc. | Process for the recovery of argon |
GB8800842D0 (en) * | 1988-01-14 | 1988-02-17 | Boc Group Plc | Air separation |
DE3840506A1 (de) * | 1988-12-01 | 1990-06-07 | Linde Ag | Verfahren und vorrichtung zur luftzerlegung |
FR2655137B1 (fr) * | 1989-11-28 | 1992-10-16 | Air Liquide | Procede et installation de distillation d'air avec production d'argon. |
US5076823A (en) * | 1990-03-20 | 1991-12-31 | Air Products And Chemicals, Inc. | Process for cryogenic air separation |
US5100447A (en) * | 1990-08-30 | 1992-03-31 | The Boc Group, Inc. | Argon recovery from partial oxidation based ammonia plant purge gases |
-
1992
- 1992-05-19 US US07/885,580 patent/US5230217A/en not_active Expired - Fee Related
-
1993
- 1993-03-02 TW TW082101534A patent/TW323962B/zh active
- 1993-05-12 CA CA002096064A patent/CA2096064A1/en not_active Abandoned
- 1993-05-18 JP JP5115513A patent/JPH074486B2/ja not_active Expired - Lifetime
- 1993-05-19 DE DE69307399T patent/DE69307399T2/de not_active Expired - Fee Related
- 1993-05-19 KR KR1019930008525A patent/KR960010365B1/ko not_active IP Right Cessation
- 1993-05-19 EP EP93303865A patent/EP0573176B1/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI786250B (zh) * | 2018-03-15 | 2022-12-11 | 日商東洋工程股份有限公司 | 非絕熱型蒸餾塔 |
Also Published As
Publication number | Publication date |
---|---|
KR960010365B1 (ko) | 1996-07-31 |
JPH067601A (ja) | 1994-01-18 |
US5230217A (en) | 1993-07-27 |
EP0573176A3 (en) | 1995-02-15 |
DE69307399D1 (de) | 1997-02-27 |
DE69307399T2 (de) | 1997-05-15 |
JPH074486B2 (ja) | 1995-01-25 |
EP0573176A2 (en) | 1993-12-08 |
EP0573176B1 (en) | 1997-01-15 |
KR930023052A (ko) | 1993-12-18 |
CA2096064A1 (en) | 1993-11-20 |
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