ES2112569T3 - Procedimiento de recuperacion de etileno con circuito abierto de agente de refrigeracion mixto. - Google Patents
Procedimiento de recuperacion de etileno con circuito abierto de agente de refrigeracion mixto.Info
- Publication number
- ES2112569T3 ES2112569T3 ES95101155T ES95101155T ES2112569T3 ES 2112569 T3 ES2112569 T3 ES 2112569T3 ES 95101155 T ES95101155 T ES 95101155T ES 95101155 T ES95101155 T ES 95101155T ES 2112569 T3 ES2112569 T3 ES 2112569T3
- Authority
- ES
- Spain
- Prior art keywords
- ethylene recovery
- open circuit
- ethylene
- mixed refrigerant
- refrigeration agent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 title abstract 6
- 239000005977 Ethylene Substances 0.000 title abstract 6
- 238000011084 recovery Methods 0.000 title abstract 4
- 238000005057 refrigeration Methods 0.000 title abstract 4
- 238000000034 method Methods 0.000 title abstract 2
- 239000003795 chemical substances by application Substances 0.000 title 1
- 239000003507 refrigerant Substances 0.000 abstract 3
- 230000003750 conditioning effect Effects 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 abstract 1
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
- F25J3/0228—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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
-
- 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
- F25J3/0204—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
- F25J3/0219—Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
-
- 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
- F25J3/0238—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 2 carbon atoms or more
-
- 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
- F25J3/0252—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 hydrogen
-
- 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
- F25J2200/80—Processes or apparatus using separation by rectification using integrated mass and heat exchange, i.e. non-adiabatic rectification in a reflux exchanger or dephlegmator
-
- 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
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation 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
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/12—Refinery or petrochemical off-gas
-
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/02—Internal refrigeration with liquid vaporising loop
-
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/04—Internal refrigeration with work-producing gas expansion loop
-
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
- F25J2270/902—Details about the refrigeration cycle used, e.g. composition of refrigerant, arrangement of compressors or cascade, make up sources, use of reflux exchangers etc.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
SE SUMINISTRA UN METODO DE REFRIGERACION EN UNA PLANTA DE RECUPERACION DE ETILENO MEDIANTE UN CICLO DE REFRIGERACION MIXTO DE CIRCUITO ABIERTO QUE UTILIZA COMPONENTES PRESENTES EN EL GAS DE SUMINISTRO QUE CONTIENE EL ETILENO COMO REFRIGERANTE MEZCLADO. LA REFRIGERACION ES SUMINISTRADA POR UN REFRIGERANTE MEZCLADO, SUBENFRIADO A ENTRE -175 (GRADOS) Y -225 (GRADOS) F PARA DESMETANIZAR EL CONDENSADOR DE CABEZA Y PARA EL ENFRIAMIENTO INICIAL Y LA CONDENSACION DEL GAS DE SUMINISTRO QUE CONTIENE ETILENO. PUEDE CONSEGUIRSE UNA RECUPERACION DE ETILENO DE HASTA EL 99.0% CON UN REDUCIDO CONSUMO DE ENERGIA EN COMPARACION CON LOS CICLOS DE RECUPERACION DE ETILENO CONVENCIONALES. ADEMAS, PUEDEN REALIZARSE AHORROS SIGNIFICATIVOS DE CAPITAL DEBIDO A LA SIMPLIFICACION DEL EQUIPO CON EL CICLO DE REFRIGERANTE MEZCLADO, DE CIRCUITO ABIERTO, QUE PUEDE SER REALIZADO VENTAJOSAMENTE A PRESIONES DE ENTRE 150 Y 400 PSIA.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/192,025 US5377490A (en) | 1994-02-04 | 1994-02-04 | Open loop mixed refrigerant cycle for ethylene recovery |
| US08/289,862 US5497626A (en) | 1994-02-04 | 1994-08-12 | Open loop mixed refrigerant cycle for ethylene recovery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2112569T3 true ES2112569T3 (es) | 1998-04-01 |
Family
ID=26887646
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES95101155T Expired - Lifetime ES2112569T3 (es) | 1994-02-04 | 1995-01-27 | Procedimiento de recuperacion de etileno con circuito abierto de agente de refrigeracion mixto. |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP0667327B1 (es) |
| JP (1) | JP2870724B2 (es) |
| CN (1) | CN1046694C (es) |
| CA (1) | CA2141385C (es) |
| DE (1) | DE69501043T2 (es) |
| ES (1) | ES2112569T3 (es) |
| NO (1) | NO306713B1 (es) |
| SG (1) | SG38863A1 (es) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DZ2527A1 (fr) * | 1997-12-19 | 2003-02-01 | Exxon Production Research Co | Pièces conteneurs et canalisations de traitement aptes à contenir et transporter des fluides à des températures cryogéniques. |
| US5979177A (en) * | 1998-01-06 | 1999-11-09 | Abb Lummus Global Inc. | Ethylene plant refrigeration system |
| US6487876B2 (en) * | 2001-03-08 | 2002-12-03 | Air Products And Chemicals, Inc. | Method for providing refrigeration to parallel heat exchangers |
| US6705113B2 (en) * | 2002-04-11 | 2004-03-16 | Abb Lummus Global Inc. | Olefin plant refrigeration system |
| US6637237B1 (en) * | 2002-04-11 | 2003-10-28 | Abb Lummus Global Inc. | Olefin plant refrigeration system |
| JP4747001B2 (ja) * | 2006-02-21 | 2011-08-10 | 石油コンビナート高度統合運営技術研究組合 | 冷熱供給システム |
| US9139491B2 (en) * | 2011-03-24 | 2015-09-22 | Lummus Technology Inc. | Methanol to olefins process |
| CN104649858B (zh) * | 2014-12-26 | 2017-01-11 | 浙江大学 | 一种丁辛醇尾气回收系统及其方法 |
| CN116989534B (zh) * | 2022-04-26 | 2025-11-21 | 中国石油化工股份有限公司 | 丙烷脱氢制丙烯气相产物中碳三馏分的分离装置及方法 |
| CN119713759B (zh) * | 2024-12-31 | 2025-09-23 | 西安交通大学 | 一种基于低温精馏的粗氦纯化液化循环系统与方法 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2339826A1 (fr) * | 1976-01-30 | 1977-08-26 | Technip Cie | Procede et installation de traitement par echanges de chaleur a basses temperatures en particulier pour le traitement des gaz naturels et des gaz craques |
| US4720293A (en) * | 1987-04-28 | 1988-01-19 | Air Products And Chemicals, Inc. | Process for the recovery and purification of ethylene |
| US4900347A (en) * | 1989-04-05 | 1990-02-13 | Mobil Corporation | Cryogenic separation of gaseous mixtures |
| US5035732A (en) * | 1990-01-04 | 1991-07-30 | Stone & Webster Engineering Corporation | Cryogenic separation of gaseous mixtures |
| US5377490A (en) * | 1994-02-04 | 1995-01-03 | Air Products And Chemicals, Inc. | Open loop mixed refrigerant cycle for ethylene recovery |
-
1995
- 1995-01-27 EP EP95101155A patent/EP0667327B1/en not_active Expired - Lifetime
- 1995-01-27 ES ES95101155T patent/ES2112569T3/es not_active Expired - Lifetime
- 1995-01-27 DE DE69501043T patent/DE69501043T2/de not_active Expired - Fee Related
- 1995-01-27 SG SG1995001084A patent/SG38863A1/en unknown
- 1995-01-30 JP JP7033024A patent/JP2870724B2/ja not_active Expired - Fee Related
- 1995-01-30 CA CA002141385A patent/CA2141385C/en not_active Expired - Fee Related
- 1995-02-01 NO NO950372A patent/NO306713B1/no unknown
- 1995-02-03 CN CN95100196A patent/CN1046694C/zh not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| AU664003B2 (en) | 1995-10-26 |
| JP2870724B2 (ja) | 1999-03-17 |
| CN1109855A (zh) | 1995-10-11 |
| AU1144995A (en) | 1995-08-24 |
| CA2141385A1 (en) | 1995-08-05 |
| EP0667327B1 (en) | 1997-11-19 |
| NO950372D0 (no) | 1995-02-01 |
| JPH07278020A (ja) | 1995-10-24 |
| DE69501043T2 (de) | 1998-06-18 |
| NO950372L (no) | 1995-08-07 |
| NO306713B1 (no) | 1999-12-13 |
| EP0667327A1 (en) | 1995-08-16 |
| DE69501043D1 (de) | 1998-01-02 |
| CA2141385C (en) | 1997-10-14 |
| CN1046694C (zh) | 1999-11-24 |
| SG38863A1 (en) | 1997-04-17 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG2A | Definitive protection |
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