BR0207619A - Sistema e processo de retificação integrado a quente avançado e processo para separar componentes gasosos - Google Patents
Sistema e processo de retificação integrado a quente avançado e processo para separar componentes gasososInfo
- Publication number
- BR0207619A BR0207619A BR0207619-5A BR0207619A BR0207619A BR 0207619 A BR0207619 A BR 0207619A BR 0207619 A BR0207619 A BR 0207619A BR 0207619 A BR0207619 A BR 0207619A
- Authority
- BR
- Brazil
- Prior art keywords
- processes
- gaseous components
- grinding system
- separating gaseous
- hot integrated
- Prior art date
Links
Classifications
-
- 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
-
- 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
-
- 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
- F25J3/0233—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
-
- 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
- F25J2200/74—Refluxing the column with at least a part of the partially condensed overhead 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
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/06—Splitting of the feed stream, e.g. for treating or cooling in different ways
-
- 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/62—Ethane or ethylene
-
- 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
- F25J2270/60—Closed external refrigeration cycle with single component refrigerant [SCR], e.g. C1-, C2- or C3-hydrocarbons
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
"SISTEMA E PROCESSO DE RETIFICAçãO INTEGRADO A QUENTE AVANçADO E PROCESSO PARA SEPARAR COMPONENTES GASOSOS". A presente invenção inclui novos processos e métodos e também novos aparelhos e equipamentos especialmente adaptados para executar os processos e atingir os resultados excelentes e as vantagens importantes que são obtidas por meio dos mesmos e que constituem partes essenciais e básicas da invenção. Estes aparelhos e processos obtidos desse modo incluem, mas não são ficam a eles limitados, uma torre de retificação (2) com um tambor de refluxo (16) e um trocador central de múltiplos refrigerantes (12).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/792,091 US6343487B1 (en) | 2001-02-22 | 2001-02-22 | Advanced heat integrated rectifier system |
PCT/US2002/002586 WO2002068887A1 (en) | 2001-02-22 | 2002-01-30 | Advanced heat integrated rectifier system |
Publications (2)
Publication Number | Publication Date |
---|---|
BR0207619A true BR0207619A (pt) | 2004-01-13 |
BR0207619B1 BR0207619B1 (pt) | 2011-02-22 |
Family
ID=25155763
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BRPI0207619-5A BR0207619B1 (pt) | 2001-02-22 | 2002-01-30 | sistema de retificação integrado a quente avançado. |
Country Status (6)
Country | Link |
---|---|
US (1) | US6343487B1 (pt) |
EP (1) | EP1368604B8 (pt) |
KR (1) | KR100843487B1 (pt) |
CN (1) | CN1260541C (pt) |
BR (1) | BR0207619B1 (pt) |
WO (1) | WO2002068887A1 (pt) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SG102589A1 (en) * | 2000-08-16 | 2004-03-26 | Inst Materials Research & Eng | Buried hetero-structure opto-electronic device |
US7437891B2 (en) | 2004-12-20 | 2008-10-21 | Ineos Usa Llc | Recovery and purification of ethylene |
CN100346856C (zh) * | 2005-10-14 | 2007-11-07 | 清华大学 | 精馏塔的一种自动控制和优化方法 |
CN100440081C (zh) * | 2006-12-26 | 2008-12-03 | 浙江大学 | 空分塔的广义预测控制系统及方法 |
CN104841153A (zh) * | 2015-05-28 | 2015-08-19 | 江西永通科技股份有限公司 | 一种对叔丁基甲苯精馏分离的设备及其分离工艺 |
CN112452095B (zh) * | 2020-11-10 | 2022-11-08 | 中国石油化工股份有限公司 | 一种改进的尾气精馏方法 |
CN114307219B (zh) * | 2022-02-23 | 2023-03-17 | 万华化学集团股份有限公司 | 丙烯精馏塔精馏调节方法、设备及计算机可读存储介质 |
Family Cites Families (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1932903A (en) | 1927-11-17 | 1933-10-31 | Ralph H Mckee | Process of and apparatus for liquefying gases |
US2214790A (en) | 1935-07-05 | 1940-09-17 | Du Pont | Process and apparatus for separating gases |
US2247470A (en) * | 1938-08-09 | 1941-07-01 | Solvay Process Co | Process for the separation of nitrosyl chloride and chlorine |
US2582068A (en) | 1948-12-30 | 1952-01-08 | Elliott Co | Method and apparatus for separating gases |
US3186182A (en) | 1963-05-27 | 1965-06-01 | Phillips Petroleum Co | Low-temperature, low-pressure separation of gases |
US3444696A (en) | 1967-02-10 | 1969-05-20 | Stone & Webster Eng Corp | Demethanization employing different temperature level refrigerants |
AT284801B (de) | 1967-02-13 | 1970-09-25 | Linde Ag | Verfahren und Vorrichtung zum Zerlegen eines Kohlenwasserstoffgemisches unter gleichzeitiger Gewinnung von Acetylen |
US4033735A (en) * | 1971-01-14 | 1977-07-05 | J. F. Pritchard And Company | Single mixed refrigerant, closed loop process for liquefying natural gas |
US4002042A (en) | 1974-11-27 | 1977-01-11 | Air Products And Chemicals, Inc. | Recovery of C2 + hydrocarbons by plural stage rectification and first stage dephlegmation |
US4270940A (en) | 1979-11-09 | 1981-06-02 | Air Products And Chemicals, Inc. | Recovery of C2 hydrocarbons from demethanizer overhead |
US4496381A (en) * | 1983-02-01 | 1985-01-29 | Stone & Webster Engineering Corp. | Apparatus and method for recovering light hydrocarbons from hydrogen containing gases |
DE3408760A1 (de) | 1984-03-09 | 1985-09-12 | Linde Ag, 6200 Wiesbaden | Verfahren zur gewinnung von c(pfeil abwaerts)3(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts)-kohlenwasserstoffen |
US4657571A (en) | 1984-06-29 | 1987-04-14 | Snamprogetti S.P.A. | Process for the recovery of heavy constituents from hydrocarbon gaseous mixtures |
DE3445994A1 (de) * | 1984-12-17 | 1986-06-19 | Linde Ag | Verfahren zur gewinnung von c(pfeil abwaerts)2(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts)- oder von c(pfeil abwaerts)3(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts)-kohlenwasserstoffen |
FR2578637B1 (fr) * | 1985-03-05 | 1987-06-26 | Technip Cie | Procede de fractionnement de charges gazeuses et installation pour l'execution de ce procede |
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 |
DE4235006A1 (de) * | 1992-10-16 | 1994-04-21 | Linde Ag | Verfahren zum Auftrennen eines im wesentlichen aus Wasserstoff, Methan und C¶3¶/C¶4¶-Kohlenwasserstoffen bestehenden Einsatzstromes |
US5505049A (en) | 1995-05-09 | 1996-04-09 | The M. W. Kellogg Company | Process for removing nitrogen from LNG |
CN1070385C (zh) | 1997-05-14 | 2001-09-05 | 中国石油化工总公司 | 改进的分凝分馏塔系统 |
US5979177A (en) * | 1998-01-06 | 1999-11-09 | Abb Lummus Global Inc. | Ethylene plant refrigeration system |
US6244070B1 (en) * | 1999-12-03 | 2001-06-12 | Ipsi, L.L.C. | Lean reflux process for high recovery of ethane and heavier components |
DE10013073A1 (de) * | 2000-03-17 | 2000-10-19 | Linde Ag | Verfahren und Vorrichtung zur Tieftemperaturzerlegung von Luft |
WO2001088447A1 (en) * | 2000-05-18 | 2001-11-22 | Phillips Petroleum Company | Enhanced ngl recovery utilizing refrigeration and reflux from lng plants |
-
2001
- 2001-02-22 US US09/792,091 patent/US6343487B1/en not_active Expired - Lifetime
-
2002
- 2002-01-30 CN CNB028052145A patent/CN1260541C/zh not_active Expired - Lifetime
- 2002-01-30 WO PCT/US2002/002586 patent/WO2002068887A1/en not_active Application Discontinuation
- 2002-01-30 EP EP02709213.9A patent/EP1368604B8/en not_active Expired - Lifetime
- 2002-01-30 BR BRPI0207619-5A patent/BR0207619B1/pt not_active IP Right Cessation
- 2002-01-30 KR KR1020037010431A patent/KR100843487B1/ko active IP Right Grant
Also Published As
Publication number | Publication date |
---|---|
BR0207619B1 (pt) | 2011-02-22 |
KR100843487B1 (ko) | 2008-07-03 |
EP1368604A1 (en) | 2003-12-10 |
CN1492989A (zh) | 2004-04-28 |
EP1368604B1 (en) | 2015-12-02 |
CN1260541C (zh) | 2006-06-21 |
EP1368604B8 (en) | 2016-02-17 |
EP1368604A4 (en) | 2005-06-15 |
WO2002068887A1 (en) | 2002-09-06 |
US6343487B1 (en) | 2002-02-05 |
KR20030094247A (ko) | 2003-12-11 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
B09A | Decision: intention to grant [chapter 9.1 patent gazette] | ||
B16A | Patent or certificate of addition of invention granted [chapter 16.1 patent gazette] |
Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 30/01/2002, OBSERVADAS AS CONDICOES LEGAIS. |
|
B25C | Requirement related to requested transfer of rights |
Owner name: STONE AND WEBSTER, INC. (US) Free format text: A FIM DE ATENDER A ALTERACAO DE NOME REQUERIDA ATRAVES DA PETICAO NO 020120027736/RJ DE 30/03/2012, E NECESSARIO REAPRESENTAR O DOCUMENTO DEVIDAMENTE CONSULARIZADO. |
|
B25A | Requested transfer of rights approved |
Owner name: STONE AND WEBSTER PROCESS TECHNOLOGY, INC. (US) |
|
B21A | Patent or certificate of addition expired [chapter 21.1 patent gazette] |
Free format text: PATENTE EXTINTA EM 30.01.2022 |