ES8605565A1 - Un procedimiento y una instalacion de los hidrocarburos mas pesados de una mezcla gaseosa - Google Patents
Un procedimiento y una instalacion de los hidrocarburos mas pesados de una mezcla gaseosaInfo
- Publication number
- ES8605565A1 ES8605565A1 ES539032A ES539032A ES8605565A1 ES 8605565 A1 ES8605565 A1 ES 8605565A1 ES 539032 A ES539032 A ES 539032A ES 539032 A ES539032 A ES 539032A ES 8605565 A1 ES8605565 A1 ES 8605565A1
- Authority
- ES
- Spain
- Prior art keywords
- recovering
- installation
- gaseous mixture
- gas
- heavier hydrocarbons
- 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
Links
- 239000008246 gaseous mixture Substances 0.000 title 1
- 229930195733 hydrocarbon Natural products 0.000 title 1
- 150000002430 hydrocarbons Chemical class 0.000 title 1
- 238000009434 installation Methods 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 abstract 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 abstract 2
- 239000001273 butane Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 abstract 1
- 239000001294 propane Substances 0.000 abstract 1
- 238000011084 recovery 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
- F25J3/0252—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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G5/00—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas
- C10G5/06—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas by cooling or compressing
-
- 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
- F25J3/0242—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 3 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/02—Processes or apparatus using separation by rectification in a single 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
- F25J2200/74—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
- 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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed 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
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Water Supply & Treatment (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Measuring Or Testing Involving Enzymes Or Micro-Organisms (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Toys (AREA)
- Pens And Brushes (AREA)
- Golf Clubs (AREA)
Abstract
PROCEDIMIENTO E INSTALACION DE RECUPERACION DE LOS HIDROCARBUROS MAS PESADOS DE UNA MEZCLA GASEOSA. CONSISTE EN VAPORIZAR EN CONTRACORRIENTE CON EL GAS A TRATAR UNA PARTE DE LIQUIDO CONDENSADO Y SUBENFRIADO EN CABEZA DE LA COLUMNA DE DESTILACION. LA INSTALACION COMPRENDE: UN COMPRESOR (2); UNCAMBIADOR DE CALOR (3); UN SEPARADOR DE FASES (4); UN SEGUNDO CAMBIADOR DE CALOR (5); UN SEGUNDO SEPARADOR DE FASES (6); UNA TURBINA (7); UNA VALVULA DE EXPANSION (8); UNA COLUMNA DE DESTILACION (9); UNA VALVULA DE EXPANSION (10); UN TERCER CAMBIADOR DE CALOR (11); UN CUARTO CAMBIADOR (12); UN GRUPO FRIGORIFICO (13); UNA BOMBA (14); UN DEPOSITO (15); UN REBOSADERO (16) Y UN CONDUCTO (17), QUE LO UNE AL CAMBIADOR (5); UNA TERCERA VALVULA DE EXPANSION (18), Y OTRA (19); UN SEGUNDO GRUPO FRIGORIFICO (20).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8321062A FR2557586B1 (fr) | 1983-12-30 | 1983-12-30 | Procede et installation de recuperation des hydrocarbures les plus lourds d'un melange gazeux |
Publications (2)
Publication Number | Publication Date |
---|---|
ES539032A0 ES539032A0 (es) | 1986-03-16 |
ES8605565A1 true ES8605565A1 (es) | 1986-03-16 |
Family
ID=9295736
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES539032A Expired ES8605565A1 (es) | 1983-12-30 | 1984-12-24 | Un procedimiento y una instalacion de los hidrocarburos mas pesados de una mezcla gaseosa |
Country Status (18)
Country | Link |
---|---|
US (1) | US4666483A (es) |
EP (1) | EP0148070B1 (es) |
JP (1) | JP2667807B2 (es) |
KR (1) | KR850700137A (es) |
AT (1) | ATE35671T1 (es) |
AU (1) | AU569136B2 (es) |
BR (1) | BR8407254A (es) |
CA (1) | CA1283599C (es) |
DE (1) | DE3472669D1 (es) |
ES (1) | ES8605565A1 (es) |
FI (1) | FI77222C (es) |
FR (1) | FR2557586B1 (es) |
GR (1) | GR82533B (es) |
MY (1) | MY103410A (es) |
PT (1) | PT79768B (es) |
WO (1) | WO1985003072A1 (es) |
YU (1) | YU222684A (es) |
ZA (1) | ZA849966B (es) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4695303A (en) * | 1986-07-08 | 1987-09-22 | Mcdermott International, Inc. | Method for recovery of natural gas liquids |
US4921514A (en) * | 1989-05-15 | 1990-05-01 | Air Products And Chemicals, Inc. | Mixed refrigerant/expander process for the recovery of C3+ hydrocarbons |
US4936888A (en) * | 1989-12-21 | 1990-06-26 | Phillips Petroleum Company | Nitrogen rejection unit |
US5051120A (en) * | 1990-06-12 | 1991-09-24 | Union Carbide Industrial Gases Technology Corporation | Feed processing for nitrogen rejection unit |
FR2686029B1 (fr) * | 1992-01-09 | 1994-03-18 | Air Liquide | Procede et installation de purification d'hydrogene par traitement cryogenique d'un gaz. |
FR2711779B1 (fr) * | 1993-10-26 | 1995-12-08 | Air Liquide | Procédé et installation de purification cryogénique d'hydrogène. |
US5442924A (en) * | 1994-02-16 | 1995-08-22 | The Dow Chemical Company | Liquid removal from natural gas |
US5588308A (en) * | 1995-08-21 | 1996-12-31 | Air Products And Chemicals, Inc. | Recompression cycle for recovery of natural gas liquids |
US5596883A (en) * | 1995-10-03 | 1997-01-28 | Air Products And Chemicals, Inc. | Light component stripping in plate-fin heat exchangers |
AR007346A1 (es) * | 1996-06-05 | 1999-10-27 | Shell Int Research | Un metodo para separar dioxido de carbono, etano y componentes mas pesados de una corriente de gas natural a alta presion |
GB2324536B (en) * | 1997-04-24 | 2000-09-06 | Costain Oil Gas & Process Limi | Separation of hydrocarbon mixtures |
US6616999B1 (en) * | 2000-05-17 | 2003-09-09 | Raymond G. Freuler | Preapplicable phase change thermal interface pad |
FR2817766B1 (fr) * | 2000-12-13 | 2003-08-15 | Technip Cie | Procede et installation de separation d'un melange gazeux contenant du methane par distillation,et gaz obtenus par cette separation |
DE102008024427B4 (de) * | 2008-05-20 | 2010-03-11 | Lurgi Gmbh | Verfahren und Anlage zur Rückgewinnung von Arbeitsfluid |
US9777960B2 (en) * | 2010-12-01 | 2017-10-03 | Black & Veatch Holding Company | NGL recovery from natural gas using a mixed refrigerant |
JP2014122284A (ja) * | 2012-12-21 | 2014-07-03 | Japan Petroleum Exploration Co Ltd | フレアガスからの粗lpgの回収設備 |
RU2735208C1 (ru) * | 2020-03-02 | 2020-10-28 | Общество с ограниченной ответственностью "Газпром добыча Уренгой" | Способ утилизации валанжинского газа выветривания с буферных разделителей насыщенного метанола |
FR3120431B1 (fr) * | 2021-03-05 | 2023-03-31 | Air Liquide | Purification de monoxyde de carbone par distillation cryogénique |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE293561C (es) * | ||||
US3373574A (en) * | 1965-04-30 | 1968-03-19 | Union Carbide Corp | Recovery of c hydrocarbons from gas mixtures containing hydrogen |
US3397138A (en) * | 1965-12-02 | 1968-08-13 | Warren Petroleum Corp | Gas separation employing work expansion of feed and fractionator overhead |
US3595782A (en) * | 1968-12-05 | 1971-07-27 | Fluor Corp | Method for separating crabon dioxide from hydrocarbons |
DE1815532A1 (de) * | 1968-12-18 | 1970-06-25 | Linde Ag | Verfahren zum Erzeugen von Kaelte |
DE1939114B2 (de) * | 1969-08-01 | 1979-01-25 | Linde Ag, 6200 Wiesbaden | Verflüssigungsverfahren für Gase und Gasgemische, insbesondere für Erdgas |
US4242875A (en) * | 1978-05-10 | 1981-01-06 | C F Braun & Co. | Hydrogen cryogenic purification system |
JPS55162723A (en) * | 1979-05-31 | 1980-12-18 | Union Carbide Corp | Ethylene separation |
DE2932561C2 (de) * | 1979-08-10 | 1987-01-29 | Linde Ag, 6200 Wiesbaden | Verfahren und Vorrichtung zum Zerlegen eines Gasgemisches |
US4285917A (en) * | 1980-07-31 | 1981-08-25 | Bayside Holding Corp. | Method for removal of hydrogen sulfide from sour gas streams |
JPS5825394B2 (ja) * | 1980-08-04 | 1983-05-27 | 出光興産株式会社 | 石油留分から軽質成分を除去する方法 |
IT1136894B (it) * | 1981-07-07 | 1986-09-03 | Snam Progetti | Metodo per il recupero di condensati da una miscela gassosa di idrocarburi |
IT1137281B (it) * | 1981-07-07 | 1986-09-03 | Snam Progetti | Metodo per il recupero di condensati da gas naturale |
US4404008A (en) * | 1982-02-18 | 1983-09-13 | Air Products And Chemicals, Inc. | Combined cascade and multicomponent refrigeration method with refrigerant intercooling |
-
1983
- 1983-12-30 FR FR8321062A patent/FR2557586B1/fr not_active Expired
-
1984
- 1984-12-18 EP EP84402621A patent/EP0148070B1/fr not_active Expired
- 1984-12-18 DE DE8484402621T patent/DE3472669D1/de not_active Expired
- 1984-12-18 AT AT84402621T patent/ATE35671T1/de not_active IP Right Cessation
- 1984-12-20 ZA ZA849966A patent/ZA849966B/xx unknown
- 1984-12-20 GR GR82533A patent/GR82533B/el unknown
- 1984-12-24 ES ES539032A patent/ES8605565A1/es not_active Expired
- 1984-12-26 AU AU37872/85A patent/AU569136B2/en not_active Ceased
- 1984-12-26 BR BR8407254A patent/BR8407254A/pt not_active IP Right Cessation
- 1984-12-26 KR KR1019850700199A patent/KR850700137A/ko not_active Application Discontinuation
- 1984-12-26 US US06/769,628 patent/US4666483A/en not_active Expired - Lifetime
- 1984-12-26 WO PCT/FR1984/000303 patent/WO1985003072A1/fr active IP Right Grant
- 1984-12-26 JP JP60500254A patent/JP2667807B2/ja not_active Expired - Fee Related
- 1984-12-27 YU YU02226/84A patent/YU222684A/xx unknown
- 1984-12-28 CA CA000471152A patent/CA1283599C/fr not_active Expired - Lifetime
- 1984-12-28 PT PT79768A patent/PT79768B/pt unknown
-
1985
- 1985-08-27 FI FI853281A patent/FI77222C/fi not_active IP Right Cessation
-
1988
- 1988-10-04 MY MYPI88001106A patent/MY103410A/en unknown
Also Published As
Publication number | Publication date |
---|---|
US4666483A (en) | 1987-05-19 |
JP2667807B2 (ja) | 1997-10-27 |
PT79768A (fr) | 1985-01-01 |
FI77222C (fi) | 1989-02-10 |
FI853281L (fi) | 1985-08-27 |
ZA849966B (en) | 1985-08-28 |
ES539032A0 (es) | 1986-03-16 |
AU3787285A (en) | 1985-07-30 |
ATE35671T1 (de) | 1988-07-15 |
DE3472669D1 (en) | 1988-08-18 |
YU222684A (en) | 1987-06-30 |
BR8407254A (pt) | 1985-12-24 |
EP0148070A3 (en) | 1985-08-07 |
AU569136B2 (en) | 1988-01-21 |
JPS61500969A (ja) | 1986-05-15 |
GR82533B (en) | 1985-02-18 |
MY103410A (en) | 1993-06-30 |
FI853281A0 (fi) | 1985-08-27 |
WO1985003072A1 (fr) | 1985-07-18 |
FI77222B (fi) | 1988-10-31 |
CA1283599C (fr) | 1991-04-30 |
EP0148070A2 (fr) | 1985-07-10 |
FR2557586A1 (fr) | 1985-07-05 |
KR850700137A (ko) | 1985-10-25 |
PT79768B (fr) | 1986-12-10 |
FR2557586B1 (fr) | 1986-05-02 |
EP0148070B1 (fr) | 1988-07-13 |
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