BR9912987A - Processo para a produção de ácido acético mediante oxidação em fase gasosa, de hidrocarbonetos c4 saturados e suas misturas com hidrocarbonetos c4 insaturados - Google Patents
Processo para a produção de ácido acético mediante oxidação em fase gasosa, de hidrocarbonetos c4 saturados e suas misturas com hidrocarbonetos c4 insaturadosInfo
- Publication number
- BR9912987A BR9912987A BR9912987-6A BR9912987A BR9912987A BR 9912987 A BR9912987 A BR 9912987A BR 9912987 A BR9912987 A BR 9912987A BR 9912987 A BR9912987 A BR 9912987A
- Authority
- BR
- Brazil
- Prior art keywords
- hydrocarbons
- mixtures
- acetic acid
- saturated
- volume
- Prior art date
Links
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 title abstract 9
- 229930195733 hydrocarbon Natural products 0.000 title abstract 7
- 150000002430 hydrocarbons Chemical class 0.000 title abstract 7
- 239000000203 mixture Substances 0.000 title abstract 4
- 238000000034 method Methods 0.000 title abstract 3
- 230000003647 oxidation Effects 0.000 title abstract 3
- 238000007254 oxidation reaction Methods 0.000 title abstract 3
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- 229920006395 saturated elastomer Polymers 0.000 title abstract 2
- 239000007789 gas Substances 0.000 abstract 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 3
- 239000001301 oxygen Substances 0.000 abstract 3
- 229910052760 oxygen Inorganic materials 0.000 abstract 3
- 239000003054 catalyst Substances 0.000 abstract 2
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 abstract 2
- 239000000463 material Substances 0.000 abstract 2
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 abstract 1
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 abstract 1
- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical group [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 abstract 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 abstract 1
- 229930195734 saturated hydrocarbon Natural products 0.000 abstract 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0221—Coating of particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/14—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of germanium, tin or lead
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/20—Vanadium, niobium or tantalum
- B01J23/22—Vanadium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/28—Molybdenum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/195—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with vanadium, niobium or tantalum
- B01J27/198—Vanadium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/19—Catalysts containing parts with different compositions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/612—Surface area less than 10 m2/g
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0219—Coating the coating containing organic compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/215—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Patente de Invenção: <B>"PROCESSO PARA A PRODUçãO DE áCIDO ACéTICO MEDIANTE OXIDAçãO, EM FASE GASOSA, DE HIDROCARBONETOS C~ 4~ SATURADOS E SUAS MISTURAS COM HIDROCARBONETOS C~ 4~ INSATURADOS"<D>. O objetivo da invenção é o processo para a preparação de ácido acético por oxidação em fase gasosa de hidrocarbonetos C~ 4~ saturados e de suas misturas com hidrocarbonetos C~ 4~ insaturados, em um reator tubular, sob utilização de um catalisador de casca, consistindo em um material de suporte não-poroso inerte e em uma massa de óxidos mistos cataliticamente ativa, aplicada sobre a superfície externa do material de suporte, que contém a) um ou mais óxidos a partir do grupo dióxido de titânio, dióxido de zircónio, dióxido de estanho e dióxido de alumínio e b) 0,1 até 1,5% em peso, com relação ao peso do componente a) e por m^ 2^/g de superfície específica do componente a), de pentóxido de vanádio, sendo que é reagida a mistura de gases, contendo oxigênio ou gás contendo oxigênio, um ou mais hidrocarbonetos C~ 4~ e vapor d'água, com uma proporção de mistura em volume de hidrocarboneto C~ 4~/ ar (oxigênio) de 0,2 / 99,8 até 25 / 75 e com uma proporção de mistura em volume de hidrocarboneto C~ 4~/ vapor d'água de 1 / 1 até 1 / 60, em uma temperatura de 100°C até 400°C, e em uma sobre-pressão de 0,2 até 50 bar, no catalisador em casca.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19823052A DE19823052A1 (de) | 1998-05-22 | 1998-05-22 | Schalenkatalysator zur Herstellung von Essigsäure durch Gasphasenoxidation von gesättigten und/oder ungesättigten C4-Kohlenwasserstoffen |
Publications (1)
Publication Number | Publication Date |
---|---|
BR9912987A true BR9912987A (pt) | 2001-07-03 |
Family
ID=7868687
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR9912987-6A BR9912987A (pt) | 1998-05-22 | 1999-05-21 | Processo para a produção de ácido acético mediante oxidação em fase gasosa, de hidrocarbonetos c4 saturados e suas misturas com hidrocarbonetos c4 insaturados |
Country Status (11)
Country | Link |
---|---|
US (1) | US6281385B1 (pt) |
EP (1) | EP0960874B1 (pt) |
JP (1) | JP3112166B2 (pt) |
CN (1) | CN1138746C (pt) |
AT (1) | ATE199536T1 (pt) |
BR (1) | BR9912987A (pt) |
DE (2) | DE19823052A1 (pt) |
ES (1) | ES2155725T3 (pt) |
MX (1) | MX238492B (pt) |
NO (1) | NO317959B1 (pt) |
TW (1) | TW453894B (pt) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19910866A1 (de) | 1999-03-11 | 2000-09-21 | Consortium Elektrochem Ind | Verfahren und Vorrichtung zur Herstellung von gesättigten Carbonsäuren mit ein bis vier C-Atomen |
DE10159834A1 (de) | 2001-12-06 | 2003-06-26 | Consortium Elektrochem Ind | Verfahren zur Herstellung von gesättigten Carbonsäuren mit ein bis vier C-Atomen durch Gasphasenoxidation von 2-Butanon |
GB0223681D0 (en) * | 2002-10-10 | 2002-11-20 | Bp Chem Int Ltd | Catalyst and process |
US7105107B2 (en) * | 2002-12-30 | 2006-09-12 | Conocophillips Company | Use of nonmicroporous support for syngas catalyst |
US7230035B2 (en) * | 2002-12-30 | 2007-06-12 | Conocophillips Company | Catalysts for the conversion of methane to synthesis gas |
DE10335346A1 (de) * | 2003-08-01 | 2005-02-24 | Basf Ag | Katalysator für Gasphasenoxidationen |
JP2006248951A (ja) * | 2005-03-09 | 2006-09-21 | Daicel Chem Ind Ltd | 脂肪族飽和カルボン酸の製造法 |
EP1928814A2 (en) * | 2005-08-23 | 2008-06-11 | Altairnano, Inc | HIGHLY PHOTOCATALYTIC PHOSPHORUS-DOPED ANATASE-TiO2 COMPOSITION AND RELATED MANUFACTURING METHODS |
DE102007011847A1 (de) | 2007-03-12 | 2008-09-18 | Wacker Chemie Ag | Verfahren zur Herstellung von Essig- und Ameisensäure durch Gasphasenoxidation von Ethanol |
CZ200895A3 (cs) | 2008-02-21 | 2010-01-13 | Advanced Materials - Jtj S. R. O. | Katalytická struktura TiO2 pro katalytické procesy do 1000 °C a zpusob její výroby |
TW200948474A (en) * | 2008-04-09 | 2009-12-01 | Basf Se | Coated catalysts comprising a multimetal oxide comprising molybdenum |
KR101083307B1 (ko) | 2009-08-18 | 2011-11-15 | 한국전력공사 | 오산화이바나듐계 촉매 |
DE102010001399A1 (de) | 2010-01-29 | 2011-08-04 | Wacker Chemie AG, 81737 | Verfahren zur Herstellung von Carbonsäuren mit 1-3 Kohlenstoff-atomen aus nachwachsenden Rohstoffen |
DE102014203725A1 (de) | 2014-02-28 | 2015-09-03 | Basf Se | Oxidationskatalysator mit sattelförmigem Trägerformkörper |
BR112018071379B1 (pt) * | 2016-04-21 | 2022-05-17 | Rohm And Haas Company | Método para preparar monômeros de ácido carboxílico alfa,beta-insaturado e monômeros de aldeído insaturado |
Family Cites Families (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL134884C (pt) | 1965-05-18 | |||
GB1165442A (en) | 1966-01-07 | 1969-10-01 | Huels Chemische Werke Ag | Process for the Production of Acetic Acid by Catalytic Gas Phase Oxidation of Butenes |
DE1279011B (de) | 1966-01-07 | 1968-10-03 | Huels Chemische Werke Ag | Verfahren zur Herstellung von Essigsaeure durch katalytische Gasphasenoxydation von Butenen |
JPS4830614B1 (pt) | 1969-06-02 | 1973-09-21 | ||
NL7102805A (pt) | 1970-03-09 | 1971-09-13 | ||
CA939676A (en) | 1970-03-24 | 1974-01-08 | David Naden | Catalytic oxidation |
DE2016681A1 (pt) | 1970-04-08 | 1971-10-28 | ||
DE2041073C3 (de) | 1970-08-19 | 1975-02-06 | Basf Ag, 6700 Ludwigshafen | Verfahren zur Herstellung von Essigsäure |
DE2235103C3 (de) | 1972-07-18 | 1978-04-13 | Chemische Werke Huels Ag, 4370 Marl | Verfahren zur Herstellung von Essigsäure |
US4077912A (en) * | 1972-10-12 | 1978-03-07 | Standard Oil Company | Catalysts useful for exothermic reactions |
US3948807A (en) * | 1973-01-13 | 1976-04-06 | Kuraray Co., Ltd. | Oxide catalysts and process for preparation thereof |
DE2354425C3 (de) | 1973-10-31 | 1978-05-03 | Chemische Werke Huels Ag, 4370 Marl | Verfahren zur Herstellung von Essigsäure durch Gasphasenoxidation von Butenen |
GB1541928A (en) * | 1975-12-23 | 1979-03-14 | Sakai Chemical Industry Co | Production of shaped catalysts or carriers comprising titanium oxide |
US4146734A (en) | 1977-08-08 | 1979-03-27 | Celanese Corporation | Oxidation of butene to acetic acid and catalyst therefor |
US4219671A (en) * | 1977-08-29 | 1980-08-26 | Celanese Corporation | Oxidation of butene to acetic acid |
US4195188A (en) * | 1977-12-12 | 1980-03-25 | Celanese Corporation | Steam assisted hydrocarbon oxidation process |
US4328365A (en) * | 1979-08-10 | 1982-05-04 | Celanese Corporation | Hydrocarbon oxidation via carbon monoxide reduced catalyst |
US4257921A (en) | 1979-08-29 | 1981-03-24 | Celanese Corporation | Catalyst for the oxidation of butene |
US4448897A (en) | 1982-05-13 | 1984-05-15 | Atlantic Richfield Company | Method for producing a vanadium-titanium catalyst exhibiting improved intrinsic surface area |
DE3813312A1 (de) * | 1988-04-20 | 1989-11-02 | Siemens Ag | Plattenfoermiger katalysator zur verminderung der stickoxide in rauchgasen und verfahren zu seiner herstellung |
FR2728898B1 (fr) * | 1994-12-29 | 1997-01-31 | Rhone Poulenc Chimie | Procede de preparation d'acides carboxyliques par oxydation menagee des alcanes correspondants |
DE19649426A1 (de) * | 1996-11-28 | 1998-06-04 | Consortium Elektrochem Ind | Schalenkatalysator zur Herstellung von Essigsäure durch Gasphasenoxidation von ungesättigten C¶4¶-Kohlenwasserstoffen |
-
1998
- 1998-05-22 DE DE19823052A patent/DE19823052A1/de not_active Withdrawn
-
1999
- 1999-05-18 US US09/313,398 patent/US6281385B1/en not_active Expired - Fee Related
- 1999-05-19 TW TW088108160A patent/TW453894B/zh not_active IP Right Cessation
- 1999-05-20 NO NO19992413A patent/NO317959B1/no unknown
- 1999-05-21 BR BR9912987-6A patent/BR9912987A/pt not_active Application Discontinuation
- 1999-05-21 MX MX9904764A patent/MX238492B/es not_active IP Right Cessation
- 1999-05-21 AT AT99109226T patent/ATE199536T1/de not_active IP Right Cessation
- 1999-05-21 DE DE59900050T patent/DE59900050D1/de not_active Expired - Fee Related
- 1999-05-21 EP EP99109226A patent/EP0960874B1/de not_active Expired - Lifetime
- 1999-05-21 ES ES99109226T patent/ES2155725T3/es not_active Expired - Lifetime
- 1999-05-24 JP JP11143597A patent/JP3112166B2/ja not_active Expired - Fee Related
- 1999-05-24 CN CNB991075986A patent/CN1138746C/zh not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP3112166B2 (ja) | 2000-11-27 |
NO317959B1 (no) | 2005-01-17 |
EP0960874A1 (de) | 1999-12-01 |
ES2155725T3 (es) | 2001-05-16 |
NO992413D0 (no) | 1999-05-20 |
ATE199536T1 (de) | 2001-03-15 |
DE19823052A1 (de) | 1999-11-25 |
CN1138746C (zh) | 2004-02-18 |
MX238492B (es) | 2006-07-07 |
CN1236771A (zh) | 1999-12-01 |
US6281385B1 (en) | 2001-08-28 |
MXPA99004764A (es) | 2004-12-09 |
DE59900050D1 (de) | 2001-04-12 |
NO992413L (no) | 1999-11-23 |
JP2000026364A (ja) | 2000-01-25 |
TW453894B (en) | 2001-09-11 |
EP0960874B1 (de) | 2001-03-07 |
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