AR051355A1 - CATALYST TO PREPARE FTALIC ANHYDRIDE BY OXIDATION OF GASEOUS PHASE OF O-XYLENE AND / OR NAFTALENE, PROCEDURE TO PREPARE FTALIC ANHYDRIDE, AND USE OF SUCH CATALYST - Google Patents
CATALYST TO PREPARE FTALIC ANHYDRIDE BY OXIDATION OF GASEOUS PHASE OF O-XYLENE AND / OR NAFTALENE, PROCEDURE TO PREPARE FTALIC ANHYDRIDE, AND USE OF SUCH CATALYSTInfo
- Publication number
- AR051355A1 AR051355A1 ARP050102216A ARP050102216A AR051355A1 AR 051355 A1 AR051355 A1 AR 051355A1 AR P050102216 A ARP050102216 A AR P050102216A AR P050102216 A ARP050102216 A AR P050102216A AR 051355 A1 AR051355 A1 AR 051355A1
- Authority
- AR
- Argentina
- Prior art keywords
- catalyst
- active composition
- zone
- anhydride
- ftalic
- Prior art date
Links
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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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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
- B01J23/16—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
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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
- 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
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- 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
- C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
- C07C51/265—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups
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- 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
- C07C51/31—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting
- C07C51/313—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting with molecular oxygen
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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
- 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)
- Furan Compounds (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
La presente se refiere a un catalizador para preparar anhídrido ftálico por oxidacion de fase gaseosa de o-xileno y/o naftaleno, que comprende al menos tres zonas de catalizador que tienen diferente composicion, las cuales son referidas desde el lado de entrada de gas hacia el lado de salida de gas como primera, segunda y tercera zona de catalizador, teniendo las zonas de catalizador en cada caso una composicion activa que comprende TiO2, disminuyendo el contenido de composicion activa desde la primera zona de catalizador dispuesta hacia el lado de entrada de gas hacia la tercera zona de catalizador dispuesta hacia el lado de salida de gas, siempre que: a) la primera zona de catalizador tiene un contenido de composicion activa entre aproximadamente 7 y 12% en peso; b) la segunda zona de catalizador tiene un contenido de composicion activa en la zona entre 6 y 11% en peso, siendo el contenido de composicion activa de la segunda zona de catalizador menor o igual que el contenido de composicion activa de la primera zona de catalizador, y c) la tercera zona de catalizador tiene un contenido de composicion activa en la zona entre 5 y 10% en peso, siendo el contenido de composicion activa de la tercera zona de catalizador menor que o igual al contenido de composicion activa de la segunda zona de catalizador. También se describe un procedimiento preferido para preparar tal catalizador y el uso preferido de dioxido de titanio usado de acuerdo con la presente.This refers to a catalyst for preparing phthalic anhydride by gas phase oxidation of o-xylene and / or naphthalene, comprising at least three catalyst zones having different composition, which are referred from the gas inlet side to the gas outlet side as the first, second and third catalyst zone, the catalyst zones in each case having an active composition comprising TiO2, decreasing the active composition content from the first catalyst zone disposed towards the inlet side of gas towards the third catalyst zone disposed towards the gas outlet side, provided that: a) the first catalyst zone has an active composition content between about 7 and 12% by weight; b) the second catalyst zone has an active composition content in the zone between 6 and 11% by weight, the active composition content of the second catalyst zone being less than or equal to the active composition content of the first zone of catalyst, and c) the third catalyst zone has an active composition content in the area between 5 and 10% by weight, the active composition content of the third catalyst zone being less than or equal to the active composition content of the second catalyst zone A preferred method for preparing such a catalyst and the preferred use of titanium dioxide used in accordance with the present is also described.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102004026472A DE102004026472A1 (en) | 2004-05-29 | 2004-05-29 | Multi-layer catalyst for the production of phthalic anhydride |
Publications (1)
Publication Number | Publication Date |
---|---|
AR051355A1 true AR051355A1 (en) | 2007-01-10 |
Family
ID=37600968
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP050102216A AR051355A1 (en) | 2004-05-29 | 2005-05-30 | CATALYST TO PREPARE FTALIC ANHYDRIDE BY OXIDATION OF GASEOUS PHASE OF O-XYLENE AND / OR NAFTALENE, PROCEDURE TO PREPARE FTALIC ANHYDRIDE, AND USE OF SUCH CATALYST |
Country Status (3)
Country | Link |
---|---|
CN (1) | CN100496740C (en) |
AR (1) | AR051355A1 (en) |
TW (1) | TWI320722B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI763398B (en) * | 2021-03-29 | 2022-05-01 | 日商旭化成股份有限公司 | Catalyst for producing carboxylate, method for producing carboxylate, and method for producing catalyst for producing carboxylate |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2106796C3 (en) * | 1971-02-12 | 1981-09-24 | Wacker-Chemie GmbH, 8000 München | Process for the production of fixed bed catalysts with a coating of vanadium pentoxide and titanium dioxide |
US3926846A (en) * | 1972-08-25 | 1975-12-16 | Nippon Catalytic Chem Ind | Catalysts for the preparation of phthalic anhydride |
JPS63253080A (en) * | 1987-04-10 | 1988-10-20 | Nippon Steel Chem Co Ltd | Production of phthalic anhydride |
US5504218A (en) * | 1994-04-05 | 1996-04-02 | Nippon Shokubai Co., Ltd. | Method for production pyromellitic anhydride |
CN1047959C (en) * | 1994-10-25 | 2000-01-05 | 中国石油化工总公司 | Supported catalyst for preparing phthalic anhydride |
DE19707943C2 (en) * | 1997-02-27 | 1999-07-08 | Basf Ag | Process for the preparation of phthalic anhydride and catalyst therefor |
DE19823275A1 (en) * | 1998-05-26 | 1999-12-02 | Basf Ag | Process for the preparation of phthalic anhydride by catalytic gas phase oxidation of x-xylene - / - naphthalene mixtures |
DE10040827A1 (en) * | 2000-08-21 | 2002-03-07 | Basf Ag | Process for the preparation of phthalic anhydride |
DE10206989A1 (en) * | 2002-02-19 | 2003-08-21 | Basf Ag | Production of phthalic anhydride involves gas-phase oxidation of o-xylene or naphthalene in a tubular reactor containing three or more different catalyst beds with controlled hot-spot temperatures |
-
2005
- 2005-05-22 CN CNB2005800174657A patent/CN100496740C/en not_active Expired - Fee Related
- 2005-05-27 TW TW94117557A patent/TWI320722B/en not_active IP Right Cessation
- 2005-05-30 AR ARP050102216A patent/AR051355A1/en active IP Right Grant
Also Published As
Publication number | Publication date |
---|---|
CN1960805A (en) | 2007-05-09 |
CN100496740C (en) | 2009-06-10 |
TWI320722B (en) | 2010-02-21 |
TW200613053A (en) | 2006-05-01 |
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