GB977406A - Catalytic compositions and their use in making maleic anhydride - Google Patents
Catalytic compositions and their use in making maleic anhydrideInfo
- Publication number
- GB977406A GB977406A GB393061A GB393061A GB977406A GB 977406 A GB977406 A GB 977406A GB 393061 A GB393061 A GB 393061A GB 393061 A GB393061 A GB 393061A GB 977406 A GB977406 A GB 977406A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hour
- catalyst
- litres
- air flow
- benzene
- 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
Classifications
-
- 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
- B01J27/199—Vanadium with chromium, molybdenum, tungsten or polonium
-
- 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
-
- 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)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
In the manufacture of maleic anhydride by the partial oxidation of benzene, there is used a catalyst consisting of or containing 1 part MoO3, 1.5-8 parts V2O5, 0.1-0.01 part P2O5, 0.1-0.01 part Na and 0.1-0001 part Ni. The catalyst is prepared by contacting a catalyst support with a hydrochloric acid solution of precursors and simultaneously agitating the whole, followed by evaporation to dryness at 85-95 DEG C. for 4-7 hours. An example describes the manufacture of maleic anhydride using a vertical reactor tube down which a benzene/air mixture is fed. Specification 853,849 is referred to.ALSO:A catalytic composition containing 1 part MoO3, 1,5-8 parts V2O5, 0,01-0,1 part P2O5, 0,01-0,1 part Na and 0,0001-0,1 part Ni is made by contacting a catalyst support with an impregnating solution, consisting of hydrochloric acid-soluble compounds of vanadium and molybdenum, e.g. metavanadates and molybdates such as ammonium molybdate and metavanadate, and water-soluble compounds of nickel, sodium and phosphorus, e.g. sodium phosphate and nickel nitrate, and simultaneously agitating the catalyst support and impregnating solution and evaporating the solution to dryness at a temperature of from 85-95 DEG C. for from 4-7 hours. Subsequently the catalytic composition may be actuated by heating up to 175 DEG C. for 1 hour at an air flow of 60 litres/hour, 175-320 DEG C. for 1/2 hour at an air flow rate of 0 litres/hour, 320-400 DEG C. for 1/2 hour at an air flow rate of 60 litres/hour and 400 DEG C. for 5 hours at an air flow rate of 60 litres/hour. Specified catalyst supports are alumina, magnesia, zirconia, mullite and beryllia. The catalyst support may consist of a refractory support in particulate form of about 0,2-0,5 inch average diameter and having a surface area of 10 sq. metres/gm. The support particles may receive a preliminary acid wash using for example HCl, HNO3, H2SO4, H3PO4, CH3COOH, CCl3COOH, (COOH)2, C6H5COOH or (CH.COOH)2. The catalytic composition may be used to synthesize maleic acid from benzene (see Division B2). An example is given. Specification 853,849 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US612160A | 1960-02-02 | 1960-02-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB977406A true GB977406A (en) | 1964-12-09 |
Family
ID=21719417
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB393061A Expired GB977406A (en) | 1960-02-02 | 1961-02-02 | Catalytic compositions and their use in making maleic anhydride |
Country Status (5)
Country | Link |
---|---|
CH (1) | CH419094A (en) |
ES (1) | ES264476A1 (en) |
GB (1) | GB977406A (en) |
LU (1) | LU39698A1 (en) |
SE (1) | SE307782B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1286022B (en) * | 1965-07-02 | 1969-01-02 | Basf Ag | Process for the production of methacrylic acid esters by dehydration of isobutyric acid esters |
US3530169A (en) * | 1965-07-02 | 1970-09-22 | Basf Ag | Production of methacrylic esters |
-
1961
- 1961-01-26 LU LU39698D patent/LU39698A1/xx unknown
- 1961-01-31 ES ES264476A patent/ES264476A1/en not_active Expired
- 1961-02-02 CH CH122661A patent/CH419094A/en unknown
- 1961-02-02 GB GB393061A patent/GB977406A/en not_active Expired
- 1961-02-02 SE SE106561A patent/SE307782B/xx unknown
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1286022B (en) * | 1965-07-02 | 1969-01-02 | Basf Ag | Process for the production of methacrylic acid esters by dehydration of isobutyric acid esters |
US3530169A (en) * | 1965-07-02 | 1970-09-22 | Basf Ag | Production of methacrylic esters |
Also Published As
Publication number | Publication date |
---|---|
DE1443090A1 (en) | 1969-03-27 |
ES264476A1 (en) | 1961-06-16 |
SE307782B (en) | 1969-01-20 |
CH419094A (en) | 1966-08-31 |
LU39698A1 (en) | 1961-03-27 |
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