FR2135741A5 - Catalyst for paraffin dehydrogenation - contg a noble metal and tungsten or molybdenum on a low-acidity alumina support - Google Patents
Catalyst for paraffin dehydrogenation - contg a noble metal and tungsten or molybdenum on a low-acidity alumina supportInfo
- Publication number
- FR2135741A5 FR2135741A5 FR7114888A FR7114888A FR2135741A5 FR 2135741 A5 FR2135741 A5 FR 2135741A5 FR 7114888 A FR7114888 A FR 7114888A FR 7114888 A FR7114888 A FR 7114888A FR 2135741 A5 FR2135741 A5 FR 2135741A5
- Authority
- FR
- France
- Prior art keywords
- pref
- catalyst
- contg
- molybdenum
- tungsten
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/321—Catalytic processes
- C07C5/324—Catalytic processes with metals
- C07C5/325—Catalytic processes with metals of the platinum group
-
- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/652—Chromium, molybdenum or tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
- C07C5/333—Catalytic processes
- C07C5/3335—Catalytic processes with metals
- C07C5/3337—Catalytic processes with metals of the platinum group
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Catalysts for the dehydrogenation of satd. (pref. 3-40C) hydrocarbons, contain (a) alumina, (b) Pt, Ir, Pd or Ru, and (c) W (pref.) or Mo, have a specific surface of 20-150m2/g., and have a heat of neutralisation by NH3 adsorption of 10 cal/g. at 320 degrees c/300 mm Hg. The catalyst pref. contains 0.1-0.5 wt.% component (c) and 0.1-0.5 wt.% component (b). Its specific surface is pref. 50-75 m2/g. and its pore vol. 0.4-0.8 cm3/g. It is pref. prepd. by depositing the metals, drying, calcining and then reducing in a stream of H2 at 500-550 degrees C (when (c) is W) or 550-600 degrees C (when (c) is Mo). Dehydrogenation is pref. effected at 300-600 degrees C and 0.1-10 bars, with a liq. hydrocarbon flow rate of 0.1-30 times the vol. of catalyst, and with an H2/hydrocarbon molar ratio of 0.1-30 at the inlet of the reactor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7114888A FR2135741A5 (en) | 1971-04-26 | 1971-04-26 | Catalyst for paraffin dehydrogenation - contg a noble metal and tungsten or molybdenum on a low-acidity alumina support |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7114888A FR2135741A5 (en) | 1971-04-26 | 1971-04-26 | Catalyst for paraffin dehydrogenation - contg a noble metal and tungsten or molybdenum on a low-acidity alumina support |
Publications (1)
Publication Number | Publication Date |
---|---|
FR2135741A5 true FR2135741A5 (en) | 1972-12-22 |
Family
ID=9075978
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7114888A Expired FR2135741A5 (en) | 1971-04-26 | 1971-04-26 | Catalyst for paraffin dehydrogenation - contg a noble metal and tungsten or molybdenum on a low-acidity alumina support |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR2135741A5 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362663A1 (en) * | 1976-08-24 | 1978-03-24 | Exxon Research Engineering Co | Heat-resistant hydrocarbon reforming catalysts - contg. noble metal and tungsten or molybdenum, on an oxide carrier |
-
1971
- 1971-04-26 FR FR7114888A patent/FR2135741A5/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362663A1 (en) * | 1976-08-24 | 1978-03-24 | Exxon Research Engineering Co | Heat-resistant hydrocarbon reforming catalysts - contg. noble metal and tungsten or molybdenum, on an oxide carrier |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Somorjai et al. | Heterogeneous catalysis on the molecular scale | |
Tsipouriari et al. | Catalytic partial oxidation of methane to synthesis gas over Ni-based catalysts: I. Catalyst performance characteristics | |
Ruckenstein et al. | Role of Support in CO2Reforming of CH4to Syngas over Ni Catalysts | |
Passos et al. | Effect of In and Sn on the adsorption behavior and hydrogenolysis activity of Pt/Al2O3catalysts | |
Sermon et al. | Studies of hydrogen spillover. Part 4.—Factors affecting hydrogen spillover and its reversal | |
Mori et al. | Promotion effects of vanadium, niobium, molybdenum, tungsten, and rhenium oxides on surface reactions in the carbon monoxide hydrogenation over ruthenium/aluminum oxide catalyst | |
US4285837A (en) | Catalyst for steam reforming of hydrocarbons | |
US3068303A (en) | Low surface area alpha alumina catalyst support for the selective hydrogenation of hydrocarbons | |
GB1382557A (en) | Process for the production of high strength reducing gas | |
DE3663626D1 (en) | Co hydrogenation with molybdenum on wide-pore carbon catalysts | |
ES442289A1 (en) | Hydrocarbon conversion with an acidic multimetallic catalytic composite | |
JPH05505764A (en) | Method for producing polymetallic catalysts | |
FR2257336A1 (en) | Noble metal catalyst on expanded iron alloy - with coating contg. oxygen, for oxidn., redn. and exhaust gas purificn. | |
US4207211A (en) | Catalyst for steam reforming of hydrocarbons and process of preparing the catalyst | |
Grzybek et al. | Supported manganese catalysts for the selective catalytic reduction of nitrogen oxides with ammonia Part II. Catalytic experiments | |
Nagai et al. | Surface Properties of Carbided Molybdena–Alumina and Its Activity for CO2Hydrogenation | |
McCabe et al. | Exhaust-catalyst development for methanol-fueled vehicles: 2. Synergism between palladium and silver in methanol and carbon monoxide oxidation over an alumina-supported palladium-silver catalyst | |
Inui et al. | Complete conversion of nitric oxide over the composite catalyst supported on active carbon | |
GB940666A (en) | Improvements in or relating to the preparation of supported catalysts | |
Agrawal et al. | Methanation over transition metal catalysts: II. carbon deactivation of CoAl2O3 in sulfur-free studies | |
GB1509100A (en) | Metallic catalyst support | |
FR2135741A5 (en) | Catalyst for paraffin dehydrogenation - contg a noble metal and tungsten or molybdenum on a low-acidity alumina support | |
US3256205A (en) | Catalyst rejuvenating process | |
US4605639A (en) | Methods for making a supported iron-copper catalyst | |
Triantafillou et al. | Ir/KLTL zeolites: Structural characterization and catalysis ofn-hexane reforming |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
ST | Notification of lapse |