Continuously producing olefins and hydrogen by dehydrogenation of hydrocarbons, comprises contacting gaseous hydrocarbon with catalyst exhibiting silicon containing carrier, and applying it on highly dispersed vanadium oxide

Continuously producing olefins and hydrogen by dehydrogenation of hydrocarbons, comprises contacting gaseous hydrocarbon with catalyst exhibiting silicon containing carrier, and applying it on highly dispersed vanadium oxide

Continuously producing olefins and hydrogen by dehydrogenation of hydrocarbons, comprises contacting the gaseous hydrocarbon with a catalyst exhibiting a silicon containing carrier, and applying it on the highly dispersed vanadium oxide. An independent claim is also included for a catalyst produced...

Ausführliche Beschreibung

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Bibliographische Detailangaben
Hauptverfasser: OVSITSER, OLGA, KONDRATENKO, EVGENII V
Format: Patent
Sprache:eng ; ger
Schlagworte:
ACYCLIC OR CARBOCYCLIC COMPOUNDS
CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
CHEMISTRY
CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS
GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS
METALLURGY
ORGANIC CHEMISTRY
PERFORMING OPERATIONS
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE
THEIR RELEVANT APPARATUS
TRANSPORTING
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Beschreibung
Zusammenfassung:Continuously producing olefins and hydrogen by dehydrogenation of hydrocarbons, comprises contacting the gaseous hydrocarbon with a catalyst exhibiting a silicon containing carrier, and applying it on the highly dispersed vanadium oxide. An independent claim is also included for a catalyst produced by impregnating vanadyl acetylacetonate dissolved in an organic solvent, with the silicon dioxide carrier, drying and calcining. Um ein Verfahren zur Herstellung von Olefinen mittels Dehydrierung von Kohlenwasserstoffen, insbesondere Alkanen unter Verwendung eines Katalysators sowie einen Katalysator bereitzustellen, mit dem eine hohe Olefinselektivität, eine H2-Co-Produktion und gleichzeitig ein hoher Umsatz erzielt werden kann, wobei der Katalysator möglichst lange ohne Regeneration auskommen soll, wird vorgeschlagen, dass der gasförmige Kohlenwasserstoff mit einem Katalysator, der einen siliziumhaltigen Träger aufweist, auf dem hochdisperses Vanadiumoxid (VOx) aufgebracht ist, in Kontakt gebracht wird.