Endothermic removal of coke deposited on catalytic materials during carbo-metallic oil conversion
Abstract
A process is disclosed for the conversion of high boiling oil feeds having a significant level of Conradson carbon components and metals to form lighter oil products by contacting the feed under catalytic conversion conditions with a catalyst containing one of a select group of metal additives to catalyze the endothermic removal of carbon with CO/sub 2/. Conversion conditions are such that hydrocarbonaceous material and metals are deposited to deactivate the catalyst in the conversion zone. Deactivated catalyst is partially regenerated in the presence of carbon dioxide containing gas before or after oxygen regeneration at a temperature below 1600/sup 0/ F. to provide a regenerated catalyst which is recycled to the conversion zone for further contact with fresh feed. The metal additive is present on the catalyst in an amount sufficient to catalyze the endothermic removal of carbonaceous material in the presence of a carbon dioxide rich gas at regeneration temperature below 1500/sup 0/ F. The catalyst composition comprises a crystalline aluminosilicate dispersed in a solid matrix material and containing one or more of the metal additives. Metal additive may be introduced into the catalyst during the conversion process or during catalyst manufacture. Metal additives include water soluble inorganic metalmore »
- Inventors:
- Publication Date:
- OSTI Identifier:
- 6863405
- Patent Number(s):
- US 4425259
- Assignee:
- Ashland Oil, Inc.
- Resource Type:
- Patent
- Resource Relation:
- Patent File Date: Filed date 5 Aug 1981; Other Information: PAT-APPL-290277
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 02 PETROLEUM; ALUMINIUM SILICATES; CATALYTIC EFFECTS; BISMUTH; CATALYSTS; DEACTIVATION; REGENERATION; COPPER; IRIDIUM; PALLADIUM; PETROLEUM RESIDUES; CATALYTIC CRACKING; PLATINUM; RHODIUM; RUTHENIUM; SILICA; TIN; ADDITIVES; CHEMICAL REACTORS; CLAYS; COKE; DEPOSITION; REMOVAL; ALUMINIUM COMPOUNDS; CHALCOGENIDES; CHEMICAL REACTIONS; CRACKING; DECOMPOSITION; ELEMENTS; ENERGY SOURCES; FOSSIL FUELS; FUELS; METALS; MINERALS; OXIDE MINERALS; OXIDES; OXYGEN COMPOUNDS; PETROLEUM; PETROLEUM FRACTIONS; PLATINUM METALS; PYROLYSIS; SILICATES; SILICON COMPOUNDS; SILICON OXIDES; THERMOCHEMICAL PROCESSES; TRANSITION ELEMENTS; 020400* - Petroleum- Processing; 020500 - Petroleum- Products & By-Products
Citation Formats
Hettinger, W P, Hoffman, J F, and Kovach, S M. Endothermic removal of coke deposited on catalytic materials during carbo-metallic oil conversion. United States: N. p., 1984.
Web.
Hettinger, W P, Hoffman, J F, & Kovach, S M. Endothermic removal of coke deposited on catalytic materials during carbo-metallic oil conversion. United States.
Hettinger, W P, Hoffman, J F, and Kovach, S M. 1984.
"Endothermic removal of coke deposited on catalytic materials during carbo-metallic oil conversion". United States.
@article{osti_6863405,
title = {Endothermic removal of coke deposited on catalytic materials during carbo-metallic oil conversion},
author = {Hettinger, W P and Hoffman, J F and Kovach, S M},
abstractNote = {A process is disclosed for the conversion of high boiling oil feeds having a significant level of Conradson carbon components and metals to form lighter oil products by contacting the feed under catalytic conversion conditions with a catalyst containing one of a select group of metal additives to catalyze the endothermic removal of carbon with CO/sub 2/. Conversion conditions are such that hydrocarbonaceous material and metals are deposited to deactivate the catalyst in the conversion zone. Deactivated catalyst is partially regenerated in the presence of carbon dioxide containing gas before or after oxygen regeneration at a temperature below 1600/sup 0/ F. to provide a regenerated catalyst which is recycled to the conversion zone for further contact with fresh feed. The metal additive is present on the catalyst in an amount sufficient to catalyze the endothermic removal of carbonaceous material in the presence of a carbon dioxide rich gas at regeneration temperature below 1500/sup 0/ F. The catalyst composition comprises a crystalline aluminosilicate dispersed in a solid matrix material and containing one or more of the metal additives. Metal additive may be introduced into the catalyst during the conversion process or during catalyst manufacture. Metal additives include water soluble inorganic metal salts, hydrocarbon soluble organo-metallic compounds of the select group of metals, and metal contaminants found in a high boiling residual oil feed.},
doi = {},
url = {https://www.osti.gov/biblio/6863405},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Tue Jan 10 00:00:00 EST 1984},
month = {Tue Jan 10 00:00:00 EST 1984}
}