Abstract: Supported olefin conversion catalysts are activated by a method which comprises calcining the catalyst, impregnating the calcined catalyst with an alcoholic solution of an alkali metal salt, an alkali metal base or an alkali metal alcoholate and then recalcining the catalyst.
Type:
Grant
Filed:
December 3, 1974
Date of Patent:
October 26, 1976
Assignee:
Deutsche Texaco Aktiengesellschaft
Inventors:
Martin Cherubim, Elmar Wilms, Hans Arendsen
Abstract: Unsaturated hydrocarbons are separated from liquid mixtures containing same by adsorbing the unsaturated compound using a metal-loaded macroporous exchange resin and desorbing the unsaturated compound using a normally gaseous hydrocarbon.
Abstract: Refrigeration oils are prepared by subjecting a crude lubricating oil fraction to mild hydrogenation, acid treating, dewaxing and clay percolation.
Type:
Grant
Filed:
September 9, 1974
Date of Patent:
April 27, 1976
Assignee:
Texaco Inc.
Inventors:
Ralph P. Chesluk, Howard J. Platte, Edward C. Brink, Jr.
Abstract: The octane number of a hydrocarbon fraction boiling below 425.degree.F is improved by a cracking-isomerization procedure. The C.sub.5 + portion of the resulting product may be used as a motor fuel or as a blending component for motor fuels.
Type:
Grant
Filed:
May 16, 1974
Date of Patent:
April 27, 1976
Assignee:
Texaco Inc.
Inventors:
Reese A. Peck, Li C. Mih, John T. Brandenburg
Abstract: A desulfurization catalyst is activated by being heated to a temperature between about 750.degree. and 850.degree.F. in the presence of the charge stock to be desulfurized during the initial stages of the on-stream period. In a preferred embodiment the catalyst, prior to the heat treatment, is sulfided at a low temperature and low pressure. The resulting catalyst effectively desulfurizes a petroleum hydrocarbon charge stock with reduced hydrogen consumption.
Type:
Grant
Filed:
December 27, 1974
Date of Patent:
April 27, 1976
Assignee:
Texaco Inc.
Inventors:
Charles A. Ganster, Mary E. Callaghan, Lee K. Gilmer, Gerald V. Nelson, Kenneth D. Miller
Abstract: The deactivation rate of a catalyst used for the high temperature, high space velocity desulfurization of heavy oils is reduced by the incorporation in the catalyst of a small amount of a noble metal.