Process for the reactivation of sulfur deactivated cobalt titania catalysts; the catalyst compositions, use of the reactivated catalysts for conducting carbon monoxide hydrogenation, reactions and the products of such reactions

Inactive Publication Date: 2001-07-05
EXXON RES & ENG CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

0006] This need and others is achieved in accordance with the present invention which embodies, in the preparation of a cobalt catalyst, compositing cobalt with titania sufficient that when the catalyst is sulfided and deactivated by sulfur, or sulfur-bearing compounds, it can be reactivated, or regenerated, without significant loss of cobalt, if any, from the catalyst. The reactivation, or regeneration is accomplished by treating the sulfided cobalt titania catalyst in a series of steps requiring (1) contact, and treatment, with a gaseous stream of molecular oxygen, preferably air, or oxygen-enriched air or nitrogen, at temperature ranging from about 150.degree. C. to about 600.degree. C., preferably from about 300.degree. C. to about 500.degree. C., sufficient to oxidize the sulfur component (and metal component) of the catalyst, and then (2) contacting, treating or washing the sul

Problems solved by technology

When the catalyst comes in contact with sulfur, the activity of the catalyst gradually declines; eventually to

Method used

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Examples

Experimental program
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Embodiment Construction

Preparation of a Sulfided Catalyst

[0082] For comparative purposes, a sample of fresh Co--Re / TiO.sub.2 catalyst (nominally 11.5 wt. % Co, 1.25 wt. % Re on TiO.sub.2 support) was prepared, and analyzed for cobalt and sulfur content by atomic adsorption spectroscopy. The analysis showed: 11.5.+-.0.2 wt. % cobalt and 0.005.+-.0.001 wt. % sulfur.

[0083] The high concentration hydrogen sulfide gas used for sulfiding the catalyst was produced by acid evolution from an alkali metal sulfide salt. The evolved H.sub.2S was collected in a dry ice cooled trap and purified by distillation from this trap to a second dry ice cooled trap. The second trap was provided with graduations so the quantity of liquid H.sub.2S could be determined. The liquid H.sub.2S in the second trap was vaporized and collected in a 1 liter glass bulb equipped with a pressure indicator. The quantity of H.sub.2S gas in the bulb was determined from the measured pressure, temperature (ambient), and the known volume of the bulb...

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Abstract

A process for the desulfurization, and reactivation of a sulfur deactivated catalyst constituted of cobalt composited with a titania support. The sulfur deactivated cobalt titania catalyst is first contacted with a gaseous stream of molecular oxygen at temperature sufficiently high to oxidize the sulfur component of the catalyst. The sulfur oxidized catalyst is next contacted with a liquid, preferably water, to remove the oxide, or oxides of the sulfur. The catalyst is then contacted with a reducing agent, suitably hydrogen, to restore the activity of the catalyst. During the treatment there is no substantial loss, if any, of cobalt from the catalyst.

Description

1. FIELD OF THE INVENTION[0001] This invention relates to a process for the reactivation, or regeneration of cobalt catalysts deactivated by sulfur; particularly cobalt catalysts as used in hydrogenation of carbon monoxide or Fischer-Tropsch reactions. It also relates to cobalt-titania catalysts, to the process utilizing the catalyst, and the products of such process.2. BACKGROUND[0002] Fischer-Tropsch (F-T) reactions, i.e., catalytic reactions for the production of C.sub.5+ liquid hydrocarbons from mixtures of hydrogen and carbon monoxide, are well known. The F-T process has become the subject of intense study for commercial development. The catalysts used in conducting F-T reactions are typically constituted of an Iron Group metal (Periodic Table of the Elements, Sargent-Welch Scientific Company, Copyright 1979) of Group VIII, e.g., iron, nickel or cobalt, distributed on a particulate refractory inorganic oxide support, e.g., titania. In formation of the catalyst, the catalytic pr...

Claims

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Application Information

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IPC IPC(8): B01J23/94B01J21/06C10G2/00C10N70/00C10M105/04B01J38/12B01J23/889B01J23/75B01J38/48
CPCB01J38/48C10G2/332B01J38/12B01J23/75B01J21/063B01J23/94
Inventor LAPIDUS, ALBERT L'VOVICHDAAGE, MICHEL A.KOVEAL, RUSSELL J.KRYLOVA, ALLA JURIEVNAEROFEEV, ANATOLIY B.
Owner EXXON RES & ENG CO
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