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US4120780A
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Catalysts for hydrodemetallization of hydrocarbons containing metallic compounds as impurities and process for hydro-treating such hydrocarbons using such catalysts
Assignee: Chiyoda Corp
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Filing: 1977-05-26
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Granted: 1978-10-17
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Expires: 1997-05-26
Abstract
Abstract A catalyst obtained by admixing red mud with alumina or/and an alumina-containing substance, optionally adjusting the water content of the admixture and/or adding an organic binder to the admixture, kneading and shaping the admixture into pellets having suitable size and shape, and calcining the pellets of 600° C to 1,100° C. The catalyst has a high compression strength and can, when used in the hydrodemetallization of hydrocarbons, achieve a high rate of demetallization and a low yield of low boiling fractions. The rate of demetallization is enhanced when the process is carried out using a hydrogen feed containing hydrogen sulfide.
Inventors
- 👤 Tatsuo Morimoto
- 👤 Munekazu Nakamura
- 👤 Masayoshi Inooka
- 👤 Teizaburo Yawata
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 19:15
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G2300/00; C10G2300/10; C10G2300/107
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
148 words
A process for hydrodemetallization of hydrocarbons containing metallic compounds as impurities, comprising contacting hydrogen and hydrocarbons containing metallic compounds as impurities with a catalyst at a temperature of from 300° C. to 500° C. and a hydrogen pressure of from 10 to 300 kg/cm 2 , said catalyst having been prepared by admixing red mud with from 1 to 10% by weight based on the weight of the red mud of a member selected from the group consisting of alumina; clay, alumina-yielding substance and mixtures thereof, said admixture being shaped and calcined at a temperature of 600° C. to 1,100° C., the feed rate of said hydrocarbons being from 0.1 to 20 parts by volume of said hydrocarbons per hour for unit part by volume of said catalyst and the feed rate of said hydrogen being 89 to 1780 Normal liters of hydrogen per liter of said hydrocarbons.
Claim 2
Dependent Claim
148 words
A process for hydrodemetallization of hydrocarbons containing metallic compounds as impurities, comprising contacting hydrogen and hydrocarbons containing metallic compounds as impurities with a catalyst at a temperature of from 300° C. to 500° C. and a hydrogen pressure of from 10 to 300 kg/cm 2 , said catalyst having been prepared by admixing red mud with from 1 to 10% by weight based on the weight of the red mud of a member selected from the group consisting of alumina; clay, alumina-yielding substance and mixtures thereof, said admixture being shaped and calcined at a temperature of 600° C. to 1,100° C., the feed rate of said hydrocarbons being from 0.1 to 20 parts by volume of said hydrocarbons per hour for unit part by volume of said catalyst and the feed rate of said hydrogen being 89 to 1780 Normal liters of hydrogen per liter of said hydrocarbons.
Claim 3
Dependent Claim
28 words
A process in accordance with claim 1 in which the contacting of said hydrocarbons and hydrogen with said catalyst is carried out in the presence of hydrogen sulfide.
Claim 4
Dependent Claim
31 words
A process in accordance with claim 1, wherein the demetallized hydrocarbons from said contacting are then subjected to hydrodesulfurization whereby there is finally obtained hydrocarbons having reduced metal and sulfur contents.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-10-16 | 1982-04-17 | 1982-10-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-10-16 | 1986-04-17 | 1986-10-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-10-16 | 1990-04-17 | 1990-10-17 | $7700.00 | Window Closed / Lapsed |