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US3623973A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing one- and two-ring aromatics from polynuclear aromatic feedstocks

Assignee: Bethlehem Steel Corp
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Filing: 1969-11-25
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Granted: 1971-11-30
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Expires: 1989-11-25
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Abstract

Abstract In a process for upgrading a topped-tar fraction of coal tar, topped-tar feedstock containing largely polynuclear aromatic hydrocarbons is hydrocracked in a hydrogen atmosphere in a first reaction zone at a temperature and pressure sufficient to hydrocrack the large molecules to three- and two-ring aromaticnaphthenes. The hydrocracked feed which also contains olefins, is catalytically hydrotreated in a second reaction zone to saturate the olefins, and the feed is then catalytically treated in a third reaction zone at a temperature, pressure and hydrogen to hydrocarbon feed mol ratio sufficient to hydrocrack the threeand two-ring compounds to two- and one-ring aromatics, while, at the same time, naphthenes are dehydrogenated to aromatics, the alkyl aromatics are hydrodealkylated to nonsubstituted aromatic compounds, and substantially all oxygen, nitrogen and sulfur compounds unreacted in the first and second treatment zones are hydrorefined.

Inventors

  • 👤 Mehmet Orhan Tarhan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 13:20
CPC Classifications
C; C10; C10G; C10G47/00; C10G2400/00; C10G2400/30

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 27 words
A process according to claim 1 wherein the temperature, pressure and hydrogen-to-feed mol ratio in the third reaction zone are 560*-660* C., 400-1,500 p.s.i.g. and 4-12 respectively.
Claim 2
Dependent Claim 22 words
A process according to claim 2 wherein the liquid hourly space velocity in the first reaction zone is from 0.1-2.0 vol./(hr.)(catalyst vol.).
Claim 3
Dependent Claim 23 words
A process according to claim 2 wherein the reactions in the third reaction zone are performed in the presence of a chromia-alumina catalyst.
Claim 4
Dependent Claim 23 words
A process according to claim 2 wherein the temperature and pressure in the first reaction zone are 400*-550* C. and 1,000-10,000 p.s.i.g. respectively.
Claim 5
Dependent Claim 27 words
A process according to claim 4 wherein the reaction in the first reaction zone is performed in the presence of a metal sulfide catalyst supported on alumina.
Claim 6
Dependent Claim 31 words
A process according to claim 1, wherein the polynuclear aromatic hydrocarbon feedstock is obtained from the carbonization or gasification of a coal of the group consisting of bituminous, subbituminous, and lignite.
Claim 7
Dependent Claim 21 words
A process according to claim 1, wherein the polynuclear aromatic hydrocarbon feedstock is a topped tar obtained from high-temperature coal tar.
Claim 8
Dependent Claim 17 words
A process according to claim 1, wherein the polynuclear aromatic hydrocarbon feedstock is a crude coal tar.
Claim 9
Dependent Claim 78 words
A process according to claim 9 wherein chemical oil and C8 to C10 hydrocarbons are individually separated from the feedstock, the chemical oil is first hydrotreated in an additional reaction zone under conditions sufficient to saturate the olefins and remove oxygen from phenols without appreciably saturating aromatic rings, and is then treated in the third reaction zone (C), and the C8 to C10 hydrocarbons are treated only in the second and third reaction zones (B) and (C) respectively.

References Cited (Backward Citations)

US2958643A Cited
US3197518A Cited
US3317622A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-11-29 1975-05-31 1975-11-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-11-29 1979-05-31 1979-11-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-11-29 1983-05-31 1983-11-30 $7700.00 Window Closed / Lapsed

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