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US4279736A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of hydrorefining asphaltenic hydrocarbon feedstocks

Assignee: Individual
•
Filing: 1979-10-23
•
Granted: 1981-07-21
•
Expires: 1999-10-23
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Abstract

Abstract A method of hydrorefining an asphaltenic charge stock is described which comprises effecting said reaction utilizing a titanium sulfide catalyst in a hydrogen sulfide-containing H 2 atmosphere. The catalyst may be employed in slurry form or composited with a high surface area coke support. Preferably chloride is also present in the catalyst. The hydrogen sulfide suitably is present in the gas phase in an amount of from about 10 to about 25 mol. percent based on the moles of H 2 present.

Inventors

  • 👤 William K. T. Gleim

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 08:21
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/06; B01J27/08; B01J27/10; B01J27/02; B01J27/04; C; C10; C10G; C10G2300/00; C10G2300/10; C10G2300/107

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 60 words
A method of hydrorefining an asphaltenic charge stock in a hydrogen atmosphere which comprises effecting said reaction in the presence of a mixture of titanium sulfides wherein the molecular ratio of titanium to sulfide is from about 1:2 to about 1:3 and in the presence of from about 10 to about 25 mol. percent hydrogen sulfide based on said hydrogen.
Claim 2
Independent Claim 60 words
A method of hydrorefining an asphaltenic charge stock in a hydrogen atmosphere which comprises effecting said reaction in the presence of a mixture of titanium sulfides wherein the molecular ratio of titanium to sulfide is from about 1:2 to about 1:3 and in the presence of from about 10 to about 25 mol. percent hydrogen sulfide based on said hydrogen.
Claim 3
Dependent Claim 16 words
The method of claim 1 wherein the titanium sulfide is in the form of a slurry.
Claim 4
Dependent Claim 62 words
The method of claim 1 wherein the titanium sulfide is in the form of a slurry, and the titanium sulfide further comprises from about 1% to about 10% by weight chloride based on the weight of titanium sulfide, said chlorine being present in the form of titanium chloride, said titanium chloride having 2 or less chlorine atoms for each atom of titanium.
Claim 5
Dependent Claim 33 words
The method of claim 3 wherein the process is effected at a pressure of from about 1,000 to about 3,000 p.s.i.g. and a temperature of from about 250° C. to about 400° C.
Claim 6
Dependent Claim 32 words
The method of claim 1 wherein the catalyst further comprises titanium sulfide and titanium chloride composited with a high surface area coke of from about 200 to about 500 m 2 /g.
Claim 7
Dependent Claim 24 words
The method of claim 5 wherein the catalyst further comprises from about 1% to about 10% by weight chloride based on the titanium sulfide.
Claim 8
Dependent Claim 20 words
The method of claim 5 wherein the carbon support is a low temperature coke produced from brown coal or lignite.
Claim 9
Dependent Claim 20 words
The method of claim 6 wherein the carbon support is a low temperature coke produced from brown coal or lignite.
Claim 10
Dependent Claim 85 words
The method of claim 6 wherein the titanium sulfide is in the form of a slurry, and the titanium sulfide further comprises (1) a mixture of titanium sulfides wherein the molecular ratio of titanium to sulfide is from about 1:2 to about 1:3 and (2) from about 1% to about 10% by weight chlorine based on the weight of titanium sulfide, said chlorine being present in the form of titanium chloride, said titanium chloride having 3 or less chlorine atoms for each atom of titanium.
Claim 11
Dependent Claim 17 words
The method of claim 1 wherein said process is effected at a temperature below about 300° C.
Claim 12
Dependent Claim 17 words
The method of claim 2 wherein said process is effected at a temperature below about 300° C.
Claim 13
Dependent Claim 17 words
The method of claim 5 wherein said process is effected at a temperature below about 300° C.
Claim 14
Dependent Claim 17 words
The method of claim 6 wherein said process is effected at a temperature below about 300° C.
Claim 15
Dependent Claim 17 words
The method of claim 7 wherein said process is effected at a temperature below about 300° C.
Claim 16
Dependent Claim 17 words
The method of claim 8 wherein said process is effected at a temperature below about 300° C.

References Cited (Backward Citations)

US2038599A Cited
US2127383A Cited
DE1224288B Cited
US4214977A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-07-20 1985-01-19 1985-07-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-07-20 1989-01-19 1989-07-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-07-20 1993-01-19 1993-07-21 $7700.00 Window Closed / Lapsed

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