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US4560465A Expired / Lapsed US ⏱️ 0.0 years remaining

Presulfided red mud as a first-stage catalyst in a two-stage, close-coupled thermal catalytic hydroconversion process

Assignee: Chevron USA Inc
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Filing: 1984-08-27
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Granted: 1985-12-24
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Expires: 2004-08-27
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Abstract

Abstract A process for the production of transportation fuels from heavy hydrocarbonaceous feedstock is provided comprising a two-stage, close-coupled process, wherein the first stage comprises a hydrothermal zone into which is introduced a mixture comprising a feedstock and dispersed activated or presulfided red mud having demetalizing and coke-suppressing activity, and hydrogen; and the second, close-coupled stage comprises a hydrocatalytic zone into which substantially all the effluent from the first stage is directly passed and processed under hydrocatalytic conditions.

Inventors

  • 👤 S. Gary Yu
  • 👤 John G. Reynolds

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 19:46
CPC Classifications
C; C10; C10G; C10G47/00; C10G47/02; C10G45/00; C10G45/02; C10G45/04; C10G65/00; C10G65/02; C10G65/10; C10G65/12

Claims Analysis

Total Claims: 23
Claim 1
Independent Claim 207 words
A two-stage, close-coupled process for hydroprocessing a heavy hydrocarbonaceous feedstock at least 30 volume percent of which boils above 1000° F. and which has greater than 100 parts per million by weight total metal contaminants to produce high yields of transportation fuels boiling below 650° F., which comprises: (a) introducing said feedstock and dispersed presulfided red mud having activity sufficient to suppress adverse coke formation under coking conditions and having demetalizing activity, into a first-stage hydrothermal zone in the presence of hydrogen or a mixture of hydrogen and hydrogen sulfide; wherein said feedstock and red mud are introduced into said hydrothermal zone under conditions sufficient to substantially demetalate said feedstock and to convert a significant amount of the hydrocarbons of said feedstock boiling above 1000° F. to hydrocarbons boiling below 1000° F.; (b) rapidly, and without substantial reduction of pressure through the system, passing a substantial portion of the red mud entrained effluent of said first-stage hydrothermal zone directly into a second-stage catalytic reaction zone at a reduced temperature relative to said first-stage hydrothermal zone and contacting said effluent with hydroprocessing catalyst under hydroprocessing conditions, including a temperature in the range of 650° F. to 800° F.; and (c) recovering the effluent from said catalytic reactor zone.
Claim 2
Dependent Claim 207 words
A two-stage, close-coupled process for hydroprocessing a heavy hydrocarbonaceous feedstock at least 30 volume percent of which boils above 1000° F. and which has greater than 100 parts per million by weight total metal contaminants to produce high yields of transportation fuels boiling below 650° F., which comprises: (a) introducing said feedstock and dispersed presulfided red mud having activity sufficient to suppress adverse coke formation under coking conditions and having demetalizing activity, into a first-stage hydrothermal zone in the presence of hydrogen or a mixture of hydrogen and hydrogen sulfide; wherein said feedstock and red mud are introduced into said hydrothermal zone under conditions sufficient to substantially demetalate said feedstock and to convert a significant amount of the hydrocarbons of said feedstock boiling above 1000° F. to hydrocarbons boiling below 1000° F.; (b) rapidly, and without substantial reduction of pressure through the system, passing a substantial portion of the red mud entrained effluent of said first-stage hydrothermal zone directly into a second-stage catalytic reaction zone at a reduced temperature relative to said first-stage hydrothermal zone and contacting said effluent with hydroprocessing catalyst under hydroprocessing conditions, including a temperature in the range of 650° F. to 800° F.; and (c) recovering the effluent from said catalytic reactor zone.
Claim 3
Dependent Claim 202 words
A two-stage, close-coupled process for hydroprocessing a heavy hydrocarbonaceous feedstock at least 30 volume percent of which boils above 1000° F. and which has greater than 100 parts per million by weight total metal contaminants to produce high yields of transportation fuels boiling below 650° F., which comprises: (a) forming a slurry by dispersing within said feedstock presulfided red mud having activity sufficient to suppress adverse coke formation under coking conditions and having demetalizing activity, in the presence of hydrogen or a mixture of hydrogen and hydrogen sulfide; (b) introducing said slurry into a first-stage hydrothermal zone under conditions sufficient to substantially demetalate said feedstock and to convert a significant amount of the hydrocarbons of said feedstock boiling above 1000° F. to hydrocarbons boiling below 1000° F.; (c) rapidly, and without substantial reduction of pressure through the system, passing a substantial portion of the red mud entrained effluent of said first-stage hydrothermal zone directly into a second-stage catalytic reaction zone at a reduced temperature relative to said first-stage hydrothermal zone and contacting said effluent with hydroprocessing catalyst under hydroprocessing conditions, including a temperature in the range of 650° F. to 800° F.; and (d) recovering the effluent from said catalytic reaction zone.
Claim 4
Dependent Claim 202 words
A two-stage, close-coupled process for hydroprocessing a heavy hydrocarbonaceous feedstock at least 30 volume percent of which boils above 1000° F. and which has greater than 100 parts per million by weight total metal contaminants to produce high yields of transportation fuels boiling below 650° F., which comprises: (a) forming a slurry by dispersing within said feedstock presulfided red mud having activity sufficient to suppress adverse coke formation under coking conditions and having demetalizing activity, in the presence of hydrogen or a mixture of hydrogen and hydrogen sulfide; (b) introducing said slurry into a first-stage hydrothermal zone under conditions sufficient to substantially demetalate said feedstock and to convert a significant amount of the hydrocarbons of said feedstock boiling above 1000° F. to hydrocarbons boiling below 1000° F.; (c) rapidly, and without substantial reduction of pressure through the system, passing a substantial portion of the red mud entrained effluent of said first-stage hydrothermal zone directly into a second-stage catalytic reaction zone at a reduced temperature relative to said first-stage hydrothermal zone and contacting said effluent with hydroprocessing catalyst under hydroprocessing conditions, including a temperature in the range of 650° F. to 800° F.; and (d) recovering the effluent from said catalytic reaction zone.
Claim 5
Dependent Claim 28 words
The process as claimed in claim 1 or 2 wherein substantially all of the effluent from said first-stage hydrothermal zone is passed into said second-stage catalytic reaction zone.
Claim 6
Dependent Claim 29 words
The process as claimed in claim 1 or 2 wherein the temperature of said first-stage hydrothermal zone is maintained within a range of between 750° F. to 900° F.
Claim 7
Dependent Claim 52 words
The process as claimed in claim 1 or 2 wherein said red mud has been presulfided by heating red mud to a temperature of from about 600° F. to 900° F. and contacting said red mud with a mixture of hydrogen and hydrogen sulfide for sufficient time to presulfide said red mud.
Claim 8
Dependent Claim 27 words
The process as claimed in claim 5 wherein hydrogen sulfide comprises from about 5 percent by volume to 25 percent by volume of said hydrogen/hydrogen sulfide mixture.
Claim 9
Dependent Claim 31 words
The process as claimed in claim 6 wherein said hydrogen/hydrogen sulfide mixture is contacted with said red mud at a rate of from about 0.1 to 1.5 cubic feet per hour.
Claim 10
Dependent Claim 32 words
The process as claimed in claim 1 or 2 wherein the mixture of hydrogen and hydrogen sulfide present in the first-stage hydrothermal zone comprises at least 2 percent hydrogen sulfide by volume.
Claim 11
Dependent Claim 34 words
The process as claimed in claim 1 or 2 wherein said red mud has been presulfided by treating with sulfur-containing compounds selected from the group consisting of carbon disulfide, polyalkyl sulfides, and polyalkyl polysulfides.
Claim 12
Dependent Claim 34 words
The process as claimed in claim 9 wherein the presulfiding is conducted at a temperature of from about 200° F. to 1000° F. and a pressure of from about 3 atmospheres to 213 atmospheres.
Claim 13
Dependent Claim 47 words
The process as claimed in claim 1 or 2 wherein said feedstock-presulfided red mud mixture or slurry is introduced into said hydrothermal zone in an upward, essentially plug flow manner, and the effluent of said first stage is introduced into said hydrocatalytic zone in an upward manner.
Claim 14
Dependent Claim 35 words
The process as claimed in claim 1 or 2 wherein said amount of hydrocarbons in the feedstock boiling above 1000° F. which is converted to hydrocarbons boiling below 1000° F. is at least 80 percent.
Claim 15
Dependent Claim 21 words
The process as claimed in claim 1 or 2 wherein said metal contaminants in the feedstock include nickel, vanadium, and iron.
Claim 16
Dependent Claim 51 words
The process as claimed in claim 1 or 2 wherein said heavy hydrocarbonaceous feedstock is crude petroleum, topped crude petroleum, reduced crudes, petroleum residua from atmospheric or vacuum distillations, vacuum gas oils, solvent deasphalted tars and oils, and heavy hydrocarbonaceous liquids including residua derived from coal, bitumen, or coal tar pitches.
Claim 17
Dependent Claim 28 words
The process as claimed in claim 1 or 2 wherein the concentration of said presulfided red mud within said feedstock is from 0.01 to 10.0 percent by weight.
Claim 18
Dependent Claim 20 words
The process as claimed in claim 15 wherein said presulfided red mud concentration is less than 1 percent by weight.
Claim 19
Dependent Claim 28 words
The process as claimed in claim 1 or 2 wherein the catalyst in said second-stage catalytic reaction zone is maintained in a supported bed within the reaction zone.
Claim 20
Dependent Claim 25 words
The process as claimed in claim 1 or 2 wherein the process is maintained at a hydrogen partial pressure from 35 atmospheres to 680 atmospheres.
Claim 21
Dependent Claim 20 words
The process as claimed in claim 18 wherein the hydrogen partial pressure is maintained between 100 atmospheres to 340 atmospheres.
Claim 22
Dependent Claim 31 words
The process as claimed in claim 1 or 2 wherein the temperature of said second-stage hydrocatalytic zone is from 15° F. to 200° F. below that of said first-stage hydrothermal zone.
Claim 23
Dependent Claim 50 words
The process as claimed in claim 1 or 2 wherein a substantial portion of the hydroprocessing catalyst in the catalytic reaction zone is a hydrocracking catalyst comprising at least one hydrogenation component selected from Group VI or Group VIII of the Periodic Table, and is supported on a refractory base.

References Cited (Backward Citations)

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US3964995A Cited
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US4017379A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-12-23 1989-06-24 1989-12-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-12-23 1993-06-24 1993-12-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-12-23 1997-06-24 1997-12-24 $7700.00 Window Closed / Lapsed

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