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US3887455A Expired / Lapsed US ⏱️ 0.0 years remaining

Ebullating bed process for hydrotreatment of heavy crudes and residua

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1974-03-25
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Granted: 1975-06-03
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Expires: 1994-03-25
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Abstract

Abstract A process for the hydrotreatment, or hydroconversion, of heavy crudes and residua in an ebullating bed of catalyst, expanded to critical volume ranging from about 20 to 70 percent, preferably 30 to 50 percent, of its settled volume, wherein the catalyst particles are metallized or coked, or both, and segregated on a weight basis and the heavier, more aged and inactive catalyst is collected and removed from the bottom of the bed, while fresh catalyst or precatalyst is added to the top of the bed. The ebullated bed can be staged in one or more initial reactors of a series, product therefrom being fed to a subsequent ebullated or fixed-bed reactor, or reactors. If desired, an ebullating bed from which aged catalyst is stratified and removed, while fresh or regenerated catalyst is added to the top of the bed, can also constitute the final reactor, or reactors, of the series. The ebullating bed reactor, or reactors from which the segregated aged catalyst is removed can be employed in series or in parallel.

Inventors

  • 👤 Glen P Hamner
  • 👤 Kenneth R Clem

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 23:59
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08; C10G2300/00; C10G2300/10; C10G2300/107

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 392 words
IN A PROCESS FOR THE HYDROTREATMENT OF HEAVY CRUDES AND RESIDUA WHICH CONTAIN LARGE QUANTITIES OF 1050*F. + HYDROBON MATERIALS IN AN EBULLATING BED OF CATALYST OPERATED AT CONDITIONS WHEREIN THE CATALYST PARTICLES ARE METALLIZED OR COKED, OR BOTH, PARTICLES ARE ADDED TO THE UPPER PORTION OF THE EBULLATING BED AND CATALYST WITHDRAWN FROM THE BOTTOM OF THE BED, THE IMPROVEMENT COMPRISING: ESTABLISHING A BED OF CATALYST SOLIDS PARTICLES AND EBULLATING SAID BED BY UPFLOW OF A METALS-CONTAINING LIQUID HYDROCARBON FEED INTRODUCED, WITH HYDROGEN, INTO THE BED AT VELOCITY SUFFICIENT TO XPAND THE BED TO A BOLUME RANGING FROM ABOUT 20 TO ABOUT 70 PERCENT, AS CONTRASTED WITH THE VOLUME OF THE BED OF CATALYST WHEREIN THE PARTICLES THEREOF ARE IN QUIESCENT STATE, INTRODUCING A CATALYST OR PRECATALYST COMPRISING AT LEAST ABOUT 50 PERCENT OF ITS TOTAL PORE VOLUME OF ABSOLUTE DIAMTER WITHIN THE RANGE OF FROM 100A TO ABOUT 300A, AND LESS THAN ABOUT 20 PERCENT OF ITS TOTAL PORE VOLUME OF ABSOLUTE DIAMETER WITHIN THE RANGE OF 0 TO ABOUT 100A, A SURFACE AREA RANGING AT LEAST ABOUT 200 M2/G TO ABOUT 600 M1/G, A PORE VOLUME RANGING FROM ABOUT 0.8 TO ABOUT 3.0 CC/G, AND A DENSITY RANGING FROM ABOUT 0.25 TO ABOUT 0.7 G/CC, INTO THE TOP OF THE EBULLATING BED, CONDUCTING THE REACTION AT CONDITIONS CHARACTERIZED AS FOLLOWS, TEMPERATURE, *F.(E.I.T.) START-OF-RUN 650 END-OF-RUN 850 PRESSURE, PSI 500-10,000 HYDROGEN RATE, SCF/B 3000-20,000 SPACE VELOCITY, LHSV 0.2-3.0 TO PRODUCE STRATIFICATION AND GRADIING OF CATALYST PARTICLES AS A RESULT OF INCREASED DENSITY CAUSED BY ABSORPTION OF COKE OR METALS, OR BOTH, IN DIRECT RELATION WITH CATALYST AGE, THE MORE AGED CATALYST PARTICLES SETTLING TO THE BOTTOM OF THE EBULLATING BED, AND REMOVING STRATIFIED CATALYST PARTICLES FROM THE BOTTOM OF THE EBULLATING BED CHARACTERIZED AS CONTAINING A COMPOSITE OF FROM ABOUT 5 TO ABOUT 50 PERCENT OF A GROUP VIB METAL, OR COMPOUND THEREOF, OR FROM ABOUT 1 TO ABOUT 12 PERCENT OF A GROUP VIII METAL, OR COMPOUND THEREOF, OR ADMIXTURE OF BOTH SAID GROUP VIB AND GROUP VIII METALS, OR COMPOUNDS THEREOF, MEASURED AS OXIDES, A POROUS INORGAINC OXIDE SUPPORT, AND HAVING A DENSITY AT LEAST ABOUT 0.1 G/CC GREATER THAN THE DENSITY OF THE CATALYST OR PRECATALYST ADDED TO THE TOP OF THE BED AS A RESULT OF HAVING ABSORBED METALS OR COKE, OR BOTH, DURING THE REACTION.
Claim 2
Dependent Claim 392 words
IN A PROCESS FOR THE HYDROTREATMENT OF HEAVY CRUDES AND RESIDUA WHICH CONTAIN LARGE QUANTITIES OF 1050*F. + HYDROBON MATERIALS IN AN EBULLATING BED OF CATALYST OPERATED AT CONDITIONS WHEREIN THE CATALYST PARTICLES ARE METALLIZED OR COKED, OR BOTH, PARTICLES ARE ADDED TO THE UPPER PORTION OF THE EBULLATING BED AND CATALYST WITHDRAWN FROM THE BOTTOM OF THE BED, THE IMPROVEMENT COMPRISING: ESTABLISHING A BED OF CATALYST SOLIDS PARTICLES AND EBULLATING SAID BED BY UPFLOW OF A METALS-CONTAINING LIQUID HYDROCARBON FEED INTRODUCED, WITH HYDROGEN, INTO THE BED AT VELOCITY SUFFICIENT TO XPAND THE BED TO A BOLUME RANGING FROM ABOUT 20 TO ABOUT 70 PERCENT, AS CONTRASTED WITH THE VOLUME OF THE BED OF CATALYST WHEREIN THE PARTICLES THEREOF ARE IN QUIESCENT STATE, INTRODUCING A CATALYST OR PRECATALYST COMPRISING AT LEAST ABOUT 50 PERCENT OF ITS TOTAL PORE VOLUME OF ABSOLUTE DIAMTER WITHIN THE RANGE OF FROM 100A TO ABOUT 300A, AND LESS THAN ABOUT 20 PERCENT OF ITS TOTAL PORE VOLUME OF ABSOLUTE DIAMETER WITHIN THE RANGE OF 0 TO ABOUT 100A, A SURFACE AREA RANGING AT LEAST ABOUT 200 M2/G TO ABOUT 600 M1/G, A PORE VOLUME RANGING FROM ABOUT 0.8 TO ABOUT 3.0 CC/G, AND A DENSITY RANGING FROM ABOUT 0.25 TO ABOUT 0.7 G/CC, INTO THE TOP OF THE EBULLATING BED, CONDUCTING THE REACTION AT CONDITIONS CHARACTERIZED AS FOLLOWS, TEMPERATURE, *F.(E.I.T.) START-OF-RUN 650 END-OF-RUN 850 PRESSURE, PSI 500-10,000 HYDROGEN RATE, SCF/B 3000-20,000 SPACE VELOCITY, LHSV 0.2-3.0 TO PRODUCE STRATIFICATION AND GRADIING OF CATALYST PARTICLES AS A RESULT OF INCREASED DENSITY CAUSED BY ABSORPTION OF COKE OR METALS, OR BOTH, IN DIRECT RELATION WITH CATALYST AGE, THE MORE AGED CATALYST PARTICLES SETTLING TO THE BOTTOM OF THE EBULLATING BED, AND REMOVING STRATIFIED CATALYST PARTICLES FROM THE BOTTOM OF THE EBULLATING BED CHARACTERIZED AS CONTAINING A COMPOSITE OF FROM ABOUT 5 TO ABOUT 50 PERCENT OF A GROUP VIB METAL, OR COMPOUND THEREOF, OR FROM ABOUT 1 TO ABOUT 12 PERCENT OF A GROUP VIII METAL, OR COMPOUND THEREOF, OR ADMIXTURE OF BOTH SAID GROUP VIB AND GROUP VIII METALS, OR COMPOUNDS THEREOF, MEASURED AS OXIDES, A POROUS INORGAINC OXIDE SUPPORT, AND HAVING A DENSITY AT LEAST ABOUT 0.1 G/CC GREATER THAN THE DENSITY OF THE CATALYST OR PRECATALYST ADDED TO THE TOP OF THE BED AS A RESULT OF HAVING ABSORBED METALS OR COKE, OR BOTH, DURING THE REACTION.
Claim 3
Dependent Claim 223 words
In a process for the hydrotreatment of heavy crudes and residua which contain large quantities of 1050*F.+ hydrobon materials in an ebullating bed of catalyst operated at conditions wherein the catalyst particles are metallized or coked, or both, particles are added to the upper portion of the ebullating bed and catalyst withdrawn from the bottom of the bed, the improvement comprising: establishing a bed of catalyst solids particles and ebullating said bed by upflow of a metals-containing liquid hydrocarbon feed introduced, with hydrogen, into the bed at velocity sufficient to expand the bed to a volume ranging from about 20 to about 70 percent, as contrasted with the volume of the bed of catalyst wherein the particles thereof are in quiescent state, introducing a catalyst or precatalyst comprising at least about 50 percent of its total pore volume of absolute diameter within the range of from about 100A to about 300A, and less than about 20 percent of its tOtal pore volume of absolute diameter within the range of 0 to about 100A, a surface area ranging at least about 200 m2/g to about 600 m2/g, a pore volume ranging from about 0.8 to about 3.0 cc/g, and a density ranging from about 0.25 to about 0.7 g/cc, into the top of the ebullating bed, conducting the reaction at conditions characterized as follows,
Claim 4
Dependent Claim 223 words
In a process for the hydrotreatment of heavy crudes and residua which contain large quantities of 1050*F.+ hydrobon materials in an ebullating bed of catalyst operated at conditions wherein the catalyst particles are metallized or coked, or both, particles are added to the upper portion of the ebullating bed and catalyst withdrawn from the bottom of the bed, the improvement comprising: establishing a bed of catalyst solids particles and ebullating said bed by upflow of a metals-containing liquid hydrocarbon feed introduced, with hydrogen, into the bed at velocity sufficient to expand the bed to a volume ranging from about 20 to about 70 percent, as contrasted with the volume of the bed of catalyst wherein the particles thereof are in quiescent state, introducing a catalyst or precatalyst comprising at least about 50 percent of its total pore volume of absolute diameter within the range of from about 100A to about 300A, and less than about 20 percent of its tOtal pore volume of absolute diameter within the range of 0 to about 100A, a surface area ranging at least about 200 m2/g to about 600 m2/g, a pore volume ranging from about 0.8 to about 3.0 cc/g, and a density ranging from about 0.25 to about 0.7 g/cc, into the top of the ebullating bed, conducting the reaction at conditions characterized as follows,
Claim 5
Dependent Claim 20 words
The process of claim 1 wherein the ebullated bed is expanded from about 30 to about 50 during the operation.
Claim 6
Dependent Claim 57 words
The process of claim 1 wherein the catalyst introduced into the top of the ebullating bed contains at least about 75 percent of its total pore volume within the range of about 100A to about 300A, and less than 10 percent of its total pore volume of absolute diameter within the range of 0 to about 100A.
Claim 7
Dependent Claim 23 words
The process of claim 1 wherein the catalyst introduced into the top of the ebullating bed contains the following distribution of pore diameters:
Claim 8
Dependent Claim 15 words
The process of claim 4 wherein the catalyst contains the following distribution of pore diameters:
Claim 9
Dependent Claim 61 words
The process of claim 1 wherein the catalyst introduced into the top of the ebullating bed contains at least about 50 percent of the total pore volume in pore diameters ranging from about 200A to about 300A, surface area ranging at least about 250 m2/g to about 450 m2/g and pore volume ranging from about 1.1 cc/g to about 1.9 cc/g.
Claim 10
Dependent Claim 27 words
The catalyst of claim 6 wherein less than 10 percent of the total pore volume is of absolute pore diameter within the range of 0 to 100A.
Claim 11
Dependent Claim 28 words
The process of claim 1 wherein the catalyst introduced into the top of the ebullating bed is of density ranging from about 0.4 g/cc to about 0.6 g/cc.
Claim 12
Dependent Claim 15 words
The process of claim 1 wherein the reaction is conducted at conditions characterized as follows:
Claim 13
Dependent Claim 43 words
The process of claim 1 wherein the density of the catalyst removed from the bottom of the ebullating bed ranges from about 0.2 g/cc to about 0.6 g/cc greater than the density of the catalyst introduced into the top of the ebullating bed.
Claim 14
Dependent Claim 31 words
The process of claim 10 wherein the density ranges from about 0.3 g/cc to about 0.5 g/cc greater than the density of the catalyst introduced into the top of the bed.
Claim 15
Dependent Claim 17 words
The process of Claim 1 wherein the feed introduced into the ebullating bed is characterized as follows:
Claim 16
Dependent Claim 39 words
The process of claim 12 wherein the reaction is conducted at severities sufficient to convert at least about 30 percent of the 1050*F.+ material to 1050*F.- material, while removing at least about 80% of the metals from the feed.
Claim 17
Dependent Claim 17 words
The process of claim 1 wherein the feed introduced into the ebullating bed is characterized as follows:
Claim 18
Dependent Claim 39 words
The process of claim 14 wherein the reaction is conducted at severities sufficient to convert at least about 30 percent of the 1050*F.+ material to 1050*F.- material, while removing at least about 80% of the metals from the feed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-06-02 1978-12-02 1979-06-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-06-02 1982-12-02 1983-06-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-06-02 1986-12-02 1987-06-03 $7700.00 Window Closed / Lapsed

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