Two-stage, close-coupled, dual-catalytic heavy oil hydroconversion process

Patent metadata

Field	Value
Publication number	US-9334452-B2
Application number	US-201113134604-A
Country	US
Kind code	B2
Filing date	Jun 10, 2011
Priority date	Jun 30, 2010
Publication date	May 10, 2016
Grant date	May 10, 2016

Abstract

A process for the production of high yields of high quality products from heavy hydrocarbonaceous feedstock is provided comprising a two-stage, close-coupled process, wherein the first stage comprises a thermal-catalytic zone into which is introduced a mixture comprising the feedstock, coal, dispersed catalyst, and hydrogen; and the second, close-coupled stage comprises a catalytic-hydrotreating zone into which substantially all the effluent from the first stage is directly passed and processed under hydrotreating conditions.

First claim

The invention claimed is:

1. A two-stage, close-coupled process for converting a portion boiling above 1000 degree F. of a heavy hydrocarbonaceous feedstock to produce high yields of high quality fuels boiling below 1000 degrees F. comprising:
a. forming a slurry by dispersing within said feedstock
i. finely divided coal particles in a concentration relative to said feedstock of up to 10.0 percent by weight and
ii. finely divided dispersed catalyst particles in a concentration relative to said feedstock of from about 0.1 to 5.0 percent by weight having activity in the presence of hydrogen;

b. introducing said slurry into a first-stage thermal-catalytic reaction zone under conditions sufficient to convert a portion of the finely divided coal particles into coal liquids;
c. mixing the coal liquids, the finely divided dispersed catalyst particles, and the feedstock in the first-stage thermal-catalytic reaction zone to convert a significant amount of the hydrocarbons in said feedstock boiling above 1000.degree. F. to hydrocarbons boiling below 1000.degree. F. to provide a converted effluent;
d. rapidly and without substantial reduction of pressure passing a substantial portion of the converted effluent of said first-stage thermal-catalytic reaction zone directly into a second-stage catalytic-hydrotreating reaction zone at a reduced temperature relative to said first-stage thermal-catalytic reaction zone;
e. contacting said converted effluent with a supported hydroprocessing catalyst under hydrotreating conditions, including a temperature in the range of 600.degree. F. to 800.degree. F.; and
f. recovering an effluent comprising hydrocarbons boiling below 1000 degrees F. from said second-stage catalytic-hydrotreating reaction zone.

2. The process as claimed in claim 1 wherein substantially all of the converted effluent from said first-stage thermal-catalytic reaction zone is passed into said second-stage catalytic-hydrotreating reaction zone.

3. The process as claimed in claim 1 wherein the dispersed catalyst particles in the first-stage thermal-catalytic reaction zone are not supported on a base and are oxides or sulfides of metals selected from the group consisting of Group VIb, VIIb and VIIIb metals.

4. The process as claimed in claim 1 wherein the dispersed catalyst particles in the first-stage thermal-catalytic reaction zone are not supported on a base and are either a synthetic catalyst or a naturally occurring material.

5. The process as claimed in claim 1 wherein the temperature of said first-stage thermal-catalytic reaction zone is maintained within a range of between 750.degree. F. and 900.degree. F.

6. The process as claimed in claim 1 wherein the temperature of said first-stage thermal-catalytic reaction zone is maintained within a range of between 800.degree. F. and 875.degree. F.

7. The process as claimed in claim 1 wherein the temperature of said second stage catalytic-hydrotreating reaction zone is within a range between 650.Degree. F. and 780.Degree. F.

8. The process as claimed in claim 1 wherein said slurry is introduced into said first-stage thermal-catalytic reaction zone in an upward manner.

9. The process as claimed in claim 1 wherein the percentage of hydrocarbons in the feedstock boiling above 1000.degree. F. converted to hydrocarbons boiling below 1000.degree. F. is at least 50 percent.

10. The process as claimed in claim 1 wherein the percentage of hydrocarbons in the feedstock boiling above 1000.degree. F. converted to hydrocarbons boiling below 1000.degree. F. is at least 75 percent.

11. The process as claimed in claim 1 wherein the percentage of hydrocarbons in the feedstock boiling above 1000.degree. F. converted to hydrocarbons boiling below 1000.degree. F. is at least 90 percent.

12. The process as claimed in claim 1 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, or heavy hydrocarbonaceous liquids.

13. The process as claimed in claim 1 wherein the concentration of said coal particles relative to said feedstock is up to 5.0 percent by weight.

14. The process as claimed in claim 1 wherein the concentration of said dispersed catalyst particles relative to said feedstock is from 0.5 to 1.0 percent by weight.

15. The process as claimed in claim 1 wherein the residence time of the slurry in the first-stage thermal-catalytic reaction zone is from 0.5 to 3 hours.

16. The process as claimed in claim 1 wherein the residence time of the slurry in the first-stage thermal-catalytic reaction zone is from 0.5 to 1.5 hours.

17. The process as claimed in claim 1 wherein the residence time of a material comprised of said converted effluent and said supported hydroprocessing catalyst in the second-stage catalytic-hydrotreating reaction zone is from 0.5 to 4 hours.

18. The process as claimed in claim 1 wherein the residence time of a material comprised of said converted effluent and said supported hydroprocessing catalyst in the second-stage catalytic-hydrotreating reaction zone is from 0.5 to 3 hours.

19. The process as claimed in claim 1 wherein the supported hydroprocessing catalyst in said second-stage catalytic hydrotreating reaction zone is maintained in a fixed, ebullated or moving bed within the reaction zone.

20. The process as claimed in claim 1 wherein the process is maintained at a hydrogen partial pressure from 35 atmospheres to 300 atmospheres.

21. The process as claimed in claim 1 wherein the process is maintained at a hydrogen partial pressure between 100 atmospheres and 200 atmospheres.

22. The process as claimed in claim 1 wherein the process is maintained at a hydrogen partial pressure between 100 atmospheres and 175 atmospheres.

23. The process as claimed in claim 1 , further comprising converting a portion of the finely divided coal particles into coal ash in the first-stage thermal-catalytic reaction zone.

24. The process as claimed in claim 23 further comprising substantially removing metal contaminants in the feedstock in the first stage thermal-catalytic reaction zone by sequestering the metal contaminants with the coal ash.

Assignees

• Cash Dennis R
• Forder Graham J
• Mitchell David S
• Rosenthal Joe W
• Chevron Usa Inc

Inventors

• Cash Dennis R
• Forder Graham J
• Mitchell David S
• Rosenthal Joe W

Classifications

• C10G65/10

  including only cracking steps · CPC title

• C10G2300/205

  Metal content · CPC title

• C10G65/12 Primary

  including cracking steps and other hydrotreatment steps · CPC title

• C10G2300/1077

  Vacuum residues · CPC title

• C10G2300/107

  Atmospheric residues having a boiling point of at least about 538 °C · CPC title