CoMo and NiMo catalyst stacking for renewable diesel

Patent metadata

Field	Value
Publication number	US-9523046-B2
Application number	US-201314097582-A
Country	US
Kind code	B2
Filing date	Dec 5, 2013
Priority date	Dec 21, 2012
Publication date	Dec 20, 2016
Grant date	Dec 20, 2016

Abstract

Methods are provided herein for co-processing of biocomponent feeds as well processing of mineral feeds in a reaction system at hydrogen partial pressures of about 500 psig (3.4 MPag) or less. The methods include using stacked beds of both CoMo and NiMo catalysts. The stacked catalyst beds provided unexpectedly high catalyst activity as the input feed to a reaction system was switched between a mineral feed and a feed containing both mineral and biocomponent portions. Additionally, use of stacked catalyst beds can allow for maintenance of the activity for the catalyst system in a reaction system while still achieving a desired activity for both types of feeds.

First claim

What is claimed is:

1. A method for hydroprocessing sulfur-containing feeds, comprising:
exposing a first feedstock comprising a first mineral fraction and a bio-derived fraction to a first supported catalyst comprising a first Group VI metal and a Group VIII metal selected from Co or Ni under first effective hydrodesulfurization conditions, the first effective hydrodesulfurization conditions including a hydrogen partial pressure of about 500 psig (3.4 MPag) or less, to form a first effluent, the first feedstock comprising at least about 0.5 wt % of oxygen, at least about 800 wppm of sulfur, and from 1 wt % to 35 wt % of the bio-derived fraction;
exposing the first effluent to a second supported catalyst comprising a second Group VI metal and a Group VIII metal selected from Co or Ni, in the presence of hydrogen under the first effective hydrodesulfurization conditions to form a first desulfurized product having a sulfur content of about 200 wppm or less, the selected Group VIII metal in the second catalyst being different from the selected Group VIII metal in the first catalyst;
exposing a second feedstock comprising a second mineral fraction to at least a portion of the first supported catalyst in the presence of hydrogen under second effective hydrodesulfurization conditions to form a second effluent, the second effective hydrodesulfurization conditions including a hydrogen partial pressure of about 500 psig (3.4 MPag) or less, the second feedstock containing less than about 0.5 wt % of a bio-derived fraction and having a sulfur content of at least about 800 wppm, the at least a portion of the first supported catalyst comprising at least about 80 vol % of the first supported catalyst that was exposed to the first feedstock; and
exposing the second effluent to at least a portion of the second supported catalyst in the presence of hydrogen under the second effective hydrodesulfurization conditions for forming a second desulfurized product having a sulfur content of about 200 wppm or less, the at least a portion of the second supported catalyst comprising at least about 80 vol % of the second supported catalyst that was exposed to the first feedstock,
wherein the first supported catalyst and the second supported catalyst form a stacked bed of catalysts.

2. The method of claim 1 , wherein at least one of the first Group VI metal and the second Group VI metal comprises Mo, W, or a combination thereof.

3. The method of claim 1 , wherein the first effective hydrodesulfurization conditions comprise an LHSV of 0.3 to 5.0 hr −1 , a hydrogen partial pressure of at least about 200 psig (1.4 MPa), a treat gas containing at least about 80% hydrogen (remainder inert gas) with a hydrogen treat gas rate of about 500 scf/bbl (84 m 3 /m 3 ) to about 10000 scf/bbl (1685 m 3 /m 3 ), and a temperature of from about 500° F. (260° C.) to about 800° F. (427° C.).

4. The method of claim 3 , wherein the second effective hydrodesulfurization conditions comprise an LHSV of 0.3 to 5.0 hr −1 , a hydrogen partial pressure of at least about 200 psig (1.4 MPa), a treat gas containing at least about 80% hydrogen (remainder inert gas) with a hydrogen treat gas rate of about 500 scf/bbl (84 m 3 /m 3 ) to about 10000 scf/bbl (1685 m 3 /m 3 ), and a temperature of from about 500° F. (260° C.) to about 800° F. (427° C.).

5. The method of claim 4 , wherein the second effective hydrodesulfurization conditions comprise a hydrogen partial pressure that differs from a hydrogen partial pressure of the first effective hydrodesulfurization conditions by about 20% or less.

6. The method of claim 4 , wherein the second effective hydrodesulfurization conditions comprise a temperature that differs from a reaction temperature of the first effective hydrodesulfurization conditions by about 20% or less.

7. The method of claim 1 , wherein the first supported catalyst comprises Co and the first Group VI metal is Mo.

8. The method of claim 7 , wherein the first effective hydrodesulfurization conditions comprise an LHSV of 0.3 to 5.0 hr −1 , a hydrogen partial pressure of about 300 psig (2.1 MPag) to about 400 psig (2.8 MPag), a treat gas containing at least about 80% hydrogen (remainder inert gas) with a hydrogen treat gas rate of about 500 scf/bbl (84 m 3 /m 3 ) to about 10000 scf/bbl (1685 m 3 /m 3 ), and a temperature of from about 500° F. (260° C.) to about 800° F. (427° C.).

9. The method of claim 1 , wherein a support for at least one of the first supported catalyst and the second supported catalyst comprises alumina, silica, Mania, zirconia, amorphous carbon, or a combination thereof.

10. The method of claim 1 , wherein the at least a portion of the first supported catalyst comprises at least about 90 vol % of the first supported catalyst that was exposed to the first feedstock.

11. The method of claim 1 , wherein the at least a portion of the second supported catalyst comprises at least about 90 vol % of the second supported catalyst that was exposed to the first feedstock.

12. The method of claim 1 , wherein the first feedstock has an oxygen content of about 1.0 wt %.

13. The method of claim 1 , wherein the first feedstock comprises at least about 10 wt % of the bio-derived fraction.

14. A method for hydroprocessing sulfur-containing feeds, comprising:
exposing a second feedstock comprising a second mineral fraction to a first supported catalyst comprising a Group VI metal and a Group VIII metal selected from Co or Ni in the presence of hydrogen under first effective hydrodesulfurization conditions to form a first effluent, the second feedstock containing less than about 0.5 wt % of a bio-derived fraction and at least about 800 wppm of sulfur, at least about 80 vol % of the first supported catalyst having been previously exposed to a first feedstock under first effective hydrodesulfurization conditions, the first feedstock comprising a first mineral fraction and a first bio-derived fraction and having an oxygen content of at least about 1.0 wt %, the first effective hydrodesulfurization conditions including a partial pressure of hydrogen of about 400 psig or less;
exposing the first effluent to a second supported catalyst comprising a Group VI metal and a Group VIII metal selected from Co or Ni, in the presence of hydrogen under the second effective hydrodesulfurization conditions to form a first desulfurized product having a sulfur content of about 200 wppm or less, the selected Group VIII metal in the second catalyst being different from the selected Group VIII metal in the first catalyst, at least about 80 vol % of the second supported catalyst having been previously exposed to the first feedstock under the first effective hydrodesulfurization conditions;
exposing a third feedstock comprising a third mineral fraction and a third bio-derived fraction to at least a portion of the first supported catalyst in the presence of hydrogen under third effective hydrodesulfurization conditions to form a second effluent, the third feedstock having an oxygen content of at least about 0.5 wt %, a sulfur content of at least about 800 wppm, and containing from 1 wt % to about 35 wt % of the second bio-derived fraction, the at least a portion of the first supported catalyst corresponding to at least about 80 vol % of the first supported catalyst that was exposed to the second feedstock; and
exposing the second effluent to at least a portion of the second supported catalyst in the presence of hydrogen under the effective hydrodesulfurization conditions for forming a second desulfurized product having a sulfur content of about 200 wppm or less, the at least a portion of the second supported catalyst correspondi

Assignees

• Gatt Joseph E
• Fingland Bradley R
• Lewis William E
• Hanks Patrick L
• Exxonmobil Res & Eng Co

Inventors

• Gatt Joseph E
• Fingland Bradley R
• Lewis William E
• Hanks Patrick L

Classifications

• C10G3/46

  in combination with chromium, molybdenum, tungsten metals or compounds thereof · CPC title

• C10G65/04

  including only refining steps · CPC title

• C10G3/62

  Catalyst regeneration · CPC title

• C10G3/50

  in the presence of hydrogen, hydrogen donors or hydrogen generating compounds · CPC title

• Y02E50/13

  Cross-Sectional Technologies · mapped topic