SYSTEMS, METHODS, AND CATALYSTS FOR PRODUCING A CRUDE PRODUCT

• US 20100098602A1
• Filed: 11/11/2009
• Published: 04/22/2010
• Est. Priority Date: 12/19/2003
• Status: Abandoned Application

• Current Assignee: Opinder Kishan Bhan, Scott Lee Wellington
• Original Assignee: Opinder Kishan Bhan, Scott Lee Wellington
• Inventors: Wellington, Scott Lee, BHAN, Opinder Kishan
• Application Number:
  US12/616,555
• Publication Number:
  US 20100098602A1
• Time in Patent Office: Days
• US Class Current: 422/600
• CPC Class Codes: C10G 2300/107 Atmospheric residues having a boiling point of at least about 538 °C
• CPC Class Codes: C10G 2300/203 Naphthenic acids, TAN
• CPC Class Codes: C10G 29/06 Metal salts, or metal salts deposited on a carrier
• CPC Class Codes: C10G 45/02 to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
• CPC Class Codes: C10G 45/04 characterised by the catalyst used
• CPC Class Codes: C10G 45/08 in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
• CPC Class Codes: C10G 65/04 including only refining steps
• CPC Class Codes: C10G 65/12 including cracking steps and other hydrotreatment steps

Abstract

Methods and systems for contacting a crude feed that has a total acid number (TAN) of at least 0.3 with one or more catalysts produces a total product that includes a crude product are described. The one or more catalysts may include a first catalyst and a second catalyst. The crude product is a liquid mixture at 25° C. and 0.101 MPa and the crude product has a TAN of at most 90% of the TAN of the crude feed. One or more other properties of the crude product may be changed by at least 10% relative to the respective properties of the crude feed.

Claims

1. A system for producing a crude product, comprising:

an upstream contacting zone;

one or more catalysts in the upstream contacting zone, the one or more catalysts comprising a first catalyst, the first catalyst having, per gram of first catalyst, 0.0001 grams to 0.06 grams of;

one or more metals from Column 6 of the Periodic Table, one or more compounds of one or more metals from Column 6 of the Periodic Table, calculated as weight of metal, or mixtures thereof;

a downstream contacting zone positioned downstream of the upstream contacting zone; and

one or more catalysts in the downstream contacting zone, the one or more catalysts comprising a second catalyst, the second catalyst having, per gram of second catalyst, at least 0.02 grams of;

one or more metals from Column 6 of the Periodic Table, one or more compounds of one or more metals from Column 6 of the Periodic Table, calculated as weight of metal, or mixtures thereof.

2. The system of claim 1, wherein the upstream contacting zone and/or downstream contacting zone comprises one or more stacked bed reactors.

3. The system of claim 1, wherein the upstream contacting zone and/or downstream contacting zone comprises one or more ebullating bed reactors.

4. The system of claim 1, wherein the system further comprises

a crude feed conduit coupled to the upstream contacting zone, the crude feed conduit being configured to convey a crude feed to the upstream contacting zone;

a total product conduit coupled to the downstream contacting zone, the total product conduit being configured to convey the total product from the downstream contacting zone; and

one or more gas conduits, at least one of the gas conduits is coupled to the upstream contacting zone, the gas conduits being configured to convey a hydrogen source and/or a carrier gas into the upstream contacting zone and/or downstream contacting zone.

5. The system of claim 1, wherein the system further comprises:

an upstream separation zone coupled to the upstream contacting zone upstream of the upstream contacting zone, the upstream separation zone being configured to produce the crude feed; and

an additional crude feed conduit coupling the upstream separation zone to the upstream contacting zone, the additional crude feed conduit being configured to convey the crude feed from the upstream separation zone to the upstream contacting zone.

6. The system of claim 1, wherein the system further comprises:

a blending zone coupled to the downstream contacting zone downstream of the downstream contacting zone, the blending zone being configured to combine the crude product with one or more process streams and/or one or more crudes to produce a blend;

a crude product conduit coupling the downstream contacting zone to the blending zone, the crude product conduit being configured to convey the crude product from the downstream contacting zone to the blending zone; and

a blend conduit coupled to the blending zone, the blend conduit being configured to convey the blend from the blending zone.

7. The system of claim 6, wherein at least one of the crudes is a crude that is the same as or different from the crude feed.

8. The system of claim 6, wherein the system comprises in addition a stream conduit coupled to the crude product conduit, the stream conduit being configured to convey one or more streams to the crude product conduit.

9. The system of claim 6, wherein the system comprises in addition a stream conduit coupled to the blending zone, the stream conduit being configured to convey one or more streams to the blending zone.

10. The system of claim 1 wherein the system is positioned on or coupled to an offshore facility.

11. The system of claim 1 wherein a total content of Column 6 metal(s), per gram of second catalyst, is equal to or greater than the total content of Column 6 metal(s) in the first catalyst.