Process for reducing the level of sulfur in a refinery process stream and/or crude oil

• US 5,552,036 A
• Filed: 06/01/1994
• Issued: 09/03/1996
• Est. Priority Date: 06/01/1994
• Status: Expired due to Fees

• Current Assignee: Ashland Incorporated (Bank of Montreal)
• Original Assignee: Ashland Incorporated (Bank of Montreal)
• Inventors: Foret, Todd L., Mansfield, William D., Vidrine, Hubert P.
• Primary Examiner(s): Myers, Helane
• Application Number:
  US08/251,890
• Time in Patent Office: 825 Days
• Field of Search: 208/237, 208/208 R, 208/236, 210/708, 210/749, 210/757
• US Class Current: 208/236
• CPC Class Codes: C10G 29/20 Organic compounds not containing metal atoms
• CPC Class Codes: C10G 29/22 containing oxygen as the only hetero atom

Abstract

This invention relates to a process for reducing the sulfur in a refinery process stream and/or crude oil, which comprises treating said refinery process stream and/or crude oil with an effective sulfur reducing amount of a reducing agent selected from the group consisting of hydrazine, oximes, hydroxylamines, carbohydrazide, erythorbic acid, and mixtures thereof wherein the reducing agent or the hydrocarbon treated has a temperature of at least 50° C.

Claims

1. A process for reducing the sulfur in a refinery process stream selected from the group consisting of an emulsion, water stream, condensate stream, stripping stream, hydrocarbon-containing stream and mixtures thereof comprising:

adding to said refinery process stream an effective sulfur reducing amount of a reducing agent selected from the group consisting of hydrazine, oximes, hydroxylamines, carbohydrazide, erythorbic acid, and mixtures thereof wherein said reducing agent, said refinery process stream, or both have a temperature of at least 50°

C. to thereby reduce the level of sulfur in said refinery process stream.

3. The process of claim 1 wherein the reducing agent is methyl ethyl ketoxime.

4. The process of claim 3 wherein the reducing agent or the refinery process stream treated has a temperature of from 80°

C. to 150°

C.

12. The process of claim 1 wherein said refinery process stream contains a liquid hydrocarbon phase, a gaseous hydrocarbon phase and an aqueous phase.

13. The process of claim 1 wherein the amount of reducing agent is from 5 ppm to 70 ppm based upon the volume amount of the refinery stream.

14. The process of claim 1 wherein the amount of reducing agent is from 5 ppm to 70 ppm based upon the weight of the crude to be treated.

2. The process of claim 2 wherein the amount of reducing agent is from 1 ppm to 100 ppm, said ppm being based upon the volume amount of refinery stream treated.

5. The process of claim 2 wherein the refinery process stream treated is a hydrocarbon stream and the amount of methyl ethyl ketoxime is from 10 ppm to 50 ppm based upon the volume amount of hydrocarbon in the refinery process stream treated.

6. The process of claim 5 wherein the methyl ethyl ketoxime is added to a refinery process stream by adding said methyl ethyl ketoxime to a chemical feed point selected from the group consisting of raw crude, the raw crude tower, stripping steam to crude tower, crude tower reflux, splitter tower feed, reformate feed, and reformer.

7. A process for reducing the sulfur in crude oil comprising:

adding to said refinery process stream an effective sulfur reducing amount of a reducing agent selected from the group consisting of hydrazine, oximes, hydroxylamines, carbohydrazide, erythorbic acid, and mixtures thereof wherein said reducing agent, said refinery process stream, or both have a temperature of at least 50°

C. to thereby reduce the level of sulfur in said crude oil treated.

8. The process of claim 7 wherein the amount of reducing agent is from 1 ppm to 100 ppm based upon the weight of the crude to be treated.

9. The process of claim 8 wherein the reducing agent is methyl ethyl ketoxime.

10. The process of claim 9 wherein the reducing agent or the crude oil treated has a temperature of from 80°

C. to 150°

C.

11. The process of claim 10 wherein the amount of methyl ethyl ketoxime is from 10 ppm to 50 ppm based upon the weight of the crude oil to be treated.