Removal of sulfur-containing compounds from liquid hydrocarbon streams

• US 6,368,495 B1
• Filed: 10/12/2000
• Issued: 04/09/2002
• Est. Priority Date: 06/07/1999
• Status: Expired due to Term

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Kocal, Joseph A., Brandvold, Timothy A.
• Primary Examiner(s): Preisch, Nadine
• Application Number:
  US09/689,550
• Time in Patent Office: 544 Days
• Field of Search: 208/208.R, 208/243, 208/244, 208/249, 208/88, 208/240
• US Class Current: 208/240
• CPC Class Codes: C10G 27/04 with oxygen or compounds generating oxygen

Abstract

A novel process effective for the removal of organic sulfur compounds from liquid hydrocarbons is disclosed. The process more specifically addresses the removal of thiophenes and thiophene derivatives from a number of petroleum fractions, including gasoline, diesel fuel, and kerosene. In the first step of the process, the liquid hydrocarbon is subjected to oxidation conditions in order to oxidize at least some of the thiophene compounds to sulfones. Then, these sulfones can be catalytically decomposed to hydrocarbons (e.g. hydroxybiphenyl) and volatile sulfur compounds (e.g. sulfur dioxide). The hydrocarbon decomposition products remain in the treated liquid as valuable blending components, while the volatile sulfur compounds are easily separable from the treated liquid using well-known techniques such as flash vaporization or distillation.

Claims

1. A process for treating a hydrocarbon feed stream containing an organic sulfur compound, the process comprising the steps of:

(a) contacting the hydrocarbon feed stream with an oxidizing agent at oxidation conditions, thereby yielding an effluent stream containing an oxidized organic sulfur compound, and;

(b) contacting the effluent stream with a solid decomposition catalyst consisting essentially of a solid acid or base selected from the group consisting of layered double hydroxides, molecular sieves, alumina, silica, zirconia, and mixtures thereof at decomposition conditions effective to decompose the oxidized organic sulfur compound, thereby yielding a treated hydrocarbon stream and a volatile sulfur compound.

2. The process of claim 1 where the liquid hydrocarbon feed stream is a petroleum distillate selected from the group consisting of naphtha, gasoline, diesel fuel, jet fuel, kerosene, vacuum gas oil, and mixtures thereof.

3. The process of claim 1 where the liquid hydrocarbon feed stream is a hydrotreated petroleum distillate selected from the group consisting of hydrotreated naphtha, hydrotreated gasoline, hydrotreated diesel fuel, hydrotreated jet fuel, hydrotreated kerosene, hydrotreated vacuum gas oil, and mixtures thereof.

4. The process of claim 1 where the organic sulfur compound is selected from the group consisting of thiophene, benzothiophene, dibenzothiophene, alkylated dibenzothiophenes, and mixtures thereof.

5. The process of claim 1 where the oxidation conditions include a temperature from about 40°

C. to about 120°

C. and an absolute pressure from about 0.5 to about 15 atmospheres.

6. The process of claim 1 where the oxidizing agent is selected from the group consisting of alkyl hydroperoxides, peroxides, percarboxylic acids, oxygen, air, and mixtures thereof.

7. The process of claim 1 where the oxidizing agent is present in an amount from about 1 to about 100 moles per mole of the organic sulfur compound.

8. The process of claim 1 where the oxidation conditions include a residence time from about 1 to about 48 hours.

9. The process of claim 1 where the oxidation step is carried out in the presence of an oxidation catalyst comprising a solid carrier having a metal deposited thereon.

10. The process of claim 9 where the solid carrier is a molecular sieve or an inorganic metal oxide.

11. The process of claim 9 where the metal is selected from the group consisting of molybdenum, tungsten, chromium, vanadium, niobium, tantalum, titanium, cobalt, and mixtures thereof.

12. The process of claim 9 where the oxidation conditions include a weight hourly space velocity from about 0.1 to about 10 hr⁻

1.

13. The process of claim 1 where the decomposition conditions include a non-reducing environment, a temperature from about 200°

C. to about 600°

C., an absolute pressure from about 0.5 to about 20 atmospheres, and a weight hourly space velocity from about 0.1 to about 10 hr<sup>−

1</sup>.

14. The process of claim 13 where the decomposition conditions include an absolute pressure from about 5 to about 10 atmospheres.

15. The process of claim 13 where the decomposition conditions include a temperature from about 350°

C. to about 400°

C.

16. The process of claim 1 where the volatile sulfur compound is sulfur dioxide.

17. The process of claim 1 where the treated liquid stream contains less than about 60% of the organic sulfur compound in the liquid feed.

18. The process of claim 1 further comprising, subsequent to step (b), the step of:

hydrotreating the treated hydrocarbon stream.

19. The process of claim 1 further comprising, subsequent to step (b), the step of:

separating the treated hydrocarbon stream from the volatile sulfur compound.

20. The process of claim 19 where the separation is carried out using flash vaporization or distillation.