Method for desulfurizing thiophene derivatives contained in fuels

• US 7,179,368 B2
• Filed: 12/28/2000
• Issued: 02/20/2007
• Est. Priority Date: 12/28/1999
• Status: Expired due to Fees

• Current Assignee: ELF Antar France (Totalenergies Se)
• Original Assignee: ELF Antar France (Totalenergies Se)
• Inventors: Fajula, Francois, Bernard, Jean Rene, Rabion, Alain, Hulea, Vasile
• Primary Examiner(s): Caldarola; Glenn
• Assistant Examiner(s): DOUGLAS, JOHN CHRISTOPHER
• Application Number:
  US10/169,030
• Publication Number:
  US 20030102252A1
• Time in Patent Office: 2,245 Days
• Field of Search: 208/196, 208/208.R, 208/219, 208/226, 208/240
• US Class Current: 208/219
• CPC Class Codes: C07D 333/48 by oxygen atoms
• CPC Class Codes: C10G 27/12 with oxygen-generating compounds, e.g. per-compounds, chromic acid, chromates plumbites or plumbates C10G19/06
• CPC Class Codes: C10G 53/14 including at least one oxidation step
• CPC Class Codes: C10G 67/12 including oxidation as the refining step in the absence of hydrogen

Abstract

The invention concerns a method for selectively desulphurizing thiopene compounds contained in hydrocarbons derived from crude oil distillation, whether refined or not, which consists in oxidising the thiophene sulphur atoms into sulphone in the presence of an oxidising agent and in separating said sulphonated compounds from said hydrocarbons. The invention is characterised in that it consists in oxidising the thiophene compounds in a two-phase turbulent medium comprising a hydrocarbon phase and an aqueous phase, in the presence of at least an oxidising agent soluble in at least one of the two phases and of at least a metal catalyst in soluble or dispersed form in a liquid of in solid form, separation and oxidation occurring simultaneously.

Claims

1. Method of selective desulfurizing of thiophene compounds contained in refined or unrefined hydrocarbons derived from the distillation of crude oil, comprising:

oxidizing thiophene sulfur atoms into sulfone in the presence of an oxidizing agent; and

separating the sulfone compounds from said hydrocarbons,

characterized in that the thiophene compounds are oxidized in a two-phase turbulent phase consisting of a hydrocarbon phase and an aqueous phase, in the presence of at least one oxidizing agent soluble in at least one of the two phases, the oxidizing agent being selected from the group consisting of organic peroxides, hydrogen peroxide, organic hydroperoxides, peracids, alkaline persulfates, and alkaline earth persulfates, and in the presence of at least one metal catalyst selected from the group consisting of (1) metal phthalocyanines and (2) catalysts comprising (i) a support selected from the group consisting of silicas, aluminas, zirconias, amorphous or crystalline aluminosilicates, aluminophosphates, mesoporous solids, and mixtures thereof, and (ii) at least one metal selected from the group consisting of titanium, zirconium, vanadium, chromium, molybdenum, iron, manganese and tungsten, where said metal (ii) can be introduced into the support network or impregnated in complex or non complex form,

wherein the separation and the oxidation occur simultaneously, and wherein the aqueous solution pH is kept under 12.

2. Method as set forth in claim 1, characterized in that an extraction solvent selected from the group consisting of alcanols comprised of 1 to 4 carbon atoms, acetonitrile, formamide dimethyl, nitromethane, and nitrobenzene is added to the two-phase reaction medium, in a water/solvent ratio ranging between 1/99 and 99/1.

3. Method as set forth in claim 1, characterized in that the metal catalyst (expressed in metal)/oxidizing agent molar ratio ranges between 1/10⁵ and 100/1, and in that the reaction starts at ambient temperature and atmospheric pressure.

4. Method as set forth in claim 1, characterized in that the metal phthalocyanine is an iron phthalocyanine.

5. Method as set forth in claim 1, characterized in that the metal phthalocyanine is an iron phthalocyanine supported over a solid phase selected from the group consisting of refractory metal oxides, clays and organic resins.

6. Method as set forth in claim 1, characterized in that the oxidizing agent is a compound with a general formula of R₁^OOR₂, where R₁ and R₂ are independently selected from the group consisting of hydrogen and linear or branched alky groups having 1 to 30 carbon atoms.

7. Method as set forth in claim 6, characterized in that the oxidizing agent is selected from the group consisting of hydrogen peroxide, terbutyl hydroperoxide and terbutyl peroxide.

8. Method as set forth in claim 6, characterized in that the oxidizing agent is hydrogen peroxide.

9. Method as set forth in claim 1, characterized in that the oxidizing agent is a peracid with a formula of R₃COOOH, where R₃ is hydrogen or a linear or branched alkyl group comprised of 1 to 30 carbon atoms.

10. Method as set forth in claim 9, characterized in that the oxidizing agent is selected from the group consisting of peracetic acid, performic acid and perbenzoic acid.

11. Method as set forth in claim 1, characterized in that the aqueous solution/hydrocarbon mass ratio ranges between 10/1 and 1/10.

12. Method as set forth in claim 1, wherein the hydrocarbons are selected from the group consisting of hydrotreated gas oils, kerosenes and gasolines.

13. Method as set forth in claim 1, wherein the metal phthalocyanines are substituted by alkyl groups consisting of 1 to 4 carbon atoms and/or sulfonic groups.

14. Method as set forth in claim 2, wherein the water/solvent ratio ranges between 25/75 and 75/25.

15. Method as set forth in claim 3, wherein the aqueous solution pH ranges between 4 and 9.

16. Method as set forth in claim 4, wherein the iron phthalocyanine is substituted by alkyl groups comprised of 1 to 4 carbon atoms and/or sulfonic groups in an aqueous solution.

17. Method as set forth in claim 5, wherein the iron phthalocyanine is substituted by alkyl groups comprised of 1 to 4 carbon atoms and/or sulfonic groups, the refractory metal oxides are selected from the group consisting of alumina, zirconia, silica, and tungstate, and the organic resins are cationic resins functionalized by ammonium groups.

18. Method as set forth in claim 11, wherein the aqueous solution/hydrocarbon mass ratio ranges between 2/1 and 1/5.

19. Method as set forth in claim 12, wherein the gasolines are gasolines derived from catalytic cracking.

20. Method of selective desulfurizing of thiophene compounds contained in refined or unrefined hydrocarbons derived from the distillation of crude oil, comprising:

oxidizing thiophene sulfur atoms into sulfone in the presence of an oxidizing agent; and

separating the sulfone compounds from said hydrocarbons,

characterized in that the thiophene compounds are oxidized in a two-phase turbulent phase consisting of a hydrocarbon phase and an aqueous phase, in the presence of at least one oxidizing agent soluble in at least one of the two phases, the oxidizing agent being selected from the group consisting of organic peroxides, hydrogen peroxide, organic hydroperoxides, peracids, alkaline persulfates, and alkaline earth persulfates, and in the presence of at least one metal catalyst selected from the group consisting of (1) metal phthalocyanines and (2) catalysts comprising (i) a support selected from the group consisting of silicas, aluminas, zirconias, amorphous or crystalline aluminosilicates, aluminophosphates, mesoporous solids, and mixtures thereof, and (ii) at least one metal selected from the group consisting of titanium, zirconium, vanadium, chromium, molybdenum, iron, manganese and tungsten, where said metal (ii) can be introduced into the support network or impregnated in complex or non complex form,

characterized in that the metal catalyst is a titanium catalyst selected from the group consisting of titanium zeolite without extra-network titanium, with a pore diameter greater than or equal to 0.65 nm and titanium mesoporous composites, and

wherein the separation and the oxidation occur simultaneously.

21. Method as set forth in claim 20, characterized in that the metal catalyst (expressed in metal)/oxidizing agent molar ratio varies from 1/10 to 1/40.

22. Method as set forth in claim 20, wherein the titanium zeolite is titanium beta zeolite.

23. Method of selective desulfurizing of thiophene compounds contained in refined or unrefined hydrocarbons derived from the distillation of crude oil, comprising:

oxidizing thiophene sulfur atoms into sulfone in the presence of an oxidizing agent; and

separating the sulfone compounds from said hydrocarbons,

characterized in that the thiophene compounds are oxidized in a two-phase turbulent phase consisting of a hydrocarbon phase and an aqueous phase, in the presence of at least one oxidizing agent soluble in at least one of the two phases, the oxidizing agent being selected from the group consisting of organic peroxides, hydrogen peroxide, organic hydroperoxides, peracids, alkaline persulfates, and alkaline earth persulfates, and in the presence of at least one metal catalyst selected from the group consisting of (1) metal phthalocyanines and (2) catalysts comprising (i) a support selected from the group consisting of silicas, aluminas, zirconias, amorphous or crystalline aluminosilicates, aluminophosophates, mesoporous solids, and mixtures thereof, and (ii) at least one metal selected from the group consisting of titanium, zirconium, vanadium, chromium, molybdenum, iron, manganese and tungsten, where said metal (ii) can be introduced into the support network or impregnated in complex or non complex form,

wherein the separation and the oxidation occur simultaneously, and

wherein the metal catalyst is a non-oxidized titanium catalyst.