Process for the catalytic oxidation of sulfur, nitrogen and unsaturated compounds from hydrocarbon streams

• US 20020189975A1
• Filed: 05/16/2001
• Published: 12/19/2002
• Est. Priority Date: 05/16/2001
• Status: Active Grant

• Current Assignee: Petroleo Brasileiro SA - Petrobras
• Original Assignee: Petroleo Brasileiro SA - Petrobras
• Inventors: De Souza, Wladmir Ferraz
• Granted Patent: US 6,544,409 B2
• Time in Patent Office: Days
• US Class Current: 208/208R
• CPC Class Codes: C10G 27/00 Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
• 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

Abstract

A process for the catalytic oxidation of sulfur and nitrogen contaminants as well as unsaturated compounds present in a hydrocarbon fossil oil medium is described, the process comprising effecting the oxidation in the presence of at least one peroxide, at least one acid and a pulverized raw iron oxide. The process shows an improved oxidation power towards the contaminants typically present in a fossil oil medium, this deriving from the combination of the peroxy-acid and the hydroxyl radical generated in the reaction medium due to the presence of an iron oxyhydroxide such as a limonite clay, which bears a particular affinity for the oil medium. The process finds use in various applications, from a feedstock for refining until the preparation of deeply desulfurized and deeply denitrified products.

Claims

1. A process for the catalytic oxidation of sulfur, nitrogen and unsaturated compounds from fossil hydrocarbon streams contaminated with said compounds, the process comprising the following steps:

a) Providing a pulverized raw iron oxide;

b) Providing at least one acid

c) Providing at least one peroxide;

d) Oxidizing unsaturated compounds as well as sulfur and nitrogen contaminants by admixing, under atmospheric pressure and equal or higher than ambient temperature, under agitation, said organic acid and said hydrocarbon stream contaminated with sulfur, nitrogen and unsaturated compounds and then said peroxide, so as to obtain a peracid, the molar amount of peroxide and organic acid relative to the sum of the nitrogen and sulfur contents present in the hydrocarbon stream being at least 3.0, at pH between 2.0 and 6.0, for the required period to obtain a hydrocarbon stream where the unsaturated, sulfur and nitrogen contaminants have been partially oxidized;

e) Further oxidizing said unsaturated compounds as well is sulfur and nitrogen contaminants in the presence of oxidant hydroxyl radicals generated by adding to said partially oxidized hydrocarbon stream, under atmospheric pressure and equal or higher than ambient temperature, the higher than ambient temperature being generated by the process itself, under agitation, a catalytic amount of said pulverized iron oxide so as to obtain a slurry of iron oxide, hydrocarbon stream and oxidized unsaturated, sulfur and nitrogen compounds, the reaction conditions being kept during 1-2 hours and an acidic pH between 2.0 and 6.0;

f) After the end of the reaction, filtrating the reaction medium containing an aqueous phase and an oily hydrocarbon phase, and separating the spent iron oxide catalyst;

g) Decanting in order to separate the organic-rich aqueous phase;

h) Correcting the pH of the resulting hydrocarbon phase to values between 6.1 and 9.0 and recovering the oil phase;

i) Post-treating the oil phase to extract the oxidized products at the desired level; and

j) Recovering the post-treated hydrocarbon phase having sulfur compounds in the range of 0.01 weight % and 0.2 weight % and nitrogen compounds in the range of 0.001 weight % to 0.15 weight %, the final olefin content being up to 50% of the original olefin content.

5. A process according to claims 1, 2, 3 or 4 wherein the hydrocarbon fossil stream comprehend a raw petroleum oil or its heavy fractions, alone or admixed in any amount, fuels, lubricants, raw or fractionated shale oil and its fractions alone or admixed in any amounts, liquid coal oil and related products, oil sands and related products.

6. A process according to claims 1, 2, 3 or 4, wherein the End Boiling Point (EBP) of the hydrocarbon fossil stream is ca. 500°

C., that is, gasoil streams and medium distillates, such as heavy diesel oil or light diesel oil, alone or admixed in any amounts.

7. A process according to claims 1, 2, 3, or 4, wherein the hydrocarbon streams contain until 2.0 weight % total S and until 2.0 weight % total N for petroleum-derived streams and shale oil and related-derived streams as well as up to 40 weight % of unsaturated compounds as mono-, di- and polyolefins, open-chained and cyclic.

8. A process according to claims 1, 2, 3 or 4, wherein the at least one peroxide is an organic peroxide selected among an alkyl hydroperoxide and an acyl hydroperoxide of formula ROOH, wherein R is alkyl, H_n+2C_nC(═

O)—

(n>

=1), HC(═

O)—

, Aryl-C(═

O)—

.

9. A process according to claims 1, 2, 3 or 4, wherein the at least one peroxide is an inorganic peroxide consisting of hydrogen peroxide H₂O₂.

10. A process according to claims 1, 2, 3 or 4, wherein the peroxide is a mixture of organic and inorganic peroxide in any amount.

11. A process according to claims 1, 2, 3 or 4, wherein the at least one acid is an organic acid selected among a carboxylic acid, a dicarboxylic acid and a polycarboxylic acid.

12. A process according to claim 11, wherein the organic acid is formic acid, acetic acid, X_mCH_3-mCOOH (m=1˜

3, X═

F, Cl, Br).

13. A process according to claims 1, 2, 3 or 4, wherein the acid is an inorganic acid selected among phosphoric acid, carbonic acid and buffer solutions thereof.

14. A process according to claims 12 or 13, wherein the organic acid is added after an inorganic acid.

15. A process according to claims 1, 2, 3 or 4, wherein alternatively the order of addition of the components for the catalytic oxidation is the oil medium followed by organic acid, then by the pulverized raw iron oxide to obtain a slurry of iron oxide in the fossil oil medium and at least one peroxide.

16. A process according to claims 1, 2, 3 or 4, wherein alternatively the order of addition of the components for the catalytic oxidation is the fossil oil medium to which is added inorganic acid, followed by the raw iron oxide to obtain a slurry of iron oxide in the fossil oil medium, then organic acid and at least one peroxide.

17. A process according to claims 1, 2, 3 or 4, wherein alternatively the order of addition of the components for the catalytic oxidation is the fossil oil medium to which is added at least one peroxide, followed by at least an organic acid and iron oxide.

18. A process according to claims 1, 2, 3 or 4, wherein alternatively the order of addition of the components for the catalytic oxidation is at least an organic acid and at least one peroxide admixed under agitation, followed by the fossil oil medium and the pulverized raw iron oxide.

19. A process according to claims 1, 2, 3 or 4, wherein alternatively the order of addition of the components for the catalytic oxidation is the fossil oil medium to which is added the pulverized raw iron oxide and a peracid.

20. A process according to claims 1, 2, 3 or 4, wherein alternatively the order of addition of the components for the catalytic oxidation is the fossil oil medium to which is added the pulverized iron oxide and then at least an inorganic acid and a peracid.

21. A process according to claims 1, 2, 3 or 4, wherein alternatively all the components for the catalytic oxidation are admixed and introduced simultaneously into the fossil oil medium.

22. A process according to claims 1, 2, 3 or 4, wherein the temperature of said process is of between 20°

C. and 100°

C. in the absence of any added external heating.

23. A process according to claims 1, 2, 3 or 4, wherein the iron oxide compound is selected among amorphous, crystalline and semicrystalline forms of iron oxide compounds.

24. A process according to claims 1, 2, 3 or 4, wherein the pulverized raw iron oxide comprises iron oxyhydroxide of formula FeOOH.

25. A process according to claims 1, 2, 3 or 4, wherein the pulverized raw iron oxide comprises hydrated iron oxyhydroxide of formula FeOOH._nH₂O.

26. A process according to claim 25, wherein the iron oxyhydroxide is selected among the various crystalline forms such as α

-FeOOH (Goethite), γ

-FeOOH (Lepidocrocite), β

-FeOOH (Akaganeite), and δ

′

-FeOOH (Ferroxyhite).

27. A process according to claim 27, wherein the iron oxyhydroxide crystals are embedded in a limonite ore matrix the iron content of which is 40-60 weight percent.

28. A process according to claim 27, wherein the granulometry of the particles of the limonite ore is such that the size of said particles is equal or smaller than 0.71 mm (25 mesh Tyler).

29. A process according to claim 27, wherein the granulometry of the particles of the limonite ore is such that the size of said particles is equal or smaller than 0.25 mm (60 mesh Tyler).

30. A process according to claim 27, wherein the granulometry of the particles of the limonite ore is such that the size of said particles is equal or smaller than 0.04 mm (325 mesh Tyler).

31. A process according to claims 1, 2, 3, or 4, wherein the amount of pulverized raw iron oxide catalyst is of from 0.01 to 5.0 weight %, based on the amount of hydrocarbon stream being submitted to said process.

32. A process according to claims 1, 2, 3, or 4, wherein the amount of iron oxide catalyst is of from 1.0 to 3.0 weight %, based on the amount of hydrocarbon stream being submitted to said process

33. A process according to claim 1, 2, 3 or 4, wherein the spent iron oxidation catalyst separated at the end of the reaction is recycled.

34. A process according to claims 1, 2, 3 or 4, wherein the spent iron oxidation catalyst separated at the end of the reaction is eluted for the removal of the oxidized organic compounds.

35. A process according to claims 1, 2, 3 or 4, wherein the spent iron oxidation catalyst separated at the end of the reaction is used in any industrial application able to use the 40-60 weight % iron present in said spent catalyst.

36. A process according to claims 1, 2, 3 or 4, wherein the post treating step j) comprises extracting the oxidized compounds from the oil phase with water.

37. A process according to claims 1, 2, 3 and 4, wherein the post treating step j) comprises extracting the oxidized compounds from the oil phase with an aqueous solution of up to 10 weight % NaCl brine.

38. A process according to claims 1, 2, 3 or 4, wherein the post treating step j) comprises extracting the oxidized compounds from the oil phase with an aprotic polar solvent.

39. A process according to claim 38, wherein the aprotic polar solvent is N,N′

-dimethylformamide, N,N′

-dimethylsulfoxide, N-methylpyrrolidone, N,N′

-dimethylacetamide, acetonitrile, trialkylphosphates, nitromethane, methyl alcohol, ethyl alcohol, furfural, alone or admixed in any amounts.

40. A process according to claims 1, 2, 3 or 4, wherein for the oxidation of heteroatom organic compounds, the molar ratios of peroxide/heteroatoms and organic acid/heteroatoms are both equal or larger than 2.0.

41. A process according to claims 1, 2, 3 or 4, wherein the extraction step j) comprises adsorption of the oxidized compounds on an adsorbent.

42. A process according to claim 41, wherein the adsorbent is alumina.

43. A process according to claim 41, wherein the adsorbent is silica-gel.

2. A process for the removal of sulfur, nitrogen and unsaturated compounds from fossil hydrocarbon streams contaminated with said compounds through catalytic oxidation, wherein said process comprises the following steps:

a) Providing a pulverized raw iron oxide;

b) Providing at least one acid;

c) Providing at least one peroxide;

d) Oxidizing unsaturated compounds as well as sulfur and nitrogen contaminants by admixing, under atmospheric pressure and equal or higher than ambient temperature, under agitation, said organic acid and said hydrocarbon stream contaminated with sulfur, nitrogen and unsaturated compounds and then said peroxide, so as to obtain a peracid, the molar amount of peroxide and organic acid relative to the sum of the nitrogen and sulfur contents present in the hydrocarbon stream being at least 3.0, at pH between 2.0 and 6.0, for the required period to obtain a hydrocarbon stream where the unsaturated, sulfur and nitrogen contaminants have been partially oxidized;

e) Further oxidizing said unsaturated compounds as well as sulfur and nitrogen contaminants in the presence of oxidant hydroxyl radicals generated by adding to said partially oxidized hydrocarbon stream, under atmospheric pressure and equal or higher than ambient temperature, the higher than ambient temperature being generated by the process itself, under agitation, a catalytic amount of said pulverized raw iron oxide so as to obtain a slurry of iron oxide, hydrocarbon stream and oxidized unsaturated, sulfur and nitrogen compounds, the reaction conditions being kept during 1-2 hours and an acidic pH between 2.0 and 6.0;

f) After the end of the reaction, filtrating the reaction medium containing an aqueous phase and an oily hydrocarbon phase, and separating the spent iron oxide catalyst;

g) Decanting in order to separate the organic-rich aqueous phase;

h) Correcting the pH of the resulting hydrocarbon phase to values between 6.1 and 9.0 and recovering the oil phase;

i) Post-treating the oil phase to extract/remove the oxidized products at the desired level; and

j) Recovering the post-treated hydrocarbon phase having sulfur compounds in the range of 0.01 weight % and 0.2 weight % and nitrogen compounds in the range of 0.001 weight % to 0.15 weight %, the final olefin content being up to 50% of the original olefin content.

3. A process for obtaining a hydrocarbon stream suitable for refining processes through the catalytic oxidation of same hydrocarbon stream contaminated with sulfur, nitrogen and unsaturated compounds, wherein said process comprises the following steps:

a) Providing a pulverized raw iron oxide;

b) Providing at least one acid;

c) Providing at least one peroxide;

d) Oxidizing unsaturated compounds as well as sulfur and nitrogen contaminants by admixing, under atmospheric pressure and equal or higher than ambient temperature, under agitation, said organic acid and said hydrocarbon stream contaminated with sulfur, nitrogen and unsaturated compounds and then said peroxide, so as to obtain a peracid, the molar amount of peroxide and organic acid relative to the sum of the nitrogen and sulfur contents present in the hydrocarbon stream being at least 3.0, at pH between 2.0 and 6.0, for the required period to obtain a hydrocarbon stream where the unsaturated, sulfur and nitrogen contaminants have been partially oxidized;

e) Further oxidizing said unsaturated compounds as well as sulfur and nitrogen contaminants in the presence of oxidant hydroxyl radicals generated by adding to said partially oxidized hydrocarbon stream, under atmospheric pressure and equal or higher than ambient temperature, the higher than ambient temperature being generated by the process itself, under agitation, a catalytic amount of said pulverized raw iron oxide so as to obtain a slurry of iron oxide, hydrocarbon stream and oxidized unsaturated, sulfur and nitrogen compounds, the reaction conditions being kept during 1-2 hours and an acidic pH between 2.0 and 6.0;

f) After the end of the reaction, filtrating the reaction medium containing an aqueous phase and an oily hydrocarbon phase, and separating the spent iron oxide catalyst;

g) Decanting in order to separate the organic-rich aqueous phase;

h) Correcting the pH of the resulting hydrocarbon phase to values between 6.1 and 9.0 and recovering the oil phase;

i) Post-treating the oil phase to extract the oxidized products at the desired level; and

j) Recovering the post-treated hydrocarbon phase suitable for further refining having nitrogen compounds less than 0.1 weight % and mass balance yields of the order of 80-90 weight %.

4. A process for obtaining a deeply desulfurized and deeply denitrified product through the catalytic oxidation of a hydrocarbon stream containing sulfur, nitrogen and unsaturated contaminants, wherein said process comprises the following steps:

a) Providing a pulverized raw iron oxide;

b) Providing at least one acid;

c) Providing at least one peroxide;

d) Oxidizing unsaturated compounds as well as sulfur and nitrogen contaminants by admixing, under atmospheric pressure and equal or higher than ambient temperature, under agitation, said organic acid and said hydrocarbon stream contaminated with sulfur, nitrogen and unsaturated compounds and then said peroxide, so as to obtain a peracid, the molar amount of peroxide and organic acid relative to the sum of the nitrogen and sulfur contents present in the hydrocarbon stream being at least 3.0, at pH between 2.0 and 6.0, for the required period to obtain a hydrocarbon stream where the unsaturated, sulfur and nitrogen contaminants have been partially oxidized;

e) Further oxidizing said unsaturated compounds as well as sulfur and nitrogen contaminants in the presence of oxidant hydroxyl radicals generated by adding to said partially oxidized hydrocarbon stream, under atmospheric pressure and equal or higher than ambient temperature, the higher than ambient temperature being generated by the process itself, under agitation, a catalytic amount of said pulverized raw iron oxide so as to obtain a slurry of iron oxide, hydrocarbon stream and oxidized unsaturated, sulfur and nitrogen compounds, the reaction conditions being kept during 1-2 hours and an acidic pH between 2.0 and 6.0;

f) After the end of the reaction, filtrating the reaction medium containing an aqueous phase and an oily hydrocarbon phase, and separating the spent iron oxide catalyst;

g) Decanting in order to separate the organic-rich aqueous phase;

h) Correcting the pH of the resulting hydrocarbon phase to values between 6.1 and 9.0 and recovering the oil phase;

i) Post-treating the oil phase to extract the oxidized products at the desired level; and

j) Recovering the post-treated, deeply desulfurized and deeply denitrified product having sulfur compounds less than 0.015 weight % (150 ppm) and nitrogen compounds less than 0.001 weight % (10 ppm), the final olefin content being up to 50% of the original olefin content and mass balance yields of the order of 50 weight %.