WO1998054098B1 - Oxidation of aromatic hydrocarbons - Google Patents

Oxidation of aromatic hydrocarbons

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Publication number
WO1998054098B1
WO1998054098B1 PCT/US1998/011463 US9811463W WO9854098B1 WO 1998054098 B1 WO1998054098 B1 WO 1998054098B1 US 9811463 W US9811463 W US 9811463W WO 9854098 B1 WO9854098 B1 WO 9854098B1
Authority
WO
WIPO (PCT)
Prior art keywords
parts
weight
approximately
contaminated material
amount
Prior art date
Application number
PCT/US1998/011463
Other languages
French (fr)
Other versions
WO1998054098A1 (en
Filing date
Publication date
Priority claimed from US08/867,345 external-priority patent/US5849201A/en
Application filed filed Critical
Priority to AU78141/98A priority Critical patent/AU7814198A/en
Priority to EP98926264A priority patent/EP1007480A4/en
Publication of WO1998054098A1 publication Critical patent/WO1998054098A1/en
Publication of WO1998054098B1 publication Critical patent/WO1998054098B1/en

Links

Abstract

The present invention describes a method for efficient, economical and rapid remediation of aromatic hydrocarbons, and especially polycyclic aromatic hydrocarbons (PAHs), in contaminated materials, such as soils, sludges, tars, sands and liquids using catalysts in conjunction with ozone, oxidants and surfactants. The method uses multistage catalytic oxidation to convert aromatic hydrocarbons into innocuous, biodegradable, or easily decomposed compounds such as carbon dioxide and carbonyl compounds, including but not limited to aldehydes, ketones, quinones, and carboxylic acids. The method may be employed to treat dry and wet contaminated samples of large tonnage and offers an excellent alternative to incineration.

Claims

AMENDED CLAIMS
[received by the International Bureau on 30 November 1998 (30.11.98); original claims 1, 17, 18, 28, 37, 38 and 42 amended; original claims 29-36 cancelled; new claims 43-50 added; remaining claims unchanged (6 pages)]
1. A method for remediating material contaminated with aromatic hydrocarbons, comprising: combining material contaminated with aromatic hydrocarbons, a catalyst, and a first oxidaπt other than ozone, to form a mixture: mixing the mixture; and adding ozone gas to the mixture to oxidize and degrade said aromatic hydrocarbons.
2. The method of Qaim 1, wherein the mixture containing the ozone gas is mixed so as to create submicron sized ozone bubbles.
3. The method of Qaim 1 , further comprising the addition of catalyst during addition of the ozone gas to the mixture.
4. The method of Qaim 1, further comprising adjusting the mixture during mixing through addition of base to achieve an alkaline pH.
5. The method of Qaim 1 , wherein the contaminated material is processed in a continuous manner.
6. The method of Claim 1, wherein the first oxidant is selected from the group of hydrogen peroxide, perchlorate, permanganate, and persulfate.
7. The method of Qaim 1, wherein the first oxidaπt is hydrogen peroxide.
8. The method of Claim 7, wherein the hydrogen peroxide is provided as a 50% solution in an amount of approximately 10 to 50 parts by weight per 1000 parts by weight of contaminated material. 9. The method of Qaim 7, wherein the hydrogen peroxide is provided as a 50% solution in an amount of approximately 25 parts by weight per 1000 parts by weight of contaminated material.
10. The method of Claim 1, further comprising addition of surfactant to the mixture.
11. The method of Qaim 10, wherein the surfactant is selected from the group consisring of bi-terpene, soaps, solvents, supercritical fluids, detergents, degreasers and releasing agents.
12. The method of Claim 10, wherein the surfactant is bi-terpene and is provided in an amount of approximately 10 to 100 parts by weight per 1000 parts by weight of contaminated material.
13. The method of Claim 12, wherein the bi-terpene surfactant is provided in an amount of approximately 25 parts by weight per 1000 parts by weight of contaminated material.
14. The method of Claim 1, wherein the catalyst is selected from the group consisting of iron, gold, titanium, copper, silver, manganese, cobalt, nickel, stainless steel, steel wool, titania, nano-titania, and oxides, alloys, and composites and combinations thereof.
15. The method of Claim 1, wherein the catalyst is metallic iron which is provided in an amount of approximately 2 to 100 parts by weight per 1000 parts by weight of contaminated material.
16. The method of Claim 1, wherein the catalyst is metallic iron which is provided in an amount of approximately 5 to 50 parts by weight per 1000 parts by weight of contaminated material.
17. The method of Qaim 1, wherein the catalyst is titania or nano-titania which is provided in an amount of approximately 2 to 100 parts by weight per 1000 parts by weight of contaminated material. 38
18. The method of Qaim 1, wherein the catalyst is titania or nano-titania which is provided in an amount of approximately 2 to 50 parts by weight per 1000 parts by weight of contaminated material.
19. The method of Claim 1 , further comprising addition of water to the mixture,
20. The method of Claim 19, wherein the water is provided in an amount of approximately 0 to 500 parts by weight per 1000 parts by weight of contaminated material.
21. The method of Qaim 1 , wherein the water is provided in an amount of approximately 250 parts by weight per 1000 parts by weight of contaminated material.
22. The method of Claim 1, wherein the contaminated material is paniculate and the particle size is not greater than approximately 1.27 cm, further comprising addition of water and a surfactant.
23. The method of Qaim 1, wherein the contaminated material is paniculate and the particle size is not greater than approximately 0.318 cm, further comprising addition of water and a surfactant.
24. The method of Claim 1, wherein the ozone gas is provided in an amount of approximately 0.001 to 3.0 parts by weight per 1 part by weight of aromatic hydrocarbons in the contaminated material.
25. The method of Claim 1, wherein the ozone gas is provided in an amount of approximately 0.05 to 2.0 parts by weight per 1 part by weight of aromatic hydrocarbons in the contaminated material.
26. The method of Claim 1, wherein the ozone gas is provided in an amount of approximately 0.1 to 1.5 parts by weight per 1 part by weight of aromatic hydrocarbons in the contaminated material. 39
27. The method of Claim 1, wherein the contaminated material is selected from liquids, aqueous solutions, aqueous suspensions, organic solutions, organic suspensions, chemicals, solvents, paints, water, salt water, ice, snow, soil, sludge, silt, permafrost, sand, tar, tar sand, asphalt, clay, concrete, wood, ceramics, plastic, clothing, fabric, mesoporous media, vermiculite, and mixtures thereof.
28, A method for remediating material contaminated with aromatic hydrocarbons, comprising: combining contaminated material of less than 1.27 cm in particle size with water in an amount of approximately 0 to 500 parts by weight per 1000 parts by weight of contaminated material, catalysts, wherein one catalyst is metallic iron which is provided in an amount of approximately 2 to 100 parts by weight per 1000 parts by weight of contaminated material, and a second catalyst, wherein the second catalyst is titania or nano-titania which is provided in an amount of approximately 2 to 100 parts by weight per 1000 parts by weight of contaminated material, surfactant, wherein the surfactant is bi-terpene which is provided in an amount of approximately 10 to J 00 parts by weight per 1000 parts by weight of contaminated material, and a first oxidant other than ozone wherein the first oxidant is hydrogen peroxide which is provided as a 50% solution in an amount of approximately 10 to 50 parts by weight per 1000 parts by weight of contaminated material, to form a mixture; mixing the mixture; and adding ozone gas to the mixture in an amount of approximately 0.001 to 3.0 parts by weight per 1 part by weight of aromatic hydrocarbons in the material.
37. The method of Claim 1 , wherein the catalyst is in the form of divided powders, coatings, pellets, flakes, platelets, granules, spheres, balls, steel wool, ceramic wools, wires, fine filaments, threads, high porosity agglomerates or combinations thereof. 40
38. The method of Claim 1, wherein the catalyst is located on stationary fixtures, rotating fixtures, impellor blades, baffles, metal baffles, ceramic baffles, vanes, paddles, meshes, grids, honeycombs, balls, gratings, manifolds, beds, deflectors, reaction vessel walls or combinations thereof.
39. The method of Claim 1, wherein the contaminated material is paniculate and the particle size is less than approximately 500 microns.
40. The method of Qaim 1, wherein the contaminated material is paniculate and the particle size is less than approximately 200 microns.
41 , The method of Claim 1 , wherein the contaminated material is paniculate and the particle size is less than approximately 100 microns.
42. A method for remediating material contaminated with aromatic hydrocarbons, comprising: combining contaminated material of less than approximately 500 microns in particle size with an amount of water sufficient to make a mixture; mixing the mixture; and adding ozone gas to the mixture in an amount of approximately 1 to 5 parts by weight per 1 part by weight of aromatic hydrocarbons in the material.
43. The method of Qaim 42, wherein the contaminated material of less than approximately 200 microns in panicle size.
44. The method of Qaim 42, wherein the contaminated material of less than approximately 100 microns in particle size. 41
45. A method for remediating material contaminated with aromatic hydrocarbons, comprising: combining material contaminated with aromatic hydrocarbons, a catalyst, and a first oxidant other than ozone, to form a mixture, wherein the mixture includes at least about 10 parts by weight of said first oxidant per 1000 parts by weight of contaminated material; mixing the mixture; and adding ozone gas to the mixture to oxidize and degrade said aromatic hydrocarbons, wherein the catalyst is located on coatings, stationary fixtures, rotating fixtures, impellor blades, baffles, metal baffles, ceramic baffles, vanes, paddles, wires, fine filaments, threads, meshes, grids, honeycombs, balls, gratings, manifolds, beds, deflectors, reaction vessel walls or combinations thereof.
46. The method of Claim 45, wherein the catalyst is titania, nano-titania, metal, composites thereof, or combinations thereof.
47. The method of Claim 46, wherein the metal is selected from the group consisting of iron, gold, titanium, copper, silver, manganese, cobalt, nickel, stainless steel, steel wool, and oxides, alloys, and composites and combinations thereof.
48. The method of Qaim 1, wherein said mixture includes as the catalyst titania, πano-Utania or metal.
49. The method of Qaim 48, wherein the metal is selected from the group consisting of iron, gold, titanium, copper, silver, manganese, cobalt, nickel, stainless steel, steel wool, and oxides, alloys, and composites and combinations thereof.
50. The method of Claim 1, wherein the mixture includes as the catalyst at least about 2 parts by weight of metallic iron and at least about 2 parts by weight of titania or nano-titania, and at least about 10 parts by weight of the first oxidant, per 1000 parts by weight of contaminated material.
PCT/US1998/011463 1997-06-02 1998-06-02 Oxidation of aromatic hydrocarbons WO1998054098A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AU78141/98A AU7814198A (en) 1997-06-02 1998-06-02 Oxidation of aromatic hydrocarbons
EP98926264A EP1007480A4 (en) 1997-06-02 1998-06-02 Oxidation of aromatic hydrocarbons

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/867,345 US5849201A (en) 1997-06-02 1997-06-02 Oxidation of aromatic hydrocarbons
US08/867,345 1997-06-02

Publications (2)

Publication Number Publication Date
WO1998054098A1 WO1998054098A1 (en) 1998-12-03
WO1998054098B1 true WO1998054098B1 (en) 1999-01-14

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US (1) US5849201A (en)
EP (1) EP1007480A4 (en)
AU (1) AU7814198A (en)
WO (1) WO1998054098A1 (en)

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