Enhanced photocatalytic conversion of methane to methanol using a porous semiconductor membrane

• US 6,156,211 A
• Filed: 07/14/1998
• Issued: 12/05/2000
• Est. Priority Date: 01/31/1997
• Status: Expired due to Fees

• Current Assignee: Lynntech Power Systems Limited
• Original Assignee: Lynntech Incorporated
• Inventors: Murphy, Oliver J., Gonzalez-Martin, Anuncia
• Primary Examiner(s): Simmons, David A.
• Assistant Examiner(s): PRINCE JR, FREDDIE GARY
• Application Number:
  US09/115,040
• Time in Patent Office: 875 Days
• Field of Search: 210/748, 210/749, 210/758-760, 210/763, 210/198.1, 210/205, 210/209, 502/5, 502/103, 422/24, 422/186, 422/186.3, 204/157.15, 204/157.3, 204/157.6, 204/157.9
• US Class Current: 204/157.9
• CPC Class Codes: B01D 2251/104 Ozone
• CPC Class Codes: B01D 2251/106 Peroxides
• CPC Class Codes: B01D 2255/20707 Titanium
• CPC Class Codes: B01D 53/864 Removing carbon monoxide or hydrocarbons
• CPC Class Codes: B01D 53/8668 Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
• CPC Class Codes: B01J 19/123 Ultraviolet light
• CPC Class Codes: B01J 19/127 Sunlight; Visible light
• CPC Class Codes: B01J 19/2415 Tubular reactors
• CPC Class Codes: B01J 19/2475 Membrane reactors
• CPC Class Codes: B01J 2219/00067 Liquid level measurement
• CPC Class Codes: B01J 2219/00144 Sunlight; Visible light
• CPC Class Codes: B01J 2219/00162 controlling the pressure
• CPC Class Codes: B01J 2219/00164 controlling the flow
• CPC Class Codes: B01J 2219/0883 Gas-gas
• CPC Class Codes: B01J 35/30 characterised by their physical properties
• CPC Class Codes: B01J 35/39 Photocatalytic properties
• CPC Class Codes: B01J 8/009 Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
• CPC Class Codes: C01B 3/38 using catalysts
• CPC Class Codes: C02F 1/325 Irradiation devices or lamp constructions
• CPC Class Codes: C02F 1/4672 by electrooxydation
• CPC Class Codes: C02F 1/722 : Oxidation by peroxides
• CPC Class Codes: C02F 1/725 : by catalytic oxidation
• CPC Class Codes: C02F 1/78 : with ozone C02F1/4672 takes precedence
• CPC Class Codes: C02F 2101/303 : Complexing agents
• CPC Class Codes: C02F 2101/322 : Volatile compounds, e.g. benzene
• CPC Class Codes: C02F 2101/363 : PCB's; PCP's
• CPC Class Codes: C02F 2201/009 : Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells for electrolysis apparatus C02F2201/46165
• CPC Class Codes: C02F 2201/3223 : Single elongated lamp located on the central axis of a turbular reactor
• CPC Class Codes: C02F 2201/328 : Having flow diverters (baffles)
• CPC Class Codes: C02F 2305/10 : Photocatalysts
• CPC Class Codes: Y02A 20/212 : Solar-powered wastewater sewage treatment, e.g. spray evaporation
• CPC Class Codes: Y02P 20/52 : using catalysts, e.g. selective catalysts
• CPC Class Codes: Y02W 10/37 : using solar energy

Abstract

A method and apparatus for the conversion of methane in solution or gas provides photochemical conversion in a unique two-phase or three-phase boundary system formed in each pore of a semiconductor membrane in a photocatalytic reactor. In a three-phase system, gaseous oxidant, methane contained in a liquid, and solid semiconductor photocatalyst having a metal catalyst disposed thereon meet and engage in an efficient conversion reaction. The porous membrane has pores which have a region wherein the meniscus of the liquid varies from the molecular diameter of water to that of a capillary tube resulting in a diffusion layer that is several orders of magnitude smaller than the closest known reactors.

Claims

1. A process comprising the steps of:

providing methane over a photocatalyst disposed on a first surface of a porous substrate having pores extending therethrough to a second surface;

providing a reactant to the second surface and through the pores of the substrate into contact with the photocatalyst on the first surface; and

directing light onto the photocatalyst, wherein the light is selected from visible light, ultraviolet light and mixtures thereof.

2. The process of claim 1, wherein the photocatalyst is selected from titanium dioxide, tungsten oxide, bismuth trioxide, ruthenium oxide, iron oxide, cadmium sulfide and mixtures thereof.

3. The process of claim 1, wherein the photocatalyst comprises a titanium dioxide based binary oxide.

4. The process of claim 3, wherein the titanium dioxide based binary oxide is selected from TiO₂ /SiO₂, TiO₂ /ZrO₂, TiO₂ /SnO₂, TiO₂ /WO₃, TiO₂ /MoO₃, and mixtures thereof.

5. The process of claim 1, wherein the reactant contains an oxidant selected from oxygen, ozone, hydrogen peroxide and combinations thereof.

6. The process of claim 1, wherein the reactant comprises protons in solution.

7. The process of claim 1, wherein the reactant comprises electron transfer molecules.

8. The process of claim 1, further comprising the steps of:

flowing the methane through a fluid cell adjacent the photocatalyst, the fluid cell comprising a light transmission surface positioned to expose the photocatalyst, a fluid inlet, and a fluid outlet; and

flowing the reactant through a reactant cell adjacent the photocatalyst, the reactant cell comprising a reactant inlet.

9. The process of claim 1, wherein the methane is in the gaseous state.

10. The process of claim 9, wherein the reactant is in the gaseous state.

11. The process of claim 8, further comprising the step of:

removing methanol from the fluid cell.

12. The process of claim 11, wherein the oxidant comprises between about 10% and about 18% by weight of electrochemically generated ozone.

13. The process of claim 12, wherein the ultraviolet source is solar light and the ultraviolet transmission surface of the fluid cell is a ultraviolet transmission surface of a solar photoreactor.

14. The process of claim 12, wherein the ultraviolet source is an ultraviolet lamp and the ultraviolet transmission surface of the fluid cell is a ultraviolet transmission surface of the ultraviolet lamp.

15. The process of claim 12, wherein the ultraviolet source is an ultraviolet lamp which includes the ultraviolet wavelength range of 300-400 nm.

16. The process of claim 1, further comprising, the step of:

providing a two-phase or three-phase interface between the photocatalyst, the methane and the reactant; and

converting the methane at the interface.

17. The process of claim 16, further comprising the step of:

producing methanol.

18. The process of claim 16, further comprising the step of:

producing hydrogen.

40. The process of claim 1, wherein the photocatalyst is doped with a metal selected from titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, ruthenium, lanthanum, lithium, silver, platinum, and mixtures thereof.

41. The process of claim 1, wherein the photocatalyst is a semiconductor and the light has an energy equal to or higher than the band gap energy to generate electrons and holes in the semiconductor.

19. A process, comprising the steps of:

providing methane over a photocatalyst having pores therethrough, wherein the photocatalyst has a metal catalyst disposed thereon;

providing a reactant through the pores into contact with the photocatalyst; and

directing light onto the photocatalyst, wherein the light is selected from visible light, ultraviolet light and mixtures thereof.

20. The process of claim 19, wherein photocatalyst is selected from titanium dioxide, tungsten oxide, bismuth trioxide, ruthenium oxide, iron oxide, cadmium sulfide and mixtures thereof.

21. The process of claim 19, wherein the photocatalyst comprises a titanium dioxide based binary oxide.

22. The process of claim 21, wherein the titanium dioxide based binary oxide is selected from TiO₂ /SiO₂, TiO₂ /ZrO₂, TiO₂ /SnO₂, TiO₂ /WO₃, TiO₂ /MoO₃, and mixtures thereof.

23. The process of claim 19, wherein the reactant comprises an oxidant selected from oxygen, ozone, hydrogen peroxide and combinations thereof.

24. The process of claim 19, wherein the reactant comprises protons in solution.

25. The process of claim 19, wherein the reactant comprises electron transfer molecules.

26. The process of claim 19, further comprising the steps of:

flowing the methane through a fluid cell adjacent the photocatalyst, the fluid cell comprising a light transmission surface positioned to expose the photocatalyst, a fluid inlet, and a fluid outlet; and

flowing the reactant through a reactant cell adjacent the photocatalyst, the reactant cell comprising a reactant inlet.

27. The process of claim 19, wherein the metal catalyst is selected from Pt group metals, Au group metals, Ir, Ru, Sn, Os, Mo, Zr, Ni, Nb, Rh;

and mixtures thereof.

28. The process of claim 19, wherein the metal catalyst is selected from, Pt--Sn, Pt--Mo, Pt--Ru, Ni--Zr, Pt--Rh, Pt--Ir, Pt--Ru--W, Pt--Ru--Os, Pt--Ru--Sn, Pt--Ni--Ti, Pt--Ni--Zr, Pt--Ni--Nb, Pt--Ni--Ta and mixtures thereof.

29. The process of claim 19, wherein the metal catalyst is selected from Pt group metal oxides, Au group metal oxides, SnO₂, WO₃, WO₃, IrO₂, Rh₂ O₃, RuO₂ and mixtures thereof.

30. The process of claim 19, wherein the metal catalyst is selected from Pt group metals, Au group metals, Ir, Ru, Sn, Os, Mo, Zr, Ni, Nb, Rh, Pt--Sn, Pt--Mo, Pt--Ru, Ni--Zr, Pt--Rh, Pt--Ir, Pt--Ru--W, Pt--Ru--Os, Pt--Ru--Sn, Pt--Ni--Ti, Pt--Ni--Zr, Pt--Ni--Nb, Pt--Ni--Ta, Pt group metal oxides, Au group metal oxides, SnO₂, WO₃, WO₃, IrO₂, Rh₂ O₃, RuO₂ and mixtures thereof.

31. The process of claim 19, wherein the photocatalyst comprises between about 0.01 wt % and about 5 wt % metal catalyst.

32. The process of claim 26, further comprising the step of:

removing methanol from the fluid cell.

33. The process of claim 32, wherein the oxidant comprises between about 10% and about 18% by weight of electrochemically generated ozone.

34. The process of claim 33, wherein the ultraviolet source is solar light and the ultraviolet transmission surface of the fluid cell is a ultraviolet transmission surface of a solar photoreactor.

35. The process of claim 33, wherein the ultraviolet source is an ultraviolet lamp and the ultraviolet transmission surface of the fluid cell is a ultraviolet transmission surface of the ultraviolet lamp.

36. The process of claim 33, wherein the ultraviolet source is an ultraviolet lamp which includes the ultraviolet wavelength range of 300-400 nm.

37. The process of claim 19, further comprising, the step of:

providing a two-phase or three-phase interface between the solid photocatalyst, the methane and the reactant; and

converting methane at the interface.

38. The process of claim 19, wherein the methane is in the gaseous state.

39. The process of claim 38, wherein the reactant is in the gaseous state.

42. A process comprising the steps of:

providing a reactant over a photocatalyst disposed on a first surface of a porous substrate having pores extending therethrough to a second surface;

providing methane to the second surface and through the pores of the substrate into contact with the photocatalyst on the first surface; and

directing light onto the photocatalyst, wherein the light is selected from visible light, ultraviolet light and mixtures thereof.

43. The process of claim 42, further comprising the step of:

photocatalytically oxidizing the methane to methanol at the photocatalyst surface.