Supercritical fluids as diluents in combustion of liquid fuels and waste materials

• US 5,170,727 A
• Filed: 03/29/1991
• Issued: 12/15/1992
• Est. Priority Date: 03/29/1991
• Status: Expired due to Term

• Current Assignee: Union Carbide Chemicals & Plastics Technology Corporation (Dow, Inc.)
• Original Assignee: Union Carbide Chemicals & Plastics Technology Corporation (Dow, Inc.)
• Inventors: Nielsen, Kenneth A.
• Primary Examiner(s): Favors, Edward G.
• Application Number:
  US07/677,104
• Time in Patent Office: 627 Days
• Field of Search: 431/2, 110/347, 110/238, 110/346, 239/5
• US Class Current: 110/346
• CPC Class Codes: B05B 7/32 the fed liquid or other fluent material being under pressure
• CPC Class Codes: B05D 1/025 using gas close to its critical state
• CPC Class Codes: B05D 2401/90 at least one component of the composition being in supercritical state or close to supercritical state
• CPC Class Codes: C10L 1/00 Liquid carbonaceous fuels

Abstract

The present invention is directed to processes and apparatus in which supercritical fluids are used as viscosity reduction diluents for liquid fuels or waste materials which are then spray atomized into a combustion chamber. The addition of supercritical fluid to the liquid fuel and/or waste material allows viscous petroleum fractions and other liquids such as viscous waste materials that are too viscous to be atomized (or to be atomized well) to now be atomized by this invention by achieving viscosity reduction and allowing the fuel to produce a combustible spray and improved combustion efficiency. Moreover, the present invention also allows liquid fuels that have suitable viscosities to be better utilized as a fuel by achieving further viscosity reduction that improves atomization still further by reducing droplet size which enhances evaporation of the fuel from the droplets.

Claims

1. A process for forming a combustible liquid spray mixture which comprises:

a) forming a liquid mixture in a closed system, said liquid mixture comprising;

(i) at least one liquid fuel capable of being combusted; and

(ii) at least one supercritical fluid selected from the group consisting of carbon dioxide, nitrous oxide, sulfur dioxide, ammonia, methyl amines, xenon, krypton, methane, ethane, ethylene, propane, propylene, butane, butene, pentane, diemthyl ether, methyl ethyl ether, diethyl ether, formaldehyde, chlorotrifluoromethane, monofluoromethane, methyl chloride, cyclopentane, and mixtures thereof, which is at least partially miscible with the liquid fuel; and

b) spraying said liquid mixture into an atmosphere capable of sustaining combustion of said liquid fuel.

2. The process of claim 1, wherein the at least one supercritical fluid is added in an amount sufficient to render the viscosity of the liquid mixture to a point suitable for spray combustion.

3. The process of claim 2, wherein the amount of supercritical fluid in the liquid mixture ranges from about 10 to about 60 weight percent based upon the total weight of the liquid mixture.

4. The process of claim 1, wherein the liquid fuel is a petroleum product.

5. The process of claim 1, wherein the liquid fuel contains solid particulate combustible matter.

6. The process of claim 5, wherein the solid particulate combustible matter is coal.

7. The process of claim 1, wherein the liquid fuel is a liquid organic waste material.

8. The process of claim 1, wherein the at least one supercritical fluid is supercritical carbon dioxide.

9. The process of claim 8, wherein at least a portion of the supercritical carbon dioxide is carbon dioxide recovered from the combustion of said liquid fuel.

10. The process of claim 1, wherein the liquid mixture is sprayed into an atmosphere comprising air at or near atmospheric pressure.

11. The process of claim 1 further comprising heating the liquid mixture prior to spraying.

12. The process of claim 1, wherein the liquid mixture is sprayed as a decompressive spray.

13. The process of claim 12, wherein the liquid fuel contains solid particulate combustible matter.

14. The process of claim 13, wherein the solid particulate combustible matter is coal.

15. The process of claim 12, wherein the liquid fuel is a liquid organic waste material.

16. The process of claim 12, wherein the at least one supercritical fluid is supercritical carbon dioxide.

17. The process of claim 12, wherein at least a portion of the supercritical carbon dioxide is carbon dioxide recovered from combustion of said liquid fuel.

18. The process of claim 12 further comprising heating the liquid mixture prior to spraying.

19. An apparatus for the spray combustion of liquid fuels containing at least one supercritical fluid comprising, in combination:

a) means for supplying at least one liquid fuel capable of being combusted;

b) means for supplying at least one supercritical fluid;

c) means for forming a liquid mixture of the components supplied by means (a) and (b);

d) means for spraying said liquid mixture by passing the mixture under pressure through an orifice into an atmosphere capable of sustaining combustion; and

e) means to heat the liquid mixture prior to being passed to the spraying means.