Claims
- 1. A process for hydrothermal oxidation of combustible material in a hydrothermal oxidation apparatus, in which, during at least part of the oxidation, corrosive material is present and contacts the apparatus over a contact area on the apparatus, the process comprising:
- contacting in an aqueous phase the combustible material and an oxidizing agent under conditions suitable to cause oxidation of the combustible material;
- wherein the oxidation is at a temperature in the range of about 300.degree. C. to about 800.degree. C. and at pressures from about 27.5 bar (400 psi) to about 1000 bar (15,000 psi); and
- wherein the contact area comprises iridium to provide corrosion resistance from said corrosive material in said contact area.
- 2. The process of claim 1, wherein the corrosive material comprises at least one moiety selected from the group consisting of Cl, SO.sub.4 and OH and at least one moiety selected from the group consisting of H, Na, K, Ca, Mg, Ce, Pb and Zn.
- 3. The process of claim 2, wherein the corrosive material comprises (i) at least one selected from the group consisting of HCl, H.sub.2 SO.sub.4, NaOH, Na.sub.2 CO.sub.3 and (ii) a sodium salt.
- 4. The process of claim 1, wherein the aqueous phase containing the corrosive material and oxidizing agent contains greater than 50 mole percent water.
- 5. The process of claim 4, wherein the aqueous phase further contains oxygen, carbon dioxide, and at least one selected from the group consisting of acids, bases and salts.
- 6. The process of claim 1, wherein the oxidation apparatus is a reactor selected from the group consisting of vessel reactors, hydraulic column reactors, and pipe reactors.
- 7. The process of claim 1, wherein the contact area comprises a base metal overlaid with an iridium coating.
- 8. A process for hydrothermal oxidation of combustible material in a hydrothermal oxidation apparatus, in which, during at least part of the oxidation, corrosive material is present and contacts the apparatus over a contact area on the apparatus, the process comprising:
- contacting in an aqueous phase the combustible material and an oxidizing agent under conditions suitable to cause oxidation of the combustible material;
- wherein the oxidation is at a temperature in the range of about 300.degree. C. to about 800.degree. C. and at pressures from about 27.5 bar (400 psi) to about 1000 bar (15,000 psi); and
- wherein the contact area comprises an iridium based protective layer to provide corrosion resistance from said corrosive material in said contact area.
- 9. The process of claim 8, wherein the corrosive material comprises at least one moiety selected from the group consisting of Cl, SO.sub.4 and OH, and at least one moiety selected from the group consisting of H, Na, K, Ca, Mg, Ce, Pb and Zn.
- 10. The process of claim 9, wherein the corrosive material comprises (i) at least one selected from the group consisting of HCl, H.sub.2 SO.sub.4, NaOH, Na.sub.2 CO.sub.3 and (ii) a sodium salt.
- 11. The process of claim 8, wherein the aqueous phase containing the corrosive material and oxidizing agent contains greater than 50 mole percent water.
- 12. The process of claim 11, wherein the aqueous phase further contains oxygen, carbon dioxide, and at least one selected from the group consisting of acids, bases and salts.
- 13. The process of claim 8, wherein the oxidation apparatus is a reactor selected from the group consisting of vessel reactors, hydraulic column reactors, and pipe reactors.
- 14. The process of claim 8, wherein the iridium protective layer is formed in-situ by contacting an iridium surface with an oxidizing agent under conditions suitable to cause oxidation of the iridium surface.
- 15. The process of claim 14, wherein the oxidation of the iridium surface comprises contacting the iridium surface with an aqueous phase which includes the oxidizing agent at a temperature of about 300.degree. C. to about 800.degree. C. and a pressure from about 27.5 bar to about 1000 bar.
- 16. A process for hydrothermal oxidation of combustible material in a hydrothermal oxidation apparatus, in which, during at least part of the oxidation, corrosive material is present and contacts the apparatus over a contact area on the apparatus, the process comprising:
- contacting in an aqueous phase the combustible material and an oxidizing agent under conditions suitable to cause oxidation of the combustible material;
- wherein the oxidation is at a temperature in the range of about 300.degree. C. to about 800.degree. C. and at pressures from about 27.5 bar (400 psi) to about 1000 bar (15,000 psi); and
- wherein the contact area comprises an iridium alloy to provide corrosion resistance from said corrosive material in said contact area.
- 17. The process of claim 16, wherein the corrosive material comprises at least one moiety selected from the group consisting of Cl, SO.sub.4 and OH, and at least one moiety selected from the group consisting of H, Na, K, Ca, Mg, Ce, Pb and Zn.
- 18. The process of claim 17, wherein the corrosive material comprises (i) at least one selected from the group consisting of HCl, H.sub.2 SO.sub.4, NaOH, Na.sub.2 CO.sub.3 and (ii) a sodium salt.
- 19. The process of claim 16, wherein the aqueous phase containing the corrosive material and oxidizing agent contains greater than 50 mole percent water.
- 20. The process of claim 19, wherein the aqueous phase further contains oxygen, carbon dioxide, and at least one selected from the group consisting of acids, bases and salts.
- 21. The process of claim 16, wherein the oxidation apparatus is a reactor selected from the group consisting of vessel reactors, hydraulic column reactors, and pipe reactors.
- 22. The process of claim 16, wherein the contact area comprises a base metal overlaid with an iridium alloy coating.
- 23. The process of claim 16, wherein the iridium alloy comprises an iridium platinum alloy.
- 24. The process of claim 23, wherein the iridium platinum alloy comprises greater than about 50 wt. % iridium.
Government Interests
This invention was made with Government support under Subcontract No. C94-170508 awarded by the Department of Energy. The Government has certain rights in this invention.
US Referenced Citations (10)
Non-Patent Literature Citations (1)
Entry |
Materials of Construction for Chemical Engineering Equipment, Chemical & Metall. Eng., Sep./1944, p. 105. |