초록 ▼

Production of oxygen-enriched gas streams is disclosed herein. Air streams contact an oxygen-selective mixed conductor particularly a perovskite material whereby oxygen is retained or adsorbed on the perovskite and can be employed in a variety of processes such as in combusting a fuel gas, heat rec

Production of oxygen-enriched gas streams is disclosed herein. Air streams contact an oxygen-selective mixed conductor particularly a perovskite material whereby oxygen is retained or adsorbed on the perovskite and can be employed in a variety of processes such as in combusting a fuel gas, heat recovery and boiler related operations.

대표청구항 ▼

Having thus described the invention, what we claim is: 1. A method of operating an oxygen consuming process comprising sequentially the steps: a) feeding air through a reactor containing an oxygen selective mixed conductor, whereby oxygen is retained on said oxygen selective mixed conductor and sai

Having thus described the invention, what we claim is: 1. A method of operating an oxygen consuming process comprising sequentially the steps: a) feeding air through a reactor containing an oxygen selective mixed conductor, whereby oxygen is retained on said oxygen selective mixed conductor and said reactor is at a temperature greater than 300째 C.; b) feeding at least part of an oxygen-depleted product gas from said oxygen consuming process into said reactor, thereby forming an oxygen-containing gas stream substantially free of nitrogen; and c) feeding said oxygen-containing gas stream substantially free of nitrogen into said oxygen consuming process further producing a product gas stream comprising carbon dioxide and at least part of said carbon dioxide is recovered. 2. A method for forming a product gas stream for use in an oxygen consuming process comprising the steps: (a) feeding air through a first heat exchanger and into a reactor containing an oxygen selective mixed conductor, whereby oxygen is retained on said oxygen selective mixed conductor and said reactor is at a temperature greater than 300째 C.; and (b) feeding an oxygen-depleted gas stream through a second heat exchanger and through said reactor, whereby oxygen is released from said oxygen selective mixed conductor forming said product gas stream. 3. The method as claimed in claim 2 wherein said method is cyclical. 4. The method as claimed in claim 3 wherein said cyclical method is thermally self-sustaining. 5. The method as claimed in claim 2 wherein a fuel gas is added to said oxygen-depleted gas stream. 6. The method as claimed in claim 5 wherein said fuel gas is selected from the group consisting of carbon monoxide, hydrogen, methane and mixtures thereof. 7. The method as claimed in claim 2 wherein said heat exchangers are multi-pass heat exchangers. 8. The method as claimed in claim 2 wherein nitrogen-rich gas is produced as a by-product during the oxygen retention step (a). 9. The method as claimed in claim 2 wherein said air and said oxygen-depleted gas stream are fed to said reactor in a counter-current manner. 10. The method as claimed in claim 2 wherein said second heat exchanger increases the temperature of said oxygen-depleted gas stream to about 900째 C. 11. The method as claimed in claim 2 wherein said oxygen-depleted gas stream contains up to about 5% oxygen. 12. The method as claimed in claim 2 wherein said oxygen-selective mixed conductor is a perovskite type ceramic having the structural formula A1-xMxBO3-δ. 13. The method as claimed in claim 12 wherein A is a rare earth ion, M is Sr, Ca, Ba, V or mixtures of these; B is Co, Mn, Cr, Fe or mixtures of these; x varies from greater than 0 to about 1; and δ is the deviation from stoichiometric composition resulting from the substitution of Sr, Ca and Ba for rare earth ions. 14. The method as claimed in claim 13 wherein x varies from about 0.1 to about 1. 15. The method as claimed in claim 13 wherein A is La, Y or mixtures of these; M is Sr, Ca or mixtures of these; and B is Co, Fe or mixtures of these. 16. The method as claimed in claim 15 wherein x is about 0.2 to 1. 17. The method as claimed in claim 3 wherein said first heat exchanger and said second heat exchanger are selected from the group consisting of internal heat exchangers, external heat exchangers and combinations of internal and external heat exchangers.