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A method of separating oxygen from an oxygen containing feed and reacting the oxygen with a reactive substance and an oxygen ion transport membrane element utilized for such purposes. The oxygen ion transport membrane element has a self-supporting dense layer and a surface porous feature in contact

A method of separating oxygen from an oxygen containing feed and reacting the oxygen with a reactive substance and an oxygen ion transport membrane element utilized for such purposes. The oxygen ion transport membrane element has a self-supporting dense layer and a surface porous feature in contact with and supported by the dense layer. The porous surface feature may be a layer, a layer having discontinuities or a series of repeating geometrical forms. The dense layer and the porous surface feature are capable of conducting oxygen ions and electrons. The porous surface feature at least in part forms the anode side of the oxygen ion transport membrane element at which the reactive substance reacts with the separated oxygen and has a thickness less than that of the dense layer and a greater surface area than that of a surface of the dense layer adjoining the porous layer. Pores within the porous surface feature have a pore aspect ratio of pore size to pore length of between about 0.1 and about 5.

대표청구항 ▼

We claim: 1. A method of separating oxygen from an oxygen containing feed and reacting the oxygen with a reactive substance, said method comprising: contacting the oxygen containing feed with a cathode side of an oxygen ion transport membrane element and permeating the oxygen through the oxygen ion

We claim: 1. A method of separating oxygen from an oxygen containing feed and reacting the oxygen with a reactive substance, said method comprising: contacting the oxygen containing feed with a cathode side of an oxygen ion transport membrane element and permeating the oxygen through the oxygen ion transport membrane element by oxygen ion transport from the cathode side to an anode side thereof; the oxygen ion transport membrane element having a self-supporting dense layer and a surface porous feature in contact with and supported by the dense layer, each of the dense layer and the porous surface feature being capable of conducting oxygen ions and electrons, the porous surface feature at least in part forming the anode side of the oxygen ion transport membrane element and having a thickness less than that of the dense layer, a greater surface area than that of a surface of the dense layer adjoining the porous surface feature and a pore aspect ratio of pore size to pore length of pores defined in the surface porous feature of between about 0.1 and about 5; contacting the reactive substance with the anode side of the oxygen ion transport membrane element at the porous surface feature thereof and reacting the reactive substance with the oxygen permeated through the oxygen ion transport membrane element; and the reaction providing a driving force for the oxygen ion transport. 2. The method of claim 1, wherein the porous surface feature is discontinuous and covers no less than about 50 percent of the dense layer. 3. The method of claim 2, wherein the porous surface feature are repeating porous geometric formations. 4. The method of claim 3, wherein the repeating porous geometric formations are of cylindrical configuration. 5. The method of claim 1, wherein: said dense layer has a dense layer thickness of between about 500 microns and about 1000 microns; and said porous surface feature has a surface feature thickness of between about 20 microns and about 500 microns, pores having a pore size of pores of between about 1 micron and about 100 microns, and a porosity of between about 30 percent and about 70 percent. 6. The method of claim 5, wherein: said dense layer thickness is between about 700 microns and about 800 microns; and said surface feature thickness is between about 100 microns and about 500 microns. 7. The method of claim 6, wherein: the pore size is between about 10 micron and about 50 microns; the porosity is between about 35 percent and about 45 percent; and the pore aspect ratio is between about 0.1 and about 2. 8. The method of claim 7, wherein: said pore size is between about 20 microns and about 40 microns; and the pore aspect ratio is between about 0.1 and about 2. 9. The method of claim 1, wherein the dense layer and the porous surface feature are formed from a mixed conductor or a dual phase conductor. 10. The method of claim 1 or claim 2, wherein the oxygen ion transport membrane element further has a porous surface enhancement layer at the cathode side to enhance formation of oxygen ions. 11. The method of claim 10, wherein the porous surface enhancement layer has an enhancement layer thickness of less than about 300 microns and surface enhancement pores of greater than about 20 microns in pore size and a porosity of between about 35 percent and about 70 percent. 12. The method of claim 11, wherein the porosity is between about 50 percent and about 60 percent. 13. An oxygen ion transport element for separating oxygen from an oxygen containing feed and reacting the oxygen with a reactive substance, said oxygen ion transport element comprising: a self-supporting dense layer and a surface porous feature in contact with and supported by the dense layer and at which the reactive substance reacts with the oxygen; the dense layer and the porous surface feature each being capable of conducting oxygen ions and electrons between opposed cathode and anode sides thereof; and the porous surface feature at least in part forming the anode side of the oxygen ion transport membrane element and having a thickness less than that of the dense layer, a greater surface area than that of a surface of the dense layer adjoining the porous layer and a pore aspect ratio of pore size to pore length of pores defined in the surface porous feature of between about 0.1 and about 5. 14. The oxygen ion transport element of claim 13, wherein the porous surface feature is discontinuous and covers no less than about 50 percent of the dense layer. 15. The oxygen ion transport element of claim 14, wherein the porous surface feature are repeating porous geometric formations. 16. The oxygen ion transport element of claim 15, wherein the repeating porous geometric formations are of cylindrical configuration. 17. The oxygen ion transport element of claim 13, wherein: said dense layer has a dense layer thickness of between about 500 microns and about 1000 microns; and said porous surface feature has a surface feature thickness of between about 20 microns and about 500 microns, pores having a pore size of pores of between about 1 micron and about 100 microns and a porosity of between about 30 percent and about 70 percent. 18. The oxygen ion transport element of claim 17, wherein: said dense layer thickness is between about 700 microns and about 800 microns; and said surface feature thickness is between about 100 microns and about 500 microns. 19. The oxygen ion transport element of claim 18, wherein: the pore size is between about 10 micron and about 50 microns; the porosity is between about 35 percent and about 45 percent; and the pore aspect ratio is between about 0.1 and about 2. 20. The oxygen ion transport element of claim 19, wherein: said pore size is between about 20 microns and about 40 microns; and the pore aspect ratio is between about 0.1 and about 2. 21. The oxygen ion transport element of claim 13, wherein said dense layer or the porous surface feature is a mixed conductor or a dual phase conductor. 22. The oxygen ion transport element of claim 13 or claim 14, wherein the oxygen ion transport membrane element further has a porous surface enhancement layer at the cathode side to enhance the formation of oxygen ions. 23. The oxygen ion transport element of claim 22, wherein the surface enhancement layer having an enhancement layer thickness of less than about 300 microns and surface enhancement pores of greater than about 20 microns in pore size and a porosity of between about 35 percent and about 70 percent. 24. The oxygen ion transport element of claim 23, wherein the porosity is between about 50 percent and about 60 percent.