초록 ▼

It is an object of the present invention to provide a ceramic member with excellent balance between oxygen ion conductivity and endurance (resistance to cracking and the like), an oxygen ion permeation module and a chemical reactor such as an oxygen separator, using such a ceramic member. The cerami

It is an object of the present invention to provide a ceramic member with excellent balance between oxygen ion conductivity and endurance (resistance to cracking and the like), an oxygen ion permeation module and a chemical reactor such as an oxygen separator, using such a ceramic member. The ceramic member with oxygen ion conductivity in accordance with the present invention has a perovskite-type crystal structure and a composition represented by the general formula: description="In-line Formulae" end="lead"(Ln1-xMx)(Ti1-y Fey)O3 description="In-line Formulae" end="tail" (where Ln represents at least one element selected from lanthanoids, and M represents at least one element selected from the group containing Sr, Ca, and Ba, 0

대표청구항 ▼

The invention claimed is: 1. An oxygen separation method comprising: using at least one ceramic member having a perovskite-type crystal structure represented by any one of the following (A)-(B): (A) the general formula description="In-line Formulae" end="lead"(Ln1-xSrx)(Ti1-y Fey)O3 description="

The invention claimed is: 1. An oxygen separation method comprising: using at least one ceramic member having a perovskite-type crystal structure represented by any one of the following (A)-(B): (A) the general formula description="In-line Formulae" end="lead"(Ln1-xSrx)(Ti1-y Fey)O3 description="In-line Formulae" end="tail" where the Ln represents at least one element selected from lanthanoids; the x satisfies the condition 0.2≦x≦0.6, the y satisfies the condition 0.5≦yLn1-xBax)(Ti1-y Fey)O3 description="In-line Formulae" end="tail" where the Ln represents at least one element selected from lanthanoids, the x satisfies the condition 0.3≦x≦0.7the y satisfies the condition 0.5≦yLn1-xSrx)(Ti1-y Fey)O3 description="In-line Formulae" end="tail" where the Ln represents at least one element selected from lanthanoids; the x satisfies the condition 0.2≦x≦0.6 the y satisfies the condition 0.5≦yLn1-xBax)(Ti1-y Fey)O3 description="In-line Formulae" end="tail" where the Ln represents at least one element selected from lanthanoids, the x satisfies the condition 0.3≦x≦0.7, the y satisfies the condition 0.5≦yxSr1-x)M'O3 (where, 0.1≦x≦1, and M' is at least one selected from Co, Cu, Fe, and Mn) is the catalyst for enhancing the permeation of oxygen ions. 6. An oxygen ion permeation module comprising: a casing; at least one membranous ceramic member with oxygen ion conductivity and a thickness of 0.5mm or less which is accommodated in the casing, the ceramic member having a perovskite-type crystal structure and a composition represented by any one of the following (A)-(B): (A) the general formula description="In-line Formulae" end="lead"(Ln1-xSrx)(Ti1-y Fey)O3 description="In-line Formulae" end="tail" where the Ln represents at least one element selected from lanthanoids; the x satisfies the condition 0.2≦x≦0.6, the y satisfies the condition 0.5≦yLn1-xBax)(Ti1-y Fey)O3 description="In-line Formulae" end="tail" where the Ln represents at least one element selected from lanthanoids, the x satisfies the condition 0.3≦x≦0 7, the y satisfies the condition 0.5y≦y≦1, and x and y satisfy the condition 1≦x+y≦1.2; an oxygen source supply chamber for supplying an oxygen-containing gas from the outside, the oxygen source supply chamber being provided inside the casing so as to face the ceramic member; and an oxidation reaction chamber provided inside the casing so as to face the ceramic member, hermetically separated from the oxygen source supply chamber via the ceramic member and serving to induce an oxidation reaction with the participation of oxygen ions that are supplied by permeation through the ceramic member from the oxygen source supply chamber. 7. The oxygen ion permeation module according to claim 6, wherein a catalyst for enhancing the permeation of oxygen ions is applied to the surface of the membranous ceramic member on the side of the oxygen source supply chamber. 8. The oxygen ion permeation module according to claim 7, wherein (LaxSr1-x)M'O3(where, 0.1≦xxSr1-x)M'O3(where 0.1≦x≦1, and M' is at least one selected from Co, Cu, Fe, and Mn) is the catalyst for enhancing the permeation of oxygen ions. 14. The oxygen ion permeation module according to claim 11, wherein a catalyst for enhancing the oxidation reaction is applied to the surface of the ceramic member on the side of the oxidation reaction chamber and/or the porous support body located on the side of the oxidation reaction chamber from the ceramic member. 15. The oxygen ion penneation module according to claim 14, wherein an Ni-based catalyst is the catalyst for enhancing the oxidation reaction. 16. An oxygen separator comprising: an oxygen ion permeation module according to claim 6; an oxygen source supply means for causing a gas containing oxygen to flow through to the oxygen source supply chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxygen source supply chamber; and an oxidation reaction chamber gas circulation means for causing a gas with a partial pressure of oxygen lower than that on the oxygen source supply chamber side to flow through to the oxidation reaction chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxidation reaction chamber. 17. An oxygen separator comprising: an oxygen ion permeation module according to claim 11, an oxygen source supply means for causing a gas containing oxygen to flow through to the oxygen source supply chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxygen source supply chamber; and an oxidation reaction chamber gas circulation means for causing a gas with a partial pressure of oxygen lower than that on the oxygen source supply chamber side to flow through to the oxidation reaction chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxidation reaction chamber. 18. An oxidation reactor comprising: an oxygen ion permeation module according to claim 6; an oxygen source supply means for supplying a gas containing oxygen to the oxygen source supply chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxygen source supply chamber; and an oxidation target gas supply means for supplying a gas containing the oxidation target gas and having a partial pressure of oxygen lower than that on the oxygen source supply chamber side to the oxidation reaction chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxidation reaction chamber. 19. The oxidation reactor according to claim 18, wherein the oxidation reactor is a reactor for partial oxidation of hydrocarbons, and wherein the oxidation target gas is a hydrocarbon, and the flow rate of oxygen supplied by the oxygen source supply means is by a factor of two or more higher than the flow rate of the hydrocarbon supplied by the oxidation target gas supply means. 20. An oxidation reactor comprising: an oxygen ion permeation module according to claim 11; an oxygen source supply means for supplying a gas containing oxygen to the oxygen source supply chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxygen source supply chamber; and an oxidation target gas supply means for supplying a gas containing the oxidation target gas and having a partial pressure of oxygen lower than that on the oxygen source supply chamber side to the oxidation reaction chamber of the module and bringing the gas into contact with the surface of the ceramic member on the side of the oxidation reaction chamber. 21. The oxidation reactor according to claim 20, wherein the oxidation reactor is a reactor for partial oxidation of hydrocarbons, and wherein the oxidation target gas is a hydrocarbon, and the flow rate of oxygen supplied by the oxygen source supply means is by a factor of two or more higher than the flow rate of the hydrocarbon supplied by the oxidation target gas supply means.