Gas separation membrane module and gas separation method
A process for producing nitrogen-rich air by feeding high temperature air at 150° C. or more to an air separation membrane module is described. After being placed at 175° C. for two hours, the air separation module exhibits a shape-retention ratio of 95% or more in one embodiment. The nitrogen-rich air can be fed to a fuel tank for an aircraft, for example.
1. A process for producing nitrogen-rich air from the air using an air separation membrane module including an air separation membrane, the process comprising feeding the air at 175° C. or higher to the air separation membrane, wherein the air separation membrane in the air separation membrane module comprises a material having no glass-transition temperature at 300° C. or lower,
wherein for the air separation membrane module,
at the initiation of the use, an oxygen-gas permeation rate (P′ O2 ) at 175° C. is 20×10 −5 cm 3 (STP)/cm 2 ·sec ·cmHg or more and a ratio of an oxygen-gas permeation rate to a nitrogen-gas permeation rate (P′ O2 /P′ N2 )at 175° C. is 1.8 or more; and
after the use at 175° C. for 140 hours, P′ O2 and P′ O2 /P′ N2 are retained in levels of 90% or more of P′ O2 and P′ O2 /P′ N2 before the initiation of the use, respectively.
2. A process for producing nitrogen-rich air from the air using an air separation membrane module including an air separation membrane, the process comprising feeding the air at 175° C. or higher to the air separation membrane, wherein the air separation membrane in the air separation membrane module comprises a material having no glass-transition temperature at 300° C. or lower,
wherein after being placed at 175° C. for 2 hours, the air separation membrane exhibits a shape-retention ratio of 95% or more.
3. A method for explosion protection of an aircraft, comprising producing nitrogen-rich air by the production process as claimed in claim 1 and feeding the nitrogen-rich air to a fuel tank for an aircraft.
4. A method for explosion protection of an aircraft, comprising producing nitrogen-rich air by the production process as claimed in claim 2 and feeding the nitrogen-rich air to a fuel tank for an aircraft.
5. The process according to claim 1 , wherein the material having no glass-transition temperature at 300° C. or lower in the air separation membrane comprises polyimide.
6. The process according to claim 2 , wherein the material having no glass-transition temperature at 300° C. or lower in the air separation membrane comprises polyimide.