Method for separating/recovering oxygen-rich air from air, its apparatus and gas separation membrane module
A method for separating and recovering oxygen-rich air from the air, comprising, using a gas separation membrane module where a laminate consisting of a permeate-side spacer for forming a permeate gas channel communicated with a hollow section in a core tube for collecting and discharging a permeate gas and two flat-film gas separation membranes sandwiching the spacer and a feed-side spacer for forming a feed gas channel are spirally wound around the core tube such that the laminate and the feed-side spacer are alternately superimposed, vacuuming the hollow section of the core tube to 95 kPaA (absolute pressure) or less by vacuuming means while feeding the air into the feed gas channel by air feed means such that a maximum feed-air flow rate and a maximum static pressure divided by an effective membrane area of the gas separation membrane are 100 m 3 /min·m 2 or less and 4000 Pa/m 2 or less, respectively, to separate and recover oxygen-rich air from the hollow section of the core tube. Oxygen-rich air can be separated and recovered from the air by this method with high separation efficiency.
1. A method for separating and recovering oxygen-rich air from the air, comprising:
providing a gas separation membrane module where
(i) a laminate comprising a permeate-side spacer for forming a permeate gas channel communicated with a hollow section in a core tube for collecting and discharging a permeate gas and two flat-film gas separation membranes sandwiching the spacer and
(ii) a feed-side spacer for forming a feed gas channel are spirally wound around the core tube such that the laminate and the feed-side spacer are alternately superimposed, wherein a thickness ratio of the permeate-side spacer to the feed-side spacer is 1:2 to 1:10; and
vacuuming the hollow section of the core tube to 95 kPaA or less by vacuuming means while feeding the air into the feed gas channel by a fan or a blower having such a capacity that a maximum feed-air flow rate and a maximum static pressure divided by an effective membrane area of the gas separation membrane are 100 m 3 /min·m 2 or less and 4000 Pa/m 2 or less, respectively, to separate and recover oxygen-rich air from the hollow section of the core tube.
2. The method as claimed in claim 1 , wherein the gas separation membrane module has a plurality of laminates; each of the laminates comprising a permeate-side spacer for forming a permeate gas channel communicated with a hollow section in a core tube for collecting and discharging a permeate gas and two flat-film gas separation membranes sandwiching the spacer; wherein the laminates are spirally wound around the core tubes together with feed-side spacers for forming feed gas channel such that the laminates and the feed-side spacers are alternately superimposed.
3. The method as claimed in claim 1 , wherein the air flowing in the feed gas channel has substantially atmospheric pressure.
4. An apparatus for separating and recovering oxygen-rich air, comprising:
(a) a gas separation membrane module where
(i) a laminate comprising a permeate-side spacer for forming a permeate gas channel communicated with a hollow section in a core tube for collecting and discharging a permeate gas and two flat-film gas separation membranes sandwiching the spacer and
(ii) a feed-side spacer for forming a feed gas channel are spirally wound around the core tube such that the laminate and the feed-side spacer are alternately superimposed, wherein a thickness ratio of the permeate-side spacer to the feed-side spacer is 1:2 to 1:10;
(b) a fan or a blower for feeding the air into the feed gas channel, the fan or the blower having such a capacity that a maximum feed-air flow rate and a maximum static pressure divided by an effective membrane area of the gas separation membrane are 100 m 3 /min·m 2 or less and 4000 Pa/m 2 or less, respectively; and
(c) vacuuming means whereby the hollow section of the core tube is vacuumed to 95 kPaA or less to separate and recover oxygen-rich air from the hollow section of the core tube.
5. The apparatus as claimed in claim 4 , wherein the gas separation membrane module has a plurality of laminates; each of the laminates comprising a permeate-side spacer for forming a permeate gas channel communicated with a hollow section in a core tube for collecting and discharging a permeate gas and two flat-film gas separation membranes sandwiching the spacer; wherein the laminates are spirally wound around the core tubes together with feed-side spacers for forming feed gas channel such that the laminates and the feed-side spacers are alternately superimposed.
6. The apparatus as claim 4 , wherein the fan or blower, and the feed-side spacer are adapted to allow the air with substantially atmospheric pressure to flow in the feed gas channel.
7. A gas separation membrane module, comprising:
a plurality of laminates; each of the laminates comprising a permeate-side spacer for forming a permeate gas channel communicated with a hollow section in a core tube for collecting and discharging a permeate gas and two flat-film gas separation membranes sandwiching the spacer; wherein the laminates are spirally wound around the core tubes together with feed-side spacers for forming feed gas channel such that the laminates and the feed-side spacers are alternately superimposed,
wherein a thickness ratio of the permeate-side spacer to the feed-side spacer is 1:2 to 1:10, and
wherein the feed-side spacer is adapted to allow air to flow in the feed gas channel with substantially atmospheric pressure when the air is fed by a fan or a blower having such a capacity that a maximum feed-air flow rate and a maximum static pressure divided by an effective membrane area of the gas separation membrane are 100 m 3/ min m 2 or less and 4000 Pa/m 2 or less, respectively,
whereby the module separates and recovers oxygen-rich air from a hollow section by vacuuming the hollow section while feeding the air to a feed gas channel.