Gas separation device

Patent metadata

Field	Value
Publication number	US-2015151238-A1
Application number	US-201314407552-A
Country	US
Kind code	A1
Filing date	Jun 14, 2013
Priority date	Jun 19, 2012
Publication date	Jun 4, 2015
Grant date	—

Abstract

A simple and inexpensive gas separation device is provided. The gas separation device ( 100 ) includes: an adsorption tower ( 110 ) having an adsorbent ( 120 ) that adsorbs oxygen in a prescribed pressure and temperature environment, with at least one section thereof being exposed to a higher temperature atmosphere than a normal temperature; a first feed passage ( 132 ) connected to the adsorption tower for guiding into the adsorption tower air that has been blown from a blower device ( 130 ); a second feed passage ( 136 ) for guiding air, at a lower flow rate than the first feed passage, into the adsorption tower; a separated gas discharge path ( 140 ) connected to the adsorption tower for discharging a separated gas; a first heat exchanging unit ( 150 ) for exchanging heat between the separated gas discharged from the adsorption tower and the air guided into the adsorption tower from the first feed passage; an oxygen discharge unit ( 160 ) for reducing a pressure inside the adsorption tower, causing oxygen to desorb from the adsorption agent, and discharging oxygen from the adsorption tower; and a second heat exchanging unit ( 170 ) for exchanging heat between oxygen and the air guided into the adsorption tower from the second feed passage.

First claim

1 . A gas separation device comprising:
an adsorption tower that has an adsorbent to adsorb oxygen in a prescribed pressure and temperature environment, at least part of the adsorption tower being exposed to an atmosphere at a temperature higher than a normal temperature; a first feed passage connected to the adsorption tower, and configured to introduce into the adsorption tower a mixed gas sent from a blower device, the mixed gas containing nitrogen and oxygen as main components thereof, and a second feed passage connected to the adsorption tower and configured to introduce the mixed gas into the adsorption tower at a flow rate smaller than the first feed passage; a separated gas discharge passage connected to the adsorption tower and configured to discharge a separated gas from the adsorption tower, the separated gas containing nitrogen as a main component thereof, the separated gas being produced upon removal of oxygen, which is adsorbed by the adsorbent, from the mixed gas introduced from the first feed passage and the second feed passage; a first heat exchanging unit configured to cause heat exchange between the separated gas discharged from the adsorption tower and the mixed gas introduced to the adsorption tower from the first feed passage; an oxygen discharge unit configured to reduce an inner pressure of the adsorption tower, cause oxygen to desorb from the adsorbent, and discharge oxygen from the adsorption tower; and a second heat exchanging unit configured to cause heat exchange between the desorbed oxygen and the mixed gas introduced to the adsorption tower from the second feed passage.

2 . The gas separation device according to claim 1 , wherein a ratio of the mixed gas introduced into the adsorption tower from the first feed passage to the mixed gas introduced into the adsorption tower from the second feed passage is between 90/10 and 60/40.

3 . The gas separation device according to claim 1 , wherein the second heat exchanging unit includes a heat reserving element through which the mixed gas introduced into the adsorption tower from the second feed passage can flow and oxygen discharged from the adsorption tower can also flow such that heat of the mixed gas and oxygen is stored in the second heat exchanging unit.

4 . The gas separation device according to claim 1 , wherein the second heat exchanging unit is disposed at one end of the adsorption tower,
the oxygen discharge unit and the second feed passage are connected to that end of the adsorption tower at which the second heat exchanging unit is disposed, and the separated gas discharge passage is connected to another end of the adsorption tower.

5 . The gas separation device according to claim 1 , wherein the gas separation device includes a plurality of said adsorption towers, and
the second heat exchanging unit performs heat exchange between oxygen desorbed in one of the adsorption towers and the mixed gas introduced to another one of the adsorption towers from the second feed passage.

6 . The gas separation device according to claim 1 , wherein the adsorbent is a perovskite-type oxide.

7 . The gas separation device according to claim 2 , wherein the second heat exchanging unit includes a heat reserving element through which the mixed gas introduced into the adsorption tower from the second feed passage can flow and oxygen discharged from the adsorption tower can also flow such that heat of the mixed gas and oxygen is stored in the second heat exchanging unit.

8 . The gas separation device according to claim 2 , wherein the second heat exchanging unit is disposed at one end of the adsorption tower,
the oxygen discharge unit and the second feed passage are connected to that end of the adsorption tower at which the second heat exchanging unit is disposed, and the separated gas discharge passage is connected to another end of the adsorption tower.

9 . The gas separation device according to claim 2 , wherein the gas separation device includes a plurality of said adsorption towers, and
the second heat exchanging unit performs heat exchange between oxygen desorbed in one of the adsorption towers and the mixed gas introduced to another one of the adsorption towers from the second feed passage.

10 . The gas separation device according to claim 2 , wherein the adsorbent is a perovskite-type oxide.

11 . The gas separation device according to claim 3 , wherein the second heat exchanging unit is disposed at one end of the adsorption tower,
the oxygen discharge unit and the second feed passage are connected to that end of the adsorption tower at which the second heat exchanging unit is disposed, and the separated gas discharge passage is connected to another end of the adsorption tower.

12 . The gas separation device according to claim 3 , wherein the gas separation device includes a plurality of said adsorption towers, and
the second heat exchanging unit performs heat exchange between oxygen desorbed in one of the adsorption towers and the mixed gas introduced to another one of the adsorption towers from the second feed passage.

13 . The gas separation device according to claim 3 , wherein the adsorbent is a perovskite-type oxide.

14 . The gas separation device according to claim 4 , wherein the adsorbent is a perovskite-type oxide.

15 . The gas separation device according to claim 5 , wherein the adsorbent is a perovskite-type oxide.

16 . The gas separation device according to claim 7 , wherein the adsorbent is a perovskite-type oxide.

17 . The gas separation device according to claim 8 , wherein the adsorbent is a perovskite-type oxide.

18 . The gas separation device according to claim 9 , wherein the adsorbent is a perovskite-type oxide.

19 . The gas separation device according to claim 11 , wherein the adsorbent is a perovskite-type oxide.

20 . The gas separation device according to claim 12 , wherein the adsorbent is a perovskite-type oxide.

21 . The gas separation device according to claim 7 , wherein the second heat exchanging unit is disposed at one end of the adsorption tower,
the oxygen discharge unit and the second feed passage are connected to that end of the adsorption tower at which the second heat exchanging unit is disposed, and the separated gas discharge passage is connected to another end of the adsorption tower.

22 . The gas separation device according to claim 21 , wherein the adsorbent is a perovskite-type oxide.

23 . The gas separation device according to claim 7 , wherein the gas separation device includes a plurality of said adsorption towers, and
the second heat exchanging unit performs heat exchange between oxygen desorbed in one of the adsorption towers and the mixed gas introduced to another one of the adsorption towers from the second feed passage.

24 . The gas separation device according to claim 23 , wherein the adsorbent is a perovskite-type oxide.

Assignees

• Tokyo Gas Co Ltd
• Adsorption Technology Ind Ltd
• Univ Kyushu Nat Univ Corp
• Jnc Engineering Co Ltd

Inventors

• Fujimine Tomoya
• Nakashima Yoshifumi
• Izumi Jun
• Miura Norio
• TANIUCHI Tadashi
• Kuroki Manabu

Classifications

• B01J20/06

  comprising oxides or hydroxides of metals not provided for in group B01J20/04 · CPC title

• B01D53/047 Primary

  Pressure swing adsorption · CPC title

• C01B21/0455

  characterised by the adsorbent · CPC title

• B01D2257/104

  Oxygen · CPC title

• B01D2256/10

  Nitrogen · CPC title