IP Library Granted Patent US 8,409,520
Granted Patent B2
US 8,409,520 · App. 12/743,984 · Granted Apr 2, 2013

Ozone concentrator

Inventors: Koji Ota (Tokyo, JP); Yasuhiro Tanimura (Tokyo, JP); Yoichiro Tabata (Tokyo, JP); Yujiro Okihara (Tokyo, JP); Tetsuya Saitsu (Tokyo, JP); Noriyuki Nakamura (Tokyo, JP); Ryohei Ueda (Tokyo, JP)
Assignees: Mitsubishi Electric Corporation; Toshiba Mitsubishi-Electric Industrial Systems Corporation
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Quick Facts
Patent No.
US 8,409,520
App. No.
12/743,984
Granted
Apr 2, 2013
Kind
B2
Abstract

Provided is an ozone concentrator including an ozone generator ( 3 ), adsorption/desorption columns ( 4 ) in which silica gel ( 6 ) cooled with a certain-temperature refrigerant ( 25 ) for concentrating ozone generated by the ozone generator ( 3 ) is packed, a refrigerating machine ( 23 ) for cooling the refrigerant ( 25 ), a vacuum pump ( 20 ) for enhancing a concentration of the ozone in one of the adsorption/desorption columns ( 4 ) by discharging mainly oxygen from the silica gel ( 6 ) adsorbing the ozone, a plurality of valves ( 8 ) to ( 13 ) for air pressure operations, for switching passages of gas that is allowed to flow in or flow out with respect to the adsorption/desorption columns ( 4 ), and ozone concentration meters ( 28, 29 ) for measuring the concentration of the ozone enhanced by the vacuum pump ( 20 ), in which a discharge line of the vacuum pump ( 20 ) is connected to another one of the adsorption/desorption columns ( 4 ), whereby the ozone is allowed to pass through another one of the adsorption/desorption columns again. Therefore, stable ozone of high concentration can be generated at a satisfactory energy efficiency without any temperature difference between upper and lower positions of adsorption/desorption columns.

Claims (26)

1. An ozone concentrator, comprising:

an ozone generator;

a plurality of adsorption/desorption columns in which an ozone adsorbent cooled with a certain-temperature refrigerant for concentrating ozone generated by the ozone generator is packed;

cooling means for cooling the refrigerant;

discharging means connected to the plurality of adsorption/desorption columns, for concentrating the ozone in the plurality of adsorption/desorption columns by discharging a discharge gas comprising mainly oxygen from the adsorbent adsorbing the ozone; and

a plurality of valves connected to the adsorption/desorption columns, for switching passages of gas that is allowed to flow in or flow out with respect to the adsorption/desorption columns,

wherein said discharging means comprises a discharge line connecting a first adsorption/desorption column to a second adsorption/desorption column and the discharge line obtains the discharge gas from a top portion of the first adsorption/desorption column and passes the discharge gas to a bottom portion of the second adsorption/desorption column, wherein the discharge line is connected on a first end to a top portion of the first adsorption/desorption column and on a second end to a bottom portion of the second adsorption/desorption column.

2. An ozone concentrator according to claim 1 , wherein an aspiration line of the discharging means is connected to one of the plurality of adsorption/desorption columns in which adsorption has been completed.

3. An ozone concentrator according to claim 1 , wherein a period in which the discharge gas discharged from the one of the plurality of adsorption/desorption columns by the discharging means is allowed to pass through the another one of the plurality of adsorption/desorption columns and adsorbed again is set to a period from start of discharge from the one of the plurality of adsorption/desorption columns by the discharging means to achievement of a predetermined product ozone concentration by the ozone in the one of the plurality of adsorption/desorption columns.

4. An ozone concentrator according to claim 1 , wherein the adsorption/desorption columns comprise:

three adsorption/desorption columns that adsorb ozone, a vacuum that discharges the adsorbed ozone in vacuum to enhance a concentration of ozone, and a discharge line which desorps the concentrated ozone; and

one adsorption/desorption column that performs the adsorption, the vacuum discharging, and the ozone desorption independently from the three adsorption/desorption columns.

5. An ozone concentrator according to claim 1 , wherein oxygen with a purity of 99.99% or more is used as a material gas for the ozone generator.

6. An ozone concentrator, comprising:

an ozone generator;

a plurality of adsorption/desorption columns in which an ozone adsorbent cooled with a certain-temperature refrigerant for concentrating ozone generated by the ozone generator is packed;

a refrigerating machine for cooling the refrigerant;

a vacuum pump connected to the plurality of adsorption/desorption columns, for concentrating the ozone in the plurality of adsorption/desorption columns by discharging a discharge gas comprising mainly oxygen from the adsorbent adsorbing the ozone; and

a plurality of valves connected to the adsorption/desorption columns, for switching passages of gas that is allowed to flow in or flow out with respect to the adsorption/desorption columns,

wherein the vacuum pump comprises a discharge line connecting a first adsorption/desorption column to a second adsorption/desorption column and the discharge line obtains the discharge gas from a top portion of the first adsorption/desorption column and passes the discharge gas to a bottom portion of the second adsorption/desorption column, wherein the discharge line is connected on a first end to a top portion of the first adsorption/desorption column and on a second end to a bottom portion of the second adsorption/desorption column.

7. An ozone concentrator according to claim 6 , wherein an aspiration line of the vacuum pump is connected to one of the plurality of adsorption/desorption columns in which adsorption has been completed.

8. An ozone concentrator according to claim 6 , wherein a period in which the discharge gas discharged from the one of the plurality of adsorption/desorption columns by the vacuum pump is allowed to pass through the another one of the plurality of adsorption/desorption columns and adsorbed again is set to a period from start of discharge from the one of the plurality of adsorption/desorption columns by the vacuum pump to achievement of a predetermined product ozone concentration by the ozone in the one of the plurality of adsorption/desorption columns.

9. An ozone concentrator according to claim 6 , wherein the adsorption/desorption columns comprise:

three adsorption/desorption columns that adsorb ozone, a vacuum that discharges the adsorbed ozone in vacuum to enhance a concentration of ozone, and a discharge line which desorps the concentrated ozone; and

one adsorption/desorption column that performs the adsorption, the vacuum discharging, and the ozone desorption independently from the three adsorption/desorption columns.

10. An ozone concentrator according to claim 6 , wherein oxygen with a purity of 99.99% or more is used as a material gas for the ozone generator.

Assignments (3)
CHANGE OF NAME Recorded Apr 26, 2024
From: TOSHIBA MITSUBISHI-ELECTRIC INDUSTRIAL SYSTEMS CORPORATION
To: TMEIC CORPORATION
Reel/Frame 067244/0359 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 21, 2020
From: MITSUBISHI ELECTRIC CORPORATION
To: TOSHIBA MITSUBISHI-ELECTRIC INDUSTRIAL SYSTEMS CORPORATION
Reel/Frame 051887/0630 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 20, 2010
From: OTA, KOJI; TANIMURA, YASUHIRO; TABATA, YOICHIRO; OKIHARA, YUJIRO; SAITSU, TETSUYA; NAKAMURA, NORIYUKI; UEDA, RYOHEI
To: MITSUBISHI ELECTRIC CORPORATION; TOSHIBA MITSUBISHI-ELECTRIC INDUSTRIAL SYSTEMS CORPORATION
Reel/Frame 024417/0581 →
Priority Claims (1)
JP 2007-311113 · Nov 30, 2007 · national
Continuity (1)
Related Publication 20100266463A1 · Oct 21, 2010