Abstract A method of treating water with ozone comprising: (1) generating ozone from oxygen by an ozone generator, (2) supplying the resulting ozone-containing gas to at least three silica gel-packed adsorption towers one after another to cause the silica gel to adsorb ozone selectively from the gas while recycling discharged gas from the adsorption tower to the ozone generator, the adsorption tower being maintained at a temperature of -180° to 10° C, the silica gel containing a heavy metal in an amount of not greater than 1.0% by weight, (3) supplying a carrier gas to the adsorbed ozone-containing adsorption towers one after another at a pressure not higher than the pressure applied for the adsorption of ozone but not lower than the pressure at which the concentration of ozone in the carrier gas flowing out from the tower will be 20% by weight so as to desorb the ozone from the silica gel, (4) introducing oxygen into the deozonized adsorption towers one after another from one of the towers which has completed adsorption so as to purge away the carrier gas from the deozonized adsorption tower and a line extending therefrom, and (5) contacting the ozone-containing carrier gas discharged from the adsorption towers with the water to be treated.
Inventors
👤 Yusuke Sakamoto
👤 Munetaka Kinugasa
👤 Shigeki Endo
👤 Mituo Yamane
👤 Shigeyoshi Fujie
Bibliographic Details
Application Number—
JurisdictionUS
Data Sourcegoogle_patents
Last Synchronized2026-10-31 02:24
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/72; C02F1/78
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
251 words
In a method of treating water with ozone comprising generating ozone from oxygen by an ozone generator, supplying the resulting ozone-containing gas to at least three silica gel-packed adsorption towers one after another to cause the silica gel to adsorb ozone selectively from the gas while recycling discharged gas from the adsorption tower to the ozone generator, supplying a carrier gas for desirbing the ozone from the silica gel to the adsorbed ozone-containing adsorption towers one after another and contacting the ozone-containing carrier gas discharged from the adsorption towers with the water in the water treating tank so as to cause the ozone to react with the water, an improvement which comprises (i) switching the supply of carrier gas to the adsorption towers one after another from one to another when or immediately before or immediately after the ozone concentration in the carrier gas discharged from the adsorption tower starts to decrease so as to keep the water treating ability as constant as possible with a substantially constant ozone concentration and (ii) introducing oxygen into the adsorption towers to which the supply of carrier gas has been terminated one after another from one of the towers which has completed adsorption so as to purge away the carrier gas containing ozone from the adsorption tower and from a line extending therefrom into a water treating tank without venting the same to the atmosphere and so as to avoid the accumulation of impurities in the recycling gas and the contamination of the atmosphere.
Claim 2
Dependent Claim
251 words
In a method of treating water with ozone comprising generating ozone from oxygen by an ozone generator, supplying the resulting ozone-containing gas to at least three silica gel-packed adsorption towers one after another to cause the silica gel to adsorb ozone selectively from the gas while recycling discharged gas from the adsorption tower to the ozone generator, supplying a carrier gas for desirbing the ozone from the silica gel to the adsorbed ozone-containing adsorption towers one after another and contacting the ozone-containing carrier gas discharged from the adsorption towers with the water in the water treating tank so as to cause the ozone to react with the water, an improvement which comprises (i) switching the supply of carrier gas to the adsorption towers one after another from one to another when or immediately before or immediately after the ozone concentration in the carrier gas discharged from the adsorption tower starts to decrease so as to keep the water treating ability as constant as possible with a substantially constant ozone concentration and (ii) introducing oxygen into the adsorption towers to which the supply of carrier gas has been terminated one after another from one of the towers which has completed adsorption so as to purge away the carrier gas containing ozone from the adsorption tower and from a line extending therefrom into a water treating tank without venting the same to the atmosphere and so as to avoid the accumulation of impurities in the recycling gas and the contamination of the atmosphere.