Gas processing apparatus
US-2019282722-A1 · Sep 19, 2019 · US
US2018369751A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018369751-A1 |
| Application number | US-201715814823-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 16, 2017 |
| Priority date | Jun 22, 2017 |
| Publication date | Dec 27, 2018 |
| Grant date | — |
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A carbonized material, a device for removing ozone, and a method for removing ozone are provided. The carbonized material has at least a carbonyl-containing group, alkylol group, and carbon having sp 2 hybrid orbital. In particular, the at least one carbonyl-containing group has a carbon content from 10 atom % to 30 atom %, based on the total carbon atoms of the at least one carbonyl-containing group, the at least one alkylol group, and the at least one carbon having sp 2 hybrid orbital.
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What is claimed is: 1 . A carbonized material, comprising: at least one carbonyl-containing group; at least one alkylol group; and at least one carbon having sp 2 hybrid orbital, wherein the at least one carbonyl-containing group has a carbon content from 10 atom % to 30 atom %, based on the total carbon atoms of the at least one carbonyl-containing group, the at least one alkylol group, and the at least one carbon having sp 2 hybrid orbital. 2 . The carbonized material as claimed in claim 1 , wherein the carbonyl-containing group is selected from a group consisting of carbonyl group, carbonyloxy group and oxycarbonyl group. 3 . The carbonized material as claimed in claim 1 , wherein the at least one carbonyl-containing group has a carbon content from 10 atom % to 25 atom %, based on the total carbon atoms of the at least one carbonyl-containing group, the at least one alkylol group, and the at least one carbon having sp 2 hybrid orbital. 4 . The carbonized material as claimed in claim 1 , wherein 1.0 g of the carbonized material is capable of decomposing 0.8 g-2.0 g of ozone with a relative humidity of 95% at 25° C. . 5 . A device for removing ozone, comprising: a chamber; and the carbonized material as claimed in claim 1 , disposed within the chamber. 6 . The device for removing ozone as claimed in claim 5 , further comprising: an inlet for introducing a gas into the chamber; and an outlet for exhausting the gas passing through the carbonized material from the chamber. 7 . The device for removing ozone as claimed in claim 6 , further comprising: a humidifier connected to the chamber in order to maintain a specific relative humidity in the chamber. 8 . A method for removing ozone, comprising: providing a gas, wherein the gas has an ozone concentration that is higher than or equal to 0.1 ppm; and forcing the gas to pass through the carbonized material as claimed in claim 1 , such that the ozone of the gas reacts with the carbonized material. 9 . The method as claimed in claim 8 , wherein the ozone is converted into carbon dioxide and water after reacting with the carbonized material. 10 . The method as claimed in claim 8 , wherein the ozone of the gas reacts with the carbonized material with a relative humidity from 10% to 99%.
Organic compounds not provided for in groups B01D2251/206 or B01D2251/208 · CPC title
Esters of carboxylic acids; Esters of carbonic or haloformic acids (ortho esters, see the relevant groups, e.g. C07C43/32) · CPC title
by reduction · CPC title
Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen · CPC title
from inorganic compounds · CPC title
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