US2006171875A1PendingUtilityA1
Methods for making chlorine dioxide
Est. expiryAug 2, 2021(expired)· nominal 20-yr term from priority
B01J 39/04B01J 31/08B01J 39/02C01B 11/028C01B 11/08C01B 11/023C01B 11/02B01J 41/02C01B 11/024B01J 41/04C01B 11/022
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Claims
Abstract
Chlorine dioxide is generated in a controlled manner from chlorous acid by catalysis. Chlorine dioxide can be generated either subsequent to the generation of chlorous acid or simultaneously with the generation of chlorous acid. For catalysis of chlorous acid to chlorine dioxide, the chlorous acid may be generated by ion exchange or in a conventional manner.
Claims
exact text as granted — not AI-modified1 . A process for generating chlorine dioxide from chlorous acid which comprises contacting chlorous acid with an insoluble catalytic material in a moist environment for a time sufficient to form chlorine dioxide.
2 . The process of claim 1 wherein said catalytic material is deposited on an ion exchange material.
3 . The process of claim 1 wherein said catalytic material is an ion exchange material.
4 . The process of claim 1 wherein said catalytic material is deposited on an inorganic or organic substrate.
5 . The process of claim 4 wherein said catalytic material comprises platinum coated acid-washed carbon particles.
6 . The process of claim 1 wherein said catalytic material comprises a mixture of a first and second ion exchange material and said second ion exchange material has a catalyst deposited on the surface of the material.
7 . The process of claim 1 wherein said catalytic material comprises a mixture of a first and second substrate material and said second substrate material has a catalyst deposited on the surface of the material.
8 . The process of claim 1 wherein said catalytic material is selected from the group consisting of platinum, palladium, manganese dioxide, and carbon.
9 . The process of claim 6 wherein said catalytic material is selected from the group consisting of platinum, palladium, manganese dioxide, and carbon.
10 . The process of claim 2 wherein said ion exchange material is selected from the group consisting of inorganic resins, organic resins, membranes, powders and gels.
11 . The process of claim 3 wherein said ion exchange material is selected from the group consisting of inorganic resins, organic resins, membranes, powders and gels.
12 . The process of claim 2 wherein said ion exchange material is selected from the group consisting of a weak acid cation exchange resin or powder, a strong acid cation exchange resin or powder, a weak base anion exchange resin or powder, and strong base anion exchange resin or powder.
13 . The process of claim 3 wherein said ion exchange material is selected from the group consisting of a weak acid cation exchange resin or powder, a strong acid cation exchange resin or powder, a weak base anion exchange resin or powder, and strong base anion exchange resin or powder.
14 . The process of claim 2 wherein said ion exchange material is disposable.
15 . The process of claim 3 wherein said ion exchange material is disposable.
16 . The process of claim 2 wherein said ion exchange material is regenerable.
17 . The process of claim 3 wherein said ion exchange material is regenerable.
18 . The process of claim 1 wherein said moist environment is an aqueous solution.
19 . A process for generating chlorine dioxide from chlorous acid which comprises contacting chlorous acid with a inorganic cation exchange material having a catalyst deposited on the surface of said material, in a moist environment for a time sufficient to form chlorine dioxide.
20 . The process for generating chlorine dioxide from chlorous acid of claim 19 , wherein said catalyst comprises manganese dioxide.
21 . The process for generating chlorine dioxide from chlorous acid of claim 19 , wherein said catalyst comprises platinum.
22 . A process for generating chlorine dioxide from chlorous acid which comprises contacting chlorous acid with an organic anion exchange material having palladium deposited on the surface of said material, in a moist environment for a time sufficient to form chlorine dioxide.
23 . A process for generating chlorine dioxide which comprises:
a) contacting a chlorite salt solution with a cation exchange material in the hydrogen form in a moist environment for a time sufficient to effect an essentially complete substitution of cations in the chlorite salt with hydrogen ions on the cation exchange material to form chlorous acid; and b) contacting the chlorous acid produced in step a) with a catalytic material in a moist environment for a time sufficient to form chlorine dioxide.
24 . The process of claim 23 wherein said catalytic material is deposited on an ion exchange material.
25 . The process of claim 23 wherein said catalytic material is an ion exchange material.
26 . The process of claim 23 wherein said catalytic material is deposited on an inorganic or organic substrate.
27 . The process of claim 26 wherein said catalytic material comprises platinum coated acid-washed carbon particles.
28 . The process of claim 23 wherein said catalytic material comprises a mixture of a first and second ion exchange material and said second ion exchange material has a catalyst deposited on the surface of the material.
29 . The process of claim 23 wherein said catalytic material comprises a mixture of a first and second substrate material and said second substrate material has a catalyst deposited on the surface of the material.
30 . The process of claim 23 wherein said catalytic material is selected from the group consisting of platinum, palladium, manganese dioxide, and carbon.
31 . The process of claim 28 wherein said catalytic material is selected from the group consisting of platinum, palladium, manganese dioxide, and carbon.
32 . The process of claim 24 wherein said ion exchange material is selected from the group consisting of inorganic resins, organic resins, membranes, powders and gels.
33 . The process of claim 25 wherein said ion exchange material is selected from the group consisting of inorganic resins, organic resins, membranes, powders and gels.
34 . The process of claim 24 wherein said ion exchange material is selected from the group consisting of a weak acid cation exchange material or powder, a strong acid cation exchange material or powder, a weak base anion exchange resin or powder, and strong base anion exchange resin or powder.
35 . The process of claim 25 wherein said ion exchange material is selected from the group consisting of a weak acid cation exchange resin or powder, a strong acid cation exchange resin or powder, a weak base anion exchange resin or powder, and strong base anion exchange resin or powder.
36 . The process of claim 24 wherein said ion exchange material is disposable.
37 . The process of claim 25 wherein said ion exchange material is disposable.
38 . The process of claim 24 wherein said ion exchange material is regenerable.
39 . The process of claim 25 wherein said ion exchange material is regenerable.
40 . The process of claim 23 wherein said moist environment is an aqueous solution.
41 . A process for generating chlorine dioxide from chlorous acid which comprises the following steps:
a) contacting a chlorate salt solution with a cation exchange material in the hydrogen form in a moist environment for a time sufficient to to effect an essentially complete substitution of cations in the chlorate salt with hydrogen ions on the cation exchange material to form chlorous acid; and b) contacting the chlorous acid produced in step a) with an catalytic material in a moist environment for a time sufficient to form chlorine dioxide.
42 . The process of claim 41 wherein said catalytic material is deposited on an ion exchange material.
43 . The process of claim 41 wherein said catalytic material is an ion exchange material.
44 . The process of claim 41 wherein said catalytic material is deposited on an inorganic or organic substrate.
45 . The process of claim 44 wherein said catalytic material comprises platinum coated acid-washed carbon particles.
46 . The process of claim 41 wherein said catalytic material comprises a mixture of a first and second ion exchange material and said second ion exchange material has a catalyst deposited on the surface of the material.
47 . The process of claim 41 wherein said catalytic material comprises a mixture of a first and second substrate material and said second substrate material has a catalyst deposited on the surface of the material.
48 . The process of claim 46 wherein said catalytic material is selected from the group consisting of platinum, palladium, manganese dioxide, and carbon.
49 . The process of claim 47 wherein said catalytic material is selected from the group consisting of platinum, palladium, manganese dioxide, and carbon.
50 . The process of claim 42 wherein said ion exchange material is selected from the group consisting of inorganic resins, organic resins, membranes, powders and gels.
51 . The process of claim 43 wherein said ion exchange material is selected from the group consisting of inorganic resins, organic resins, membranes, powders and gels
52 . The process of claim 42 wherein said ion exchange material is selected from the group consisting of a weak acid cation exchange resin or powder, a strong acid cation exchange resin or powder, a weak base anion exchange resin or powder, and strong base anion exchange resin or powder.
53 . The process of claim 43 wherein said ion exchange material is selected from the group consisting of a weak acid cation exchange resin or powder, a strong acid cation exchange resin or powder, a weak base anion exchange resin or powder, and strong base anion exchange resin or powder.
54 . The process of claim 42 wherein said ion exchange material is disposable.
55 . The process of claim 43 wherein said ion exchange material is disposable.
56 . The process of claim 42 wherein said ion exchange material is regenerable.
57 . The process of claim 43 wherein said ion exchange material is regenerable.
58 . The process of claim 41 wherein said moist environment is an aqueous solution.Cited by (0)
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