US4059683A
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Decomposition of halogenated organic compounds
Assignee: Vista Chemical Co
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Filing: 1976-06-14
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Granted: 1977-11-22
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Expires: 1996-06-14
Abstract
Abstract A method for decomposing halogenated organic compounds which comprises: (a) preheating the halogenated organic compound to a temperature above about 300° C. and (b) contacting the preheated organic compound with a platinum catalyst in the presence of an oxidizing agent at a temperature of at least 350° C. The process converts the major part of the halide in the organic halide to hydrogen halide.
Inventors
- 👤 Robert C. Lindberg
- 👤 James D. Reedy
- 👤 Kang Yang
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 11:16
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8659; B01D53/8662; C; C01; C01B; C01B7/00; C01B7/01
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
126 words
A method for decomposing halogenated organic compounds said halogenated organic compounds containing 1 to 4 carbon atoms and containing at least as many hydrogen atoms as halogen atoms, said method comprising: a. heating the halogenated organic compounds to a temperature in the range of above about 300° C. to about 500° C., and, b. then contacting the heated organic compounds with a catalyst, which is platinum-impregnated on a nonoxidizing carrier, in the presence of an oxidizing agent and in the absence of added hydrocarbons at a temperature, which is at least 350° C. and is higher than the temperature of step (a), said method being characterized further in that at least 99% of the halogen present in the halogenated organic compounds is converted to hydrogen halides.
Claim 2
Independent Claim
126 words
A method for decomposing halogenated organic compounds said halogenated organic compounds containing 1 to 4 carbon atoms and containing at least as many hydrogen atoms as halogen atoms, said method comprising: a. heating the halogenated organic compounds to a temperature in the range of above about 300° C. to about 500° C., and, b. then contacting the heated organic compounds with a catalyst, which is platinum-impregnated on a nonoxidizing carrier, in the presence of an oxidizing agent and in the absence of added hydrocarbons at a temperature, which is at least 350° C. and is higher than the temperature of step (a), said method being characterized further in that at least 99% of the halogen present in the halogenated organic compounds is converted to hydrogen halides.
Claim 3
Independent Claim
154 words
A method for decomposing halogenated organic compounds said halogenated organic compounds containing 1 to 4 carbon atoms and containing at least as many hydrogen atoms as halogen atoms said method comprising: a. heating a gaseous stream comprising said halogenated organic compounds and an oxidizing gas selected from air and a mixture of nitrogen and air to a temperature in the range of above about 300° C. to about 500° C. and, b. passing the heated gaseous stream of step (a) to a heated zone wherein it contacts a catalyst, which is platinum-impregnated on a nonoxidizing carrier, at a temperature which is at least 350° C. and is higher than the temperature of step (a), said method being characterized further in that (a) at least 99% of the halogen present in the halogenated organic compounds is converted to hydrogen halides and (b) said halogenated organic compounds and said oxidizing gas are the only reactive materials.
Claim 4
Independent Claim
154 words
A method for decomposing halogenated organic compounds said halogenated organic compounds containing 1 to 4 carbon atoms and containing at least as many hydrogen atoms as halogen atoms said method comprising: a. heating a gaseous stream comprising said halogenated organic compounds and an oxidizing gas selected from air and a mixture of nitrogen and air to a temperature in the range of above about 300° C. to about 500° C. and, b. passing the heated gaseous stream of step (a) to a heated zone wherein it contacts a catalyst, which is platinum-impregnated on a nonoxidizing carrier, at a temperature which is at least 350° C. and is higher than the temperature of step (a), said method being characterized further in that (a) at least 99% of the halogen present in the halogenated organic compounds is converted to hydrogen halides and (b) said halogenated organic compounds and said oxidizing gas are the only reactive materials.
Claim 5
Dependent Claim
18 words
The process of claim 1 wherein the oxidizing agent is air or a mixture of nitrogen and oxygen.
Claim 6
Dependent Claim
55 words
The process of claim 3 wherein the halogenated organic compounds are selected from the group consisting of vinyl halides and mixtures of C 1 halogenated compounds and C 2 halogenated compounds containing vinyl halides wherein the total number of hydrogen atoms in the mixture is at least equal to the total number of halogen atoms.
Claim 7
Dependent Claim
15 words
The process of claim 4 wherein the halogen of said halogenated organic compounds is chlorine.
Claim 8
Dependent Claim
33 words
The process of claim 5 wherein the temperature in step (a) is above 320° C and the temperature is step (b) is in the range of about 350° C to about 600° C.
Claim 9
Dependent Claim
33 words
The process of claim 6 wherein the temperature of step (a) is above 340° C. and the temperature of step (b) is in the range of about 400° C. to about 500° C.
Claim 10
Dependent Claim
55 words
The process of claim 2 wherein the halogenated organic compounds are selected from the group consisting of vinyl halides and mixtures of C 1 halogenated compounds and C 2 halogenated compounds containing vinyl halides wherein the total number of hydrogen atoms in the mixture is at least equal to the total number of halogen atoms.
Claim 11
Dependent Claim
15 words
The process of claim 8 wherein the halogen of said halogenated organic compounds is chlorine.
Claim 12
Dependent Claim
33 words
The process of claim 9 wherein the temperature in step (a) is above 320° C. and the temperature in step (b) is in the range of about 350° C. to about 600° C.
Claim 13
Dependent Claim
33 words
The process of claim 10 wherein the temperature in step (a) is above 340° C. and the temperature in step (b) is in the range of about 400° C. to about 500° C.
Claim 14
Dependent Claim
11 words
The process of claim 11 wherein the nonoxidizing carrier is alumina.
References Cited (Backward Citations)
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| 3.5 Years (Year 4) | 1980-11-21 | 1981-05-23 | 1981-11-22 | $2000.00 | Window Closed / Lapsed |
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