Patent US4169708A successfully refreshed from Google Patents.
US4169708A
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US
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Method and apparatus for gas analysis
Assignee: Individual
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Filing: 1978-04-05
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Granted: 1979-10-02
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Expires: 1998-04-05
Abstract
Abstract A method and apparatus for determination of oxygen or hydrogen levels in a gas sample. In accordance with the method, a flowing stream of a gas sample containing a minor amount of diluent gas, oxygen and/or hydrogen is provided. A predetermined amount of a gaseous fuel is combined with the flowing stream of the gas sample to provide a reactive mixture. The reactive mixture is passed over a first sensing element and over a second sensing element. Prior to passing the flowing stream of the gas sample over the second sensing element, the stream is passed over a catalyst to cause reaction of oxygen and/or hydrogen with the fuel to produce water and heat. This causes a temperature and a moisture differential to exist between the first sensing element and the second sensing element. The difference in the moisture level or the temperature differential is converted to an electric signal. The electric signal produced is compared with a reference standard whereby the level of the oxygen and/or hydrogen is determined.
Inventors
- 👤 Robert Z. Muggli
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 07:09
CPC Classifications
G; G01; G01N; G01N33/00; G01N33/0004; G01N33/0009; G01N33/0011; G01N33/0014; Y; Y10; Y10T; Y10T436/00; Y10T436/20; Y10T436/207497; Y10T436/22
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
234 words
A method specific for determination of the oxygen or hydrogen level in a gas sample comprising providing a flowing stream of a gas sample containing a diluent gas selected from one of the group consisting of oxygen and hydrogn, mixing a stoichiometric excess of a gaseous fuel with said stream to provide a reactive mixture, passing said reactive mixture ober a catalyst in a reaction chamber whereby said diluent gas is caused to at least partially react with said fuel to produce water and heat, limiting said heat generated by said reaction by means of a method selected from the group consisting of in situ cooling, control of said diluent gas level, partial reaction of said diluent gas and combinations of said methods to limit temperture increase in said catalyst to less than 50° C. so as to prevent reaction of gases other than said diluent gas, passing said reactive mixture over a first sensing element prior to causing said catalytic reaction, passing said reacted mixture over a second sensing element after causing said catalytic reaction, sensing the difference caused by said catalytic reaction in a physical parameter selected from one of the group consisting of moisture and temperature, generating an electric signal by said difference sensing and comparing said electrica signal with the electric signal caused by the difference of a reference standard whereby the level of said diluent gas may be determined.
Claim 2
Independent Claim
234 words
A method specific for determination of the oxygen or hydrogen level in a gas sample comprising providing a flowing stream of a gas sample containing a diluent gas selected from one of the group consisting of oxygen and hydrogn, mixing a stoichiometric excess of a gaseous fuel with said stream to provide a reactive mixture, passing said reactive mixture ober a catalyst in a reaction chamber whereby said diluent gas is caused to at least partially react with said fuel to produce water and heat, limiting said heat generated by said reaction by means of a method selected from the group consisting of in situ cooling, control of said diluent gas level, partial reaction of said diluent gas and combinations of said methods to limit temperture increase in said catalyst to less than 50° C. so as to prevent reaction of gases other than said diluent gas, passing said reactive mixture over a first sensing element prior to causing said catalytic reaction, passing said reacted mixture over a second sensing element after causing said catalytic reaction, sensing the difference caused by said catalytic reaction in a physical parameter selected from one of the group consisting of moisture and temperature, generating an electric signal by said difference sensing and comparing said electrica signal with the electric signal caused by the difference of a reference standard whereby the level of said diluent gas may be determined.
Claim 3
Dependent Claim
23 words
A method in accordance with claim 1 wherein said sensing elements are selected from the group consisting of moisture detectors and electrothermic transducers.
Claim 4
Dependent Claim
31 words
A method in accordance with claim 1 wherein the level of said diluent gas in said gas sample is in the range of from about 0.001 ppm to about 20,000 ppm.
Claim 5
Dependent Claim
37 words
A method in accordance with claim 2 wherein said sensing element is an electrothermic transducer and wherein said dilutent gas is present in said gas sample at a level of less than about 2 percent by volume.
Claim 6
Dependent Claim
13 words
A method in accordance with claim 1 wherein said diluent gas is oxygen.
Claim 7
Dependent Claim
13 words
A method in accordance with claim 1 wherein said diluent gas is hydrogen.
Claim 8
Dependent Claim
13 words
A method in accordance with claim 5 wherein said fuel gas is hydrogen.
Claim 9
Dependent Claim
13 words
A method in accordance with claim 6 wherein said fuel gas is oxygen.
Claim 10
Dependent Claim
30 words
A method in accordance with claim 1 wherein said partial reaction of said diluent is insufficient to increase the temperature of said catalyst in said chamber above about 50° C.
Claim 11
Dependent Claim
31 words
A method in accordance with claim 1 wherein in situ cooling is sufficient to prevent the increase of the temperature of said catalyst in said reaction chamber above about 50° C.
Claim 12
Dependent Claim
31 words
A method in accordance with claim 1 wherein diluent gas level is controlled so that said temperature increase of the said catalyst in reaction chamber is limited to about 50° C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-10-01 | 1983-04-02 | 1983-10-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-10-01 | 1987-04-02 | 1987-10-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-10-01 | 1991-04-02 | 1991-10-02 | $7700.00 | Window Closed / Lapsed |