US3958956A
Expired / Lapsed
US
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Methane production process and arrangement therefor
Assignee: Krupp Koppers GmbH
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Filing: 1974-07-09
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Granted: 1976-05-25
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Expires: 1994-07-09
Abstract
Abstract The gaseous product obtained by the partial oxidation of a fuel such as coal and/or oil is desulfurized and then admitted into a packed gas-liquid contact column. Here, the gas comes into contact with water so as to become at least partially saturated with water vapor. The gas is next conveyed to a reactor wherein it undergoes a methane-forming reaction under isothermal conditions, the methane-forming reaction taking place without previously subjecting the gas to a conversion reaction. The methane-forming reaction is carried out catalytically with a nickel-containing catalyst and deposition of carbon from the gas onto the catalyst is prevented by virtue of the water vapor present during the reaction. The quantity of water vapor present during the reaction is adjusted so as to lie between predetermined limits. After completion of the reaction, the gas is admitted into another packed gas-liquid column wherein it is cooled by contact with cooling water at which time residual water vapor in the gas condenses. Subsequent to the cooling operation, the gas may be scrubbed so as to remove carbon dioxide therefrom and thereby obtain a gas containing at least 80 volume percent methane. The cooling water is heated during the cooling operation and this cooling water, together with the condensed water vapor, is conveyed to the first-mentioned column where it is used for at least partially saturating the gas to be treated with water vapor. Excess water which is not used for the saturation is conveyed back to the second-mentioned column to be used as cooling water.
Inventors
- 👤 Eberhard Goeke
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 01:17
CPC Classifications
C; C10; C10K; C10K3/00; C10K3/02; C01; C01B; C01B3/00; C01B3/02; C01B3/22; C01B3/32; C01B3/34; C01B3/36; C07; C07C; C07C1/00; C07C1/02; C07C2523/00; C07C2523/70; C07C2523/74; C07C2523/755
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
294 words
A continuous process for methanizing the gaseous product obtained in the partial oxidation of coal or heavy hydrocarbon oil comprising the steps, carried out in continuous operation, of a. passing said gaseous oxidation product, as obtained from said oxidation process and without preceding modification of its carbon monoxide, carbon dioxide or hydrogen contents, in countercurrent through high temperature water in a gas-liquid contact tower so as to at least partially saturate the gas with water vapor; b. then passing the gas from said saturation tower into a catalytic reactor and there bringing it in contact with a nickel catalyst at a temperature of about 330° to 450°C and a pressure of about 3 to 60 atm above atmospheric so as to methanize the gas; c. then passing the gas into a second gas-liquid contact tower and moving it in countercurrent to cooling water so as to cool it and dry it by condensation of the accompanying water vapor, and d. withdrawing and recovering the gas having a high methane content from said cooling tower; the said high temperature saturation water and water vapor and the said cooling water being moved in a single closed flow circuit between said two towers, the high temperature water and steam being obtained from the heat exchange between the cooling water and the hot methanized gas in said cooling tower and being passed through a portion of said flow circuit from the bottom of said cooling tower to the head of said saturation tower, and the said cooling water being obtained from the heat exchange between the high temperature water and the fresh incoming gas and being passed through another portion of said flow circuit from the bottom of said saturation tower to the head of said cooling tower.
Claim 2
Dependent Claim
294 words
A continuous process for methanizing the gaseous product obtained in the partial oxidation of coal or heavy hydrocarbon oil comprising the steps, carried out in continuous operation, of a. passing said gaseous oxidation product, as obtained from said oxidation process and without preceding modification of its carbon monoxide, carbon dioxide or hydrogen contents, in countercurrent through high temperature water in a gas-liquid contact tower so as to at least partially saturate the gas with water vapor; b. then passing the gas from said saturation tower into a catalytic reactor and there bringing it in contact with a nickel catalyst at a temperature of about 330° to 450°C and a pressure of about 3 to 60 atm above atmospheric so as to methanize the gas; c. then passing the gas into a second gas-liquid contact tower and moving it in countercurrent to cooling water so as to cool it and dry it by condensation of the accompanying water vapor, and d. withdrawing and recovering the gas having a high methane content from said cooling tower; the said high temperature saturation water and water vapor and the said cooling water being moved in a single closed flow circuit between said two towers, the high temperature water and steam being obtained from the heat exchange between the cooling water and the hot methanized gas in said cooling tower and being passed through a portion of said flow circuit from the bottom of said cooling tower to the head of said saturation tower, and the said cooling water being obtained from the heat exchange between the high temperature water and the fresh incoming gas and being passed through another portion of said flow circuit from the bottom of said saturation tower to the head of said cooling tower.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein the said gaseous oxidation product is subjected to desulfurization prior to entering said saturation tower.
Claim 4
Dependent Claim
27 words
The process of claim 1 wherein the high methane content gas after removal from the cooling tower is subjected to removal of the carbon dioxide contained therein.
Claim 5
Dependent Claim
38 words
The process of claim 1 wherein the saturated gas is further preheated prior to entering the reactor to a temperature of about 270° to 300°C with the hot methanized gas flowing from the reactor to the cooling tower.
Claim 6
Dependent Claim
17 words
The process of claim 1 wherein the circulation of the water in the closed circuit is power-forced.
Claim 7
Dependent Claim
26 words
The process of claim 1, wherein steam is added to the gas from an external source to increase the saturation of the gas with water vapor.
Claim 8
Dependent Claim
29 words
The process of claim 6 wherein the steam is added to the flow of saturated gas from said saturation tower prior to entering of the gas into the reactor.
Claim 9
Dependent Claim
33 words
The process of claim 1 wherein the temperature in the reactor is maintained substantially constant by a heat exchange system while the excess steam generated in the system is withdrawn for external use.
Claim 10
Independent Claim
207 words
An apparatus for methanizing the gaseous product obtained in the partial oxidation of coal or heavy hydrocarbon oil, the said apparatus comprising a saturation tower for at least partially saturating the gas with water vapor, an inlet for the gaseous oxidation product disposed at the lower portion of said saturation tower, a reactor vessel for bringing the gas in contact with the catalyst in order to methanize it, a cooling tower for cooling the hot methanized gas, an outlet at the upper portion of said cooling tower for discharging the methanized gas, gas conduit means for passing the at least partially saturated gas from the top portion of the reactor vessel and for passing the methanized gas from the bottom portion of the reactor vessel to the lower portion of the cooling tower, water conduit means for passing high temperature water from the bottom of the cooling tower to the head of the saturation tower and passing cooling water from the bottom of the saturation tower to the head of the cooling tower and means for withdrawing the cooled methanized gas from the apparatus, the said means for passing heated water and means for passing cooling water, together with said two towers, forming a closed flow circuit.
Claim 11
Independent Claim
207 words
An apparatus for methanizing the gaseous product obtained in the partial oxidation of coal or heavy hydrocarbon oil, the said apparatus comprising a saturation tower for at least partially saturating the gas with water vapor, an inlet for the gaseous oxidation product disposed at the lower portion of said saturation tower, a reactor vessel for bringing the gas in contact with the catalyst in order to methanize it, a cooling tower for cooling the hot methanized gas, an outlet at the upper portion of said cooling tower for discharging the methanized gas, gas conduit means for passing the at least partially saturated gas from the top portion of the reactor vessel and for passing the methanized gas from the bottom portion of the reactor vessel to the lower portion of the cooling tower, water conduit means for passing high temperature water from the bottom of the cooling tower to the head of the saturation tower and passing cooling water from the bottom of the saturation tower to the head of the cooling tower and means for withdrawing the cooled methanized gas from the apparatus, the said means for passing heated water and means for passing cooling water, together with said two towers, forming a closed flow circuit.
Claim 12
Dependent Claim
24 words
The apparatus of claim 9 which includes separate pumps disposed in said flow circuit for moving the high temperature water and the cooling water.
Claim 13
Dependent Claim
32 words
The apparatus of claim 9 which includes means for admitting steam to said gas from an external source at a point prior to where said gas conduit means leads into said reactor.
Claim 14
Dependent Claim
45 words
The apparatus of claim 9 which includes heat-exchange means disposed ahead of the reactor vessel and adapted to provide heat-exchange between the at least partially saturated gas and the methanized gas whereby a preheating of the circulating gas is effected prior to the methanized reaction.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-05-25 | 1979-11-24 | 1980-05-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-05-25 | 1983-11-24 | 1984-05-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-05-25 | 1987-11-24 | 1988-05-25 | $7700.00 | Window Closed / Lapsed |