GB191216855A - Improvements in the Production of Nitrogen from Products of Combustion. - Google Patents
Improvements in the Production of Nitrogen from Products of Combustion.Info
- Publication number
- GB191216855A GB191216855A GB191216855DA GB191216855A GB 191216855 A GB191216855 A GB 191216855A GB 191216855D A GB191216855D A GB 191216855DA GB 191216855 A GB191216855 A GB 191216855A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gases
- gas
- air
- copper
- catalyst
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/04—Purification or separation of nitrogen
- C01B21/0405—Purification or separation processes
- C01B21/0411—Chemical processing only
- C01B21/0422—Chemical processing only by reduction
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0045—Oxygen
Landscapes
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
16,855. Harger, J. July 19. Nitrogen.-An inert gaseous mixture consisting principally or entirely of nitrogen and carbon dioxide, and which may be separated into its components, is prepared by passing a mixture of air and combustible gases in combining proportions, or the products of a carefully regulated combustion, under high pressure and relatively low temperature over a catalytic agent such as titaniferous bog iron ore, fireclay, or asbestos, with or without the employment of a mixture of copper and copper oxide which acts as an equilibrator. Preferably a gas-fired boiler is the source of the products of combustion, the catalyst being conveniently placed in the boiler tubes. The gases are delivered from an air-compressor and mixed in the right proportions for complete combustion, a convenient combustible being mine gas, containing a small proportion of methane, alone or mixed with producer-gas. A coal-dust fired boiler may also be used, or the exhaust from a gas - engine, except from an air - scavenged engine, or, less suitably, ordinary flue gases. For use, the bog iron ore may be mixed with fire-clay and moulded or burnt into small bricks &c. The heat of the burnt gases after passing over the catalyst may be used to heat feedwater, or the air and gas supply in the case of a gas-fired boiler. Any excess of oxygen in the gases passing from the catalyst is removed by the copper in the equilibrator, and any carbon monoxide is oxidized by the copper oxide. The equilibrator is preferably constructed to contain the catalyst and the copper and copper oxide in two compartments of the same apparatus, made of iron, the second compartment being fitted with a silica observation plate. Copper and copper oxide may be placed in the boiler tubes to act as both catalyst and equilibrator. The gases obtained are first scrubbed with limestone to remove sulphur dioxide, but sulphur compounds are preferably removed from the gas before reaching the gasengine, when such is used. The carbon dioxide is then extracted by compressing (if not already sufficiently compressed) and cooling the gases in presence of water, and finally cooling by expansion so that the dioxide is liquefied and can be trapped off, for example, by causing the compressed gases to expand while doing work in an air-engine, the exhaust from which is used to cool the compressed gas which is led to the air - engine, water being thoroughly removed from the compressed gas before being cooled. Heat evolved during compression may be used for heating feed-water &c. The gases which leave the motor are free from all traces of water or carbon monoxide and contain only a small quantity of carbon dioxide. Or the compressed mixed gases are cooled to air temperature and led away for use. Specification 28,075/11, [Class 1(i), Chemical processes &c.], is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB191216855T | 1912-07-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB191216855A true GB191216855A (en) | 1913-07-21 |
Family
ID=32642077
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB191216855D Expired GB191216855A (en) | 1912-07-19 | 1912-07-19 | Improvements in the Production of Nitrogen from Products of Combustion. |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB191216855A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2740693A (en) * | 1950-03-08 | 1956-04-03 | Edmund S Pomykala | Separation and purification of nitrogen and other insoluble gases from flue gases |
FR2971169A1 (en) * | 2011-09-23 | 2012-08-10 | Air Liquide | Oxy-combustion and purification of residual gas obtained from combustion and oxy-combustion, by partially removing oxygen contained in residual gas in presence of catalytic bed and providing oxygen-depleted residual gas to desiccation unit |
-
1912
- 1912-07-19 GB GB191216855D patent/GB191216855A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2740693A (en) * | 1950-03-08 | 1956-04-03 | Edmund S Pomykala | Separation and purification of nitrogen and other insoluble gases from flue gases |
FR2971169A1 (en) * | 2011-09-23 | 2012-08-10 | Air Liquide | Oxy-combustion and purification of residual gas obtained from combustion and oxy-combustion, by partially removing oxygen contained in residual gas in presence of catalytic bed and providing oxygen-depleted residual gas to desiccation unit |
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