GB714284A - Improvements relating to processes for the treatment of hydrocarbon gases - Google Patents
Improvements relating to processes for the treatment of hydrocarbon gasesInfo
- Publication number
- GB714284A GB714284A GB3062/52A GB306252A GB714284A GB 714284 A GB714284 A GB 714284A GB 3062/52 A GB3062/52 A GB 3062/52A GB 306252 A GB306252 A GB 306252A GB 714284 A GB714284 A GB 714284A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- per cent
- steam
- combustion products
- town
- 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
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/388—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the heat being generated by superheated steam
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
714,284. Reforming hydrocarbon gases. GALOCSY, Z. DE. Feb. 5, 1952 [Feb. 9, 1951], No. 3062/52. Class 55 (2) A two-step process for the treatment of hydrocarbon gases to render them suitable for use as synthesis or hydrogenation gases or as town's gas comprises burning a primary gas in air, oxygenenriched air or oxygen, the combustion products then being used to reform the hydrocarbon gas to obtain a gas containing carbon monoxide and hydrogen. In the first step of the process, a gas, e.g. a part of the gas to be treated or a part of the final reformed gas, is burnt in air or oxygen, the maximum temperature in the combustion vessel being limited to about 2000‹ C. by adding preheated steam or carbon dioxide to the gas to be burnt. In the second step, which may be conducted under pressure, the hot combustion products meet the preheated hydrocarbon gas, the steam, carbon dioxide and any excess oxygen present in the combustion products reacting with the hydrocarbons to give a gas containing carbon monoxide and hydrogen. If the sensible heat of the products is insufficient for the endothermic reforming reactions, the reforming vessel may be externally heated, e.g. electrically. To reduce the reacting temperature, the reforming vessel may be lined with a catalyst or may contain a fluidized bed of catalytic material. When the reformed gas is to be used for synthesis or hydrogenation purposes or for the production of a non-toxic town's gas, it is reacted with steam in the presence of an iron catalyst to remove its carbon monoxide content. For example, to produce a town's gas, a natural gas containing 2 per cent of C0 2 , 4 per cent of N, and 94 per cent of CH 4 was reformed with combustion products made by burning this gas, to give a gas containing 1.9 per cent of C0 2 ; 21.4 per cent of CO ; 64.6 per cent of H 2 and 12.1 per cent of N 2 , After conversion with steam, removal by washing of part of the CO 2 formed and addition of methane to raise the calorific value, the final gas has a composition of 6.0 per cent of C0 2 ; 1 per cent of CO ; 55.6 per cent of H 2 ; 26 per cent of CH 4 and 11.4 per cent of N,.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT714284X | 1951-02-09 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB714284A true GB714284A (en) | 1954-08-25 |
Family
ID=11314805
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB3062/52A Expired GB714284A (en) | 1951-02-09 | 1952-02-05 | Improvements relating to processes for the treatment of hydrocarbon gases |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB714284A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11059720B1 (en) | 2020-01-28 | 2021-07-13 | Saudi Arabian Oil Company | Catalyst carrier for dry reforming processes |
| US11066299B1 (en) | 2020-01-28 | 2021-07-20 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for steam reforming processes |
| WO2021154911A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for bi-reforming processes |
| WO2021154790A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst carrier for steam reforming processes |
| WO2021154795A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst carrier for bi-reforming processes |
| WO2021154793A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst carrier for autothermal reforming processes |
| US11286160B2 (en) | 2020-01-28 | 2022-03-29 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for autothermal reforming processes |
| US11338270B2 (en) | 2020-01-28 | 2022-05-24 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for autothermal reforming processes |
| US11365120B2 (en) | 2020-01-28 | 2022-06-21 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for steam reforming processes |
| US11396006B2 (en) * | 2020-01-28 | 2022-07-26 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for bi-reforming processes |
| US11478777B2 (en) | 2020-01-28 | 2022-10-25 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for dry reforming processes |
| US11498053B2 (en) * | 2020-01-28 | 2022-11-15 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for dry reforming processes |
-
1952
- 1952-02-05 GB GB3062/52A patent/GB714284A/en not_active Expired
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11059720B1 (en) | 2020-01-28 | 2021-07-13 | Saudi Arabian Oil Company | Catalyst carrier for dry reforming processes |
| US11066299B1 (en) | 2020-01-28 | 2021-07-20 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for steam reforming processes |
| WO2021154867A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for steam reforming processes |
| WO2021154788A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst carrier for dry reforming processes |
| WO2021154911A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for bi-reforming processes |
| WO2021154790A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst carrier for steam reforming processes |
| WO2021154795A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst carrier for bi-reforming processes |
| WO2021154793A1 (en) * | 2020-01-28 | 2021-08-05 | Saudi Arabian Oil Company | Catalyst carrier for autothermal reforming processes |
| US11242246B2 (en) | 2020-01-28 | 2022-02-08 | Saudi Arabian Oil Company | Catalyst carrier for autothermal reforming processes |
| US11242245B2 (en) | 2020-01-28 | 2022-02-08 | Saudi Arabian Oil Company | Catalyst carrier for steam reforming processes |
| US11247898B2 (en) | 2020-01-28 | 2022-02-15 | Saudi Arabian Oil Company | Catalyst carrier for bi-reforming processes |
| US11286160B2 (en) | 2020-01-28 | 2022-03-29 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for autothermal reforming processes |
| US11338270B2 (en) | 2020-01-28 | 2022-05-24 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for autothermal reforming processes |
| US11365120B2 (en) | 2020-01-28 | 2022-06-21 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for steam reforming processes |
| US11396006B2 (en) * | 2020-01-28 | 2022-07-26 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for bi-reforming processes |
| US11478777B2 (en) | 2020-01-28 | 2022-10-25 | Saudi Arabian Oil Company | Catalyst compositions having enhanced acidity for dry reforming processes |
| US11498053B2 (en) * | 2020-01-28 | 2022-11-15 | Saudi Arabian Oil Company | Nickel-containing catalyst composition having enhanced acidity for dry reforming processes |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| ES300406A1 (en) | A procedure to form a gas of rich synthesis in hydrogen (Machine-translation by Google Translate, not legally binding) | |
| US1957743A (en) | Production of hydrogen | |
| GB996327A (en) | A method of raising the calorific value of gasification gases | |
| GB1448562A (en) | Process for the production of methane containing gases | |
| GB714284A (en) | Improvements relating to processes for the treatment of hydrocarbon gases | |
| ES8800881A1 (en) | Heat exchange steam-reforming process and reactor. | |
| GB820257A (en) | Process for the production of gases containing methane from hydrocarbons | |
| US1874801A (en) | Process for the decomposition of hydrocarbons | |
| US2135694A (en) | Process for the production of hydrogen | |
| GB1028965A (en) | Preparation of a mixture of gases | |
| US2383715A (en) | Production of gas mixture for methanol | |
| ES313860A1 (en) | A procedure for the production of gases with methane content. (Machine-translation by Google Translate, not legally binding) | |
| JP2001213610A (en) | Method and apparatus for producing gas rich in hydrogen and carbon monoxide | |
| US1903845A (en) | Process of converting natural gas and similar gaseous hydrocarbons into a mixture ofcarbon monoxide and hydrogen in controlled proportions | |
| GB503158A (en) | Manufacture of combustible gases | |
| US2135695A (en) | Process for producing a mixture of nitrogen and hydrogen | |
| GB895038A (en) | Process for the production of gases rich in hydrogen | |
| GB231218A (en) | Improvements in the manufacture and production of hydrogen or of hydrogen-nitrogen mixtures | |
| US3920804A (en) | Hydrogen process | |
| US2013699A (en) | Process for producing hydrogen and carbon black | |
| US2942959A (en) | Process for the production of fuel gas | |
| US1905326A (en) | Process of producing mixtures of carbon monoxide and hydrogen | |
| GB243122A (en) | Improvements in and relating to the production of mixtures of nitrogen and hydrogen from ammonia synthesis | |
| GB356838A (en) | ||
| US2135693A (en) | Process for the production of hydrogen |