GB680159A - Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compounds - Google Patents
Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compoundsInfo
- Publication number
- GB680159A GB680159A GB14690/50A GB1469050A GB680159A GB 680159 A GB680159 A GB 680159A GB 14690/50 A GB14690/50 A GB 14690/50A GB 1469050 A GB1469050 A GB 1469050A GB 680159 A GB680159 A GB 680159A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oxygen
- gas
- tower
- returned
- heat exchanger
- 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
- C01B3/36—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 oxygen or mixtures containing oxygen as gasifying agents
-
- 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
- C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
<PICT:0680159/III/1> Hydrocarbon residues such as heavy oils, tars, and cracked residues are subjected to incomplete combustion with such an amount of oxygen or gas containing free oxygen as to yield a gas mixture, containing 0.7 to 0.9 volumes of hydrogen per volume of carbon monoxide, which is then used in the catalytic synthesis of oxygen-containing organic compounds. Water vapour, carbon dioxide, and/or methane may be added to the oxygen and the combustion should be carried out under elevated pressure. Fuel oil is pumped to combustion chamber 3 from tank 1 and burns with oxygen passing through line 4 and preheater 5. The hot synthesis gas passes through reaction chamber 6 having heat exchanger 7, heat exchanger 5 and cooler 8 to desulphurization device 9. The gas is then passed to synthesis furnace 10 containing an iron catalyst, and the products are separated in device 11 comprising a condenser, a washer, and an activated carbon absorber. The remaining gases pass to wash tower 12 and are washed with water under pressure, which passes to depressurization vessels 13, 14 and degasifying tower 15 to recover carbon dioxide, which is returned to the combustion chamber, and wash liquid, which is returned to tower 12. Methane, obtained as residual gas from tower 12, may be returned to the combustion chamber, or added to the gas before the synthesis furnace. In alternative arrangements the hot gases at say 1,600 DEG C are passed directly through a gas turbine after reaction 6 or the heat exchanger 7 is replaced by the tube system of a closed circuit turbine system.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1018552X | 1949-06-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB680159A true GB680159A (en) | 1952-10-01 |
Family
ID=7711374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB14690/50A Expired GB680159A (en) | 1949-06-27 | 1950-06-13 | Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compounds |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR1018552A (en) |
GB (1) | GB680159A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1062880B (en) * | 1957-10-10 | 1959-08-06 | Bataafsche Petroleum | Process for the production of methane-rich gases |
DE1102112B (en) * | 1958-07-26 | 1961-03-16 | Basf Ag | Process for the simultaneous production of synthesis gas and of oxygen and nitrogen |
DE1188050B (en) * | 1961-08-17 | 1965-03-04 | Conch Int Methane Ltd | Process for reforming natural gas |
WO2010078871A1 (en) * | 2009-01-07 | 2010-07-15 | Aquarden Technologies Aps | Method and apparatus for production of hydrogen from methanol |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1185548B (en) * | 1959-02-24 | 1965-01-14 | Bernard Taubert | Tool set for inserting and removing flexible watch glasses |
-
1950
- 1950-05-22 FR FR1018552D patent/FR1018552A/en not_active Expired
- 1950-06-13 GB GB14690/50A patent/GB680159A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1062880B (en) * | 1957-10-10 | 1959-08-06 | Bataafsche Petroleum | Process for the production of methane-rich gases |
DE1102112B (en) * | 1958-07-26 | 1961-03-16 | Basf Ag | Process for the simultaneous production of synthesis gas and of oxygen and nitrogen |
DE1188050B (en) * | 1961-08-17 | 1965-03-04 | Conch Int Methane Ltd | Process for reforming natural gas |
WO2010078871A1 (en) * | 2009-01-07 | 2010-07-15 | Aquarden Technologies Aps | Method and apparatus for production of hydrogen from methanol |
US8586003B2 (en) | 2009-01-07 | 2013-11-19 | Aquarden Technologies Aps | Method and apparatus for production of hydrogen from methanol |
Also Published As
Publication number | Publication date |
---|---|
FR1018552A (en) | 1953-01-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1957743A (en) | Production of hydrogen | |
RU2012126748A (en) | METHOD FOR PRODUCING HYDROGEN BASED ON LIQUID HYDROCARBONS, GAS-HYDROCARBON HYDROCARBONS AND / OR OXYGEN-CONTAINING COMPOUNDS, INCLUDING PRODUCED FROM BIOMASS | |
SU802354A1 (en) | Method and device for dry coke quenching and producing hydrogen- and carbonmonoxide-containing gases | |
GB680159A (en) | Process for the utilisation of heavy oils and residues for the production of oxygen-containing organic compounds | |
US2659453A (en) | Separation of acetylene from gaseous mixtures by glycolonitrile | |
GB947923A (en) | Process for the manufacture of olefines | |
GB1354073A (en) | Process and apparatus for the oxygenative cracking of hydrocarbons | |
GB522640A (en) | Improvements in the manufacture of combustible gas and coke from carbonaceous materials | |
GB363344A (en) | Improvements in the manufacture and production of hydrocarbons | |
GB468709A (en) | Improvements in or relating to the circulation of gases in processes for the production of valuable hydrocarbons by heat treatment of compounds of carbon with hydrogenating gases under pressure | |
GB454948A (en) | Method of increasing yield in the catalytic synthesis of aliphatic hydrocarbons | |
GB836909A (en) | Improvements in and relating to the production of unsaturated hydrocarbons and methanol | |
GB851681A (en) | Treatment of hydrocarbons | |
US2007754A (en) | Production of hydrocarbons | |
GB314432A (en) | Treating coke oven gas | |
GB845401A (en) | Improved process for the production of gases containing hydrogen | |
GB528338A (en) | Improvements in the gasification of carbonaceous materials | |
GB328586A (en) | Improvements in the manufacture and production of valuable hydrocarbons and oxygen derivatives of hydrocarbons, in particular those of low boiling point | |
GB323864A (en) | Improved process for obtaining a mixture of hydrogen and carbon monoxide by the decomposition of hydrocarbon gases or vapours in the presence of steam | |
GB349067A (en) | Process of treating saturated hydrocarbons and gaseous mixtures rich in saturated hydrocarbons | |
GB414347A (en) | An improved manufacture of acetylene and organic compounds therefrom | |
GB986090A (en) | Process and apparatus for the catalytic cracking of gaseous or liquid hydrocarbons for the production of high calorific value gases more particularly town gas | |
GB683516A (en) | Process of carrying out exothermic catalytic gas reactions | |
GB267512A (en) | Plant for the manufacture of liquid fuels | |
GB1008409A (en) | Process for cracking gaseous and/or liquid hydrocarbons in periodic operation |