GB586027A - Improved method of carrying out cracking, pyrolysis, and partial oxidation reactions - Google Patents
Improved method of carrying out cracking, pyrolysis, and partial oxidation reactionsInfo
- Publication number
- GB586027A GB586027A GB6479/44A GB647944A GB586027A GB 586027 A GB586027 A GB 586027A GB 6479/44 A GB6479/44 A GB 6479/44A GB 647944 A GB647944 A GB 647944A GB 586027 A GB586027 A GB 586027A
- Authority
- GB
- United Kingdom
- Prior art keywords
- combustion
- submerged
- hydrogen
- pyrolysis
- water
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/76—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
- C07C2/78—Processes with partial combustion
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/42—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor
- C07C5/48—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with oxygen as an acceptor
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
- C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
- C10G9/38—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours produced by partial combustion of the material to be cracked or by combustion of another hydrocarbon
-
- 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
Abstract
Cracking, pyrolysis, and partial oxidation reactions of organic substances are effected by partial combustion of organic substances, in the presence of insufficient oxygen for complete combustion, in a submerged-combustion burner submerged in an inorganic liquid which is inert under the conditions. The said liquid may be water, one or more molten salts or molten metal. Hydrocarbons such as methane, ethane or propane may be converted to acetylene, ethylene or carbon black. A fuel such as hydrogen or carbon monoxide-containing gas may be added to the reaction mixture. The reaction conditions may be controlled by varying the proportions in the mixture by preheating or adding an inert gas. The method is also applicable to the production of hydrogen, carbon monoxide mixtures. A catalyst, as vapour or powdered solid, may be supplied to the combustion zone or solid catalyst located partly or wholly in said zone. Olefins, obtained for example by pyrolysis of paraffins, may be oxidised to oxides, hydrocarbons or alcohols to aldehydes, acids or anhydrides. Petroleum oils or products of their distillation, cracking or reforming, coal tar products, and carbonaceous materials, such as coal in finely divided form, may also be treated. Natural gas may be converted by means of air or air enriched with oxygen into gas of lower calorific value for public supply. The heat generated may be utilized for evaporating the liquid which may be used in a motive power engine or for steam generation. In examples, methane or ethylene admixed with hydrogen and preheated to 900 or 800 DEG C. is fed with a deficiency of oxygen to a submerged-combustion burner beneath the surface of water. The gases remain at the high temperature for .005 sec. before quenching by the water, and contain acetylene.ALSO:Cracking, pyrolysis, and partial oxidation reactions of organic substances are effected by partial combustion of organic substances, in the presence of insufficient oxygen for complete combustion, in a submerged-combustion burner submerged in an inorganic liquid which is inert under the conditions. The said liquid may be water, one or more molten salts or molten metal. Hydrocarbons such as methane, ethane or propane may be converted to acetylene, ethylene or carbon black. A fuel such as hydrogen or carbon monoxide-containing gas may be added to the reaction mixture. The reaction conditions may be controlled by varying the proportions in the mixture, by preheating or adding an inert gas. The method is also applicable to the production of hydrogen, carbon monoxide mixtures. A catalyst, as vapour or powdered solid, may be supplied to the combustion zone or solid catalyst located partly or wholly in said zone. Olefins, obtained for example by pyrolysis of paraffins, may be oxidized to oxides, hydrocarbons or alcohols to aldehydes, acids or anhydrides. Petroleum oils or products of their distillation, cracking or reforming, coal tar products, and carbonaceous materials, such as coal in finely divided form, may also be treated. Natural gas may be converted by means of air or air enriched with oxygen into gas of lower calorific value for public supply. The heat generated may be utilized for evaporating the liquid which may be used in a motive power engine or for steam generation. In examples, methane or ethylene admixed with hydrogen and preheated to 900 or 800 DEG C. is fed with a deficiency of oxygen to a submerged-combustion burner beneath the surface of water. The gases remain at the high temperature for .005 sec. before quenching by the water, and contain acetylene.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB6479/44A GB586027A (en) | 1944-04-06 | 1944-04-06 | Improved method of carrying out cracking, pyrolysis, and partial oxidation reactions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB6479/44A GB586027A (en) | 1944-04-06 | 1944-04-06 | Improved method of carrying out cracking, pyrolysis, and partial oxidation reactions |
Publications (1)
Publication Number | Publication Date |
---|---|
GB586027A true GB586027A (en) | 1947-03-05 |
Family
ID=9815233
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB6479/44A Expired GB586027A (en) | 1944-04-06 | 1944-04-06 | Improved method of carrying out cracking, pyrolysis, and partial oxidation reactions |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB586027A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11123705B1 (en) | 2018-10-23 | 2021-09-21 | Sabic Global Technologies B.V. | Method and reactor for conversion of hydrocarbons |
-
1944
- 1944-04-06 GB GB6479/44A patent/GB586027A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11123705B1 (en) | 2018-10-23 | 2021-09-21 | Sabic Global Technologies B.V. | Method and reactor for conversion of hydrocarbons |
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