GB330025A - Improved process and apparatus for the cracking or the destructive hydrogenation of oils, or suspensions of coal in oil - Google Patents
Improved process and apparatus for the cracking or the destructive hydrogenation of oils, or suspensions of coal in oilInfo
- Publication number
- GB330025A GB330025A GB856029A GB856029A GB330025A GB 330025 A GB330025 A GB 330025A GB 856029 A GB856029 A GB 856029A GB 856029 A GB856029 A GB 856029A GB 330025 A GB330025 A GB 330025A
- Authority
- GB
- United Kingdom
- Prior art keywords
- pipe
- tubes
- cracking
- hydrogen
- oils
- 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
- 238000005336 cracking Methods 0.000 title abstract 4
- 230000001066 destructive effect Effects 0.000 title abstract 4
- 239000003921 oil Substances 0.000 title abstract 4
- 238000005984 hydrogenation reaction Methods 0.000 title abstract 3
- 239000003245 coal Substances 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- 239000000725 suspension Substances 0.000 title abstract 2
- 239000007789 gas Substances 0.000 abstract 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 4
- 239000001257 hydrogen Substances 0.000 abstract 4
- 229910052739 hydrogen Inorganic materials 0.000 abstract 4
- 239000000463 material Substances 0.000 abstract 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 2
- 229910000851 Alloy steel Inorganic materials 0.000 abstract 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 abstract 1
- 229910001209 Low-carbon steel Inorganic materials 0.000 abstract 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 abstract 1
- 229910000831 Steel Inorganic materials 0.000 abstract 1
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 1
- 239000001569 carbon dioxide Substances 0.000 abstract 1
- 229910052804 chromium Inorganic materials 0.000 abstract 1
- 239000011651 chromium Substances 0.000 abstract 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 229910052742 iron Inorganic materials 0.000 abstract 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000003863 metallic catalyst Substances 0.000 abstract 1
- 229910052750 molybdenum Inorganic materials 0.000 abstract 1
- 239000011733 molybdenum Substances 0.000 abstract 1
- 229910052759 nickel Inorganic materials 0.000 abstract 1
- 229910052757 nitrogen Inorganic materials 0.000 abstract 1
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 abstract 1
- 238000010926 purge Methods 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000010959 steel Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
Classifications
-
- 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
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/06—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
- C10G1/065—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation in the presence of a solvent
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
330,025. Hunter, T. G., and Imperial Chemical Industries, Ltd. March 16, 1929. Hydrogenation, destructive; hydrocarbons, cracking.-In a process for the destructive hydro. genation or cracking of oils or suspensions of coal in oils with or without a catalyst, the material is caused to pass,by means of the injector action of a gas, through heated vertical tubes and is projected against a baffle which causes it to fall back in the form of a parabolic curtain, through which the gases and vapours must pass. The pressures employed range from one to 300 atmospheres or more, hydrogen at high pressure, being used for destructive hydrogenation, and carbon dioxide or nitrogen for the injector action during cracking. In the apparatus shown, fresh material is furnished by the supply pipe 14 of a pump 7 and is forced up tubes 2 by hydrogen or other gas under pressure, entering by a pipe 8, which by injector action carries the material to be treated up the tubes 2. Situated above the tubes 2 is a baffle plate having a concave base 4<a> and a central conical portion 4 which causes the material impinging thereon to fall as a parabolic curtain and be returned to the pipe 14 by a pipe 6. Hydrogen may enter the upper part 3 of the apparatus by a pipe 8<a>. Heated gases are sup-, plied to the chamber by a pipe 9 at a pressure approximately the same as that of the hydrogen or other gas. Vapours and gases-pass off by a pipe 11 to a catchpot 12, any separated liquid being returned by a pipe 13 to the supply pipe 14. A valved purge 15 for solid matter is provided at the lower part of the chamber 3. The temperatures employed vary from 400‹ to 500‹ C., and the tubes and other pressure resisting parts may be constructed of mild steel having an iron sheath or of an alloy steel such as a nickel, chromium, molybdenum steel. The catalyst may consists of ferric oxide in a fine state of division or the tubes 2 may be coated with a metallic catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB856029A GB330025A (en) | 1929-03-16 | 1929-03-16 | Improved process and apparatus for the cracking or the destructive hydrogenation of oils, or suspensions of coal in oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB856029A GB330025A (en) | 1929-03-16 | 1929-03-16 | Improved process and apparatus for the cracking or the destructive hydrogenation of oils, or suspensions of coal in oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB330025A true GB330025A (en) | 1930-06-05 |
Family
ID=9854804
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB856029A Expired GB330025A (en) | 1929-03-16 | 1929-03-16 | Improved process and apparatus for the cracking or the destructive hydrogenation of oils, or suspensions of coal in oil |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB330025A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2439811A (en) * | 1941-05-21 | 1948-04-20 | Kellogg M W Co | Catalytic conversion of hydrocarbons |
| US2968610A (en) * | 1958-09-22 | 1961-01-17 | Socony Mobil Oil Co Inc | Recycle catalytic conversion of liquid reactants |
| US4390503A (en) | 1981-05-13 | 1983-06-28 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
| WO1991009920A1 (en) * | 1989-12-27 | 1991-07-11 | Gfk Gesellschaft Für Kohleverflüssigung Mbh | Process for hydrogenating a carbonaceous material, in particular coal and/or heavy oil |
| US5045176A (en) * | 1981-05-13 | 1991-09-03 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
-
1929
- 1929-03-16 GB GB856029A patent/GB330025A/en not_active Expired
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2439811A (en) * | 1941-05-21 | 1948-04-20 | Kellogg M W Co | Catalytic conversion of hydrocarbons |
| US2968610A (en) * | 1958-09-22 | 1961-01-17 | Socony Mobil Oil Co Inc | Recycle catalytic conversion of liquid reactants |
| US4390503A (en) | 1981-05-13 | 1983-06-28 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
| US5045176A (en) * | 1981-05-13 | 1991-09-03 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
| WO1991009920A1 (en) * | 1989-12-27 | 1991-07-11 | Gfk Gesellschaft Für Kohleverflüssigung Mbh | Process for hydrogenating a carbonaceous material, in particular coal and/or heavy oil |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| GB330025A (en) | Improved process and apparatus for the cracking or the destructive hydrogenation of oils, or suspensions of coal in oil | |
| GB983798A (en) | Treating coke | |
| GB255159A (en) | Improvements in or relating to the cracking and hydrogenation of hydrocarbon oils | |
| US3234300A (en) | Production of acetylene by the partial combustion process | |
| US1656813A (en) | Producing gasoline from natural gases | |
| US1969422A (en) | Treatment of coals, tars, mineral oils, and the like | |
| US2398012A (en) | Electrode for electron discharge devices | |
| US2215950A (en) | Chemical process | |
| US2089616A (en) | Process for the hydrogenation and cracking of hydrocarbon oils | |
| US1250879A (en) | Method of and apparatus for fractionating hydrocarbons. | |
| US1928784A (en) | Process of manufacturing oil gas | |
| GB360404A (en) | Improvements relating to the production of volatilisable products from coal and oil and to the production of gas by heat treatment of carbonaceous materials | |
| GB220732A (en) | Improvements relating to the cracking of hydrocarbon oils and the treatment of solidcarbonaceous substances | |
| GB366494A (en) | Improvements in the conversion of methane into liquid hydrocarbons | |
| GB191124905A (en) | Improved Process of Manufacturing Liquefiable Hydro-carbon Gases. | |
| US2904497A (en) | Process for the high temperature reaction of hydrocarbons | |
| GB263381A (en) | Process and apparatus for the purification and hydrogenation of liquid hydrocarbons | |
| US1553300A (en) | Apparatus for cracking or converting oils | |
| 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 | |
| US1781935A (en) | Production of hydrogen | |
| GB230339A (en) | Improvements in apparatus for cracking hydrocarbons | |
| GB191317121A (en) | Improvements in the Conversion of Heavy Hydrocarbons into Lighter Hydrocarbons. | |
| US1829213A (en) | Process of treating hydrocarbons | |
| GB780813A (en) | A method of manufacturing acetylene from hydrocarbons | |
| GB293231A (en) | Improved method of and apparatus for coking hydrocarbon oils |