DE829343C - Process for splitting petroleum, tar and coal tar - Google Patents
Process for splitting petroleum, tar and coal tarInfo
- Publication number
- DE829343C DE829343C DEP18928D DEP0018928D DE829343C DE 829343 C DE829343 C DE 829343C DE P18928 D DEP18928 D DE P18928D DE P0018928 D DEP0018928 D DE P0018928D DE 829343 C DE829343 C DE 829343C
- Authority
- DE
- Germany
- Prior art keywords
- tar
- splitting
- petroleum
- vapors
- coal
- 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
- 239000011280 coal tar Substances 0.000 title 1
- 239000003208 petroleum Substances 0.000 title 1
- 239000011269 tar Substances 0.000 title 1
- 239000003054 catalyst Substances 0.000 claims description 3
- 239000011300 coal pitch Substances 0.000 claims 1
- 239000011301 petroleum pitch Substances 0.000 claims 1
- 239000011271 tar pitch Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 230000004992 fission Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000007017 scission Effects 0.000 description 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Das Rohmaterial wird nach dem Vorwärmen im Tank 15 in den Spaltraum r gepumpt. In diesem wird eine Temperatur von 4oo bis 45o° und normalem Druck gehalten.After being preheated in the tank 15, the raw material is placed in the gap r pumped. In this, a temperature of 400 to 45o ° and normal pressure is maintained.
Der dort aus dem Rohmaterial entstehende Dampf geht durch das im Spaltraum angeordnete Gitter 7, auf welchem der Katalysator liegt.The steam generated there from the raw material passes through the gap arranged grid 7 on which the catalyst lies.
Der Katalysator ist eine Mischung von Kieselgar und Na C t. Hierbei werden die Dämpfe gespalten, und es scheidet sich Kohlestoff ab, welcher sich am Boden des Spaltraumes absetzt und sofort durch eine Spezialkratzvorrichtung 12 laufend nach Kammer 4 transportiert wird.The catalyst is a mixture of kieselgar and Na C t. Here the vapors are split, and carbon is deposited, which is on the The bottom of the gap is deposited and immediately running through a special scraper device 12 is transported to chamber 4.
Aus dieser Kammer 'kann der Koks periodisch mit Hilfe von Schieber 3 und Deckel 16 ausgestoßen werden.From this chamber the coke can periodically with the help of a slide 3 and cover 16 are ejected.
Die Spaltdämpfe steigen in Kammer 5, wo sie mit Hilfe des Ventilators: 8 abgekühlt werden. Die Temperatur, auf welche die .Spaltdämpfe abgekühlt werden, entspricht jeweils dem gewünschten Spaltprodukt.The fission vapors rise into chamber 5, where with the help of the fan they: 8 can be cooled down. The temperature to which the fission vapors are cooled corresponds in each case to the desired cleavage product.
Die bei dieser Temperatur nicht kondensierten Dämpfe und Gase gelangen durch das Rohr to in den Wasserkühler, während die kondensierten Anteile in den Spaltraum zuriickgelangen und erneut gespalten werden.The vapors and gases that have not condensed at this temperature will get there through the pipe to into the water cooler, while the condensed fractions in the Cleft space can be returned and cleaved again.
Die im Wasserkühler kondensierten Dämpfe und Gase werden anschließend mit Schwefelsäure behandelt. h-Ian erhält ein Benzin reit dem spez. Ge--,vicht von o,6oo als Endprodukt.The vapors and gases condensed in the water cooler are then treated with sulfuric acid. h-Ian receives a gasoline ride the spec. Ge -, weighted by o, 6oo as the end product.
Die im Wasserkühler kondensierten Dämpfe ergeben ein Benzin mit einem spez. Gewicht von 0,720 und normaler Oktanzahl.The vapors condensed in the water cooler result in a gasoline with a spec. Weight of 0.720 and normal octane number.
Man kann aber die Arbeitsbedingungen so einstellen, daß als Endprodukt auch normales Dieselöl und Koks erhalten wird.But you can adjust the working conditions so that as the end product normal diesel oil and coke is also obtained.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP18928D DE829343C (en) | 1948-10-21 | 1948-10-21 | Process for splitting petroleum, tar and coal tar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP18928D DE829343C (en) | 1948-10-21 | 1948-10-21 | Process for splitting petroleum, tar and coal tar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE829343C true DE829343C (en) | 1952-01-24 |
Family
ID=7367241
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DEP18928D Expired DE829343C (en) | 1948-10-21 | 1948-10-21 | Process for splitting petroleum, tar and coal tar |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE829343C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1991004308A1 (en) * | 1989-09-13 | 1991-04-04 | Antero Ollila | A method for the thermal cracking of hydrocarbon oils and other liquid/gas reactions |
-
1948
- 1948-10-21 DE DEP18928D patent/DE829343C/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1991004308A1 (en) * | 1989-09-13 | 1991-04-04 | Antero Ollila | A method for the thermal cracking of hydrocarbon oils and other liquid/gas reactions |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE829343C (en) | Process for splitting petroleum, tar and coal tar | |
| DEP0018928DA (en) | Process for splitting petroleum, tar and coal tar | |
| DE535473C (en) | Process for converting high-boiling to low-boiling hydrocarbons | |
| SU121385A1 (en) | Coal Flotation Reagent | |
| DE715624C (en) | Process for the production of non-resinous motor fuels | |
| DE761509C (en) | Process for the production of knock-proof petrol | |
| DE405974C (en) | Process for splitting hydrocarbons | |
| DE726519C (en) | Process for the splitting hydrogenation of high-boiling hydrocarbon oils | |
| DE568544C (en) | Process for obtaining valuable, especially low-boiling, hydrocarbons | |
| AT107594B (en) | Process for splitting hydrocarbons. | |
| DE737024C (en) | Process for splitting the gaseous and steamy carbonization products that arise during carbonization | |
| DE582717C (en) | Process for the extraction of oils | |
| DE663374C (en) | Process for the production of hydrocarbons, especially low-boiling ones, from coals, tars, mineral oils, their distillation and extraction products or residues | |
| DE397860C (en) | Process for the production of gaseous and liquid olefins | |
| DE1032025B (en) | Motor petrol | |
| AT122515B (en) | Process for the production of liquid products from coal or carbonaceous material. | |
| DE678808C (en) | Process for the production of hydrocarbon oils from coals, tars, mineral oils or their distillation or extraction products or residues | |
| DE570558C (en) | Process for processing high molecular weight organic substances to substances of low molecular size | |
| DE366542C (en) | Process for the production of pulpy-liquid fuel mixtures from carbonaceous substances | |
| DE540088C (en) | Process for the splitting of hydrocarbon oils | |
| DE807418C (en) | Process for processing asphalt and resinous mineral oils, tars or their high-boiling fractions | |
| DE847001C (en) | Process for the production of gaseous, unsaturated hydrocarbons, in particular of ethylene, and of aromatic hydrocarbons | |
| AT101325B (en) | Process for the distillation of liquids which are emulsions and have a tendency to bubble and foam, in particular tars. | |
| DE844738C (en) | Process for the decomposition of mixtures of isobutyl and methyl alcohol | |
| DE675409C (en) | Process for the catalytic pressure hydrogenation of liquid carbonaceous substances |