DEP0018928DA - Process for splitting petroleum, tar and coal tar - Google Patents
Process for splitting petroleum, tar and coal tarInfo
- Publication number
- DEP0018928DA DEP0018928DA DEP0018928DA DE P0018928D A DEP0018928D A DE P0018928DA DE P0018928D A DEP0018928D A DE P0018928DA
- Authority
- DE
- Germany
- Prior art keywords
- tar
- coal
- splitting
- petroleum
- vapors
- 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
- 238000000034 method Methods 0.000 title description 3
- 239000011269 tar Substances 0.000 title description 2
- 239000011280 coal tar Substances 0.000 title 1
- 239000003208 petroleum Substances 0.000 title 1
- 239000003054 catalyst Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 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
- 239000007789 gas Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000011294 coal tar pitch Substances 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000011271 tar pitch Substances 0.000 description 1
Description
rietr. :Akt.Z. p-4&^ /1τΓ9 Antrag auf Patenterteilung für Diplom Ingenieur Roman Schestopal8 Gundelsheimm ,Jagdhaus.rietr. : Current time p-4 & ^ / 1τΓ 9 Application for a patent for graduate engineer Roman Schestopal 8 G undelsheim m , Jagdhaus.
/ Verfahren zum Spalten vo a Srd öle a A Teer und J31 ei nkohl en t e er Verfahren zum opalten von Erdolen9Teer und Steinkohlenpech mittels Katalysatoren bei hohen Temperaturen, dadurcti gekennzeichnet9dao als Katalysator .<\ieselgu«f und Natriumchlorid jeder für sich,oder gemischt Anwendung finden. */*/ Method to m columns vo a Srd oils a A tar and J31 ei nkohl en he te method for opalten of Erdolen 9 tar and coal tar pitch by means of catalysts at high temperatures, dadurcti in 9 dao as catalyst. <\ Ieselgu "f and sodium chloride each for can be used individually or mixed. * / *
Das Eohmaterial wird nach dem irmen im Tank 15 in den Spaltraum 1 gepumpt .In diesem wird eine Temperatur von 4oo bis A-^o0 und normalem Drucl· gehalten.The raw material is then pumped into the gap 1 in the tank 15, where a temperature of 400 to A- ^ 0 and normal pressure is maintained.
Der dort aus dem Hohmaterial entstehende Dampf geht durch das im Spaltraum angeordnete Gitter 7 auf welchem der Katalysator liegt. Der \atalysator ist eine Mischung von Kieselgur und Na C1. Hierbei werden die Dämpfe gespalten und es scneidet sich Kohlestoff ab,welcher sich am Soden des Spaltraumes absetzt und sofort durch eine Spezialkratzvorrichtung 12 laufend nach Kammer 4 transportiert wird.The steam produced there from the raw material passes through the grid 7 arranged in the gap space on which the catalyst lies. The analyzer is a mixture of diatomite and Na C1. The vapors are split and carbon is cut off, which is deposited on the bottom of the gap and is immediately transported continuously to chamber 4 by a special scraper device 12.
Aus dieser Kammer kann der Koks periodisch mit Hilfe von Schieber 3 und Deckel 16 ausgestoßen werden.The coke can be ejected periodically from this chamber with the aid of slide 3 and cover 16.
Die Spaltdämpfe steigen in Kamraer 5,wo sie mit Hilfe des Ventilators 8 abgekühlt werden.Die Temperatur auf welche die Spaltdimpfe abgekühlt werden,entspricht? öeweils dem gewünschten Spaltprodukt.The fissure vapors rise into chamber 5, where they are cooled with the aid of the fan 8. The temperature to which the gap vapors are cooled be, corresponds to? depending on the desired cleavage product.
Die bei dieser Temperatur nicht kondensierten Dämpfe und Gase gelangen durch das Hohr 1o in den Wasserkijhler9Wahrend die kondensierten Anteile in den Spaltraum zurückgelangen und, erneut gespalten werden.The vapors and gases that are not condensed at this temperature pass through the Hohr 1o into the water cooler 9, while the condensed fractions return to the gap and are split again.
Die im WasservJciihler sieht kondensierten*Gase werden anschließend mit Schwefelsäure behandelt.Man erhält ein Benzin mit dem spec.Gewicht von o,6oo als Endprodukt.The v in water Jciihler sees condensed * gases are then treated with sulfuric acid behandelt.Man receives a gasoline with the spec.Gewicht of o, 6oo as an end product.
Die iüi Aasserkühler kondensierten Dämpfe ergeben ein Benzin mit einem spec.Gewicht von o,72o und normaler Jictanzahl.The iüi carrion cooler condensed vapors result in a gasoline with a specific weight of o.72o and a normal number of jets.
ä.ian kann aber die Arbeitsbedingungen so einstellen,daß als Endprodukt auch normales Dieselöl und Koks erhalten wird.But the like can adjust the working conditions in such a way that normal diesel oil and coke are also obtained as the end product.
Claims (1)
Family
ID=
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