DE695276C - Process for the production of hydrocarbons from solid carbonaceous substances - Google Patents
Process for the production of hydrocarbons from solid carbonaceous substancesInfo
- Publication number
- DE695276C DE695276C DE1935I0060567 DEI0060567D DE695276C DE 695276 C DE695276 C DE 695276C DE 1935I0060567 DE1935I0060567 DE 1935I0060567 DE I0060567 D DEI0060567 D DE I0060567D DE 695276 C DE695276 C DE 695276C
- Authority
- DE
- Germany
- Prior art keywords
- hydrocarbons
- solid carbonaceous
- production
- carbonaceous substances
- substances
- 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
- 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
- C10G1/08—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
- C10G1/086—Characterised by the catalyst used
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)
Description
Verfahren zur Herstellung von Kohlenwasserstoffen aus festen kohlenstoffhaltigen Stoffen Es wurde gefunden, daß man bei der Druckhydrierung fester, kohlenstoffhaltiger Stoffe gute Ausbeuten an wertvollen Verfiüssigungsprodukteu erhält, wenn man als Katalysator Calciumaluminat verwendet. Dieses wird in fein verteilter, trockener oder, suspendierter oder in gelöster Form den zu behandelnden Ausgangssteffen zugegeben. Es kann auch mit anderen z. B. als Katalysatoren, für die Druckhydrierung schon vorgeschla genen Metallverbindungen, z. B. solchen der Metalle der 6. bis B. Gruppe des periodischen Systems, verwendet werden. Als besondersi vorteilhaft hat sich der Zusatz von Nickelverbindungen, wie Nickelcarbonat, erwiesen. Der Katalysator wird den Ausgangsstoffen in einer Menge von o, 5 bis 5 % zugesetzt.Process for the production of hydrocarbons from solid carbonaceous Substances It has been found that pressure hydrogenation produces stronger, more carbon-containing substances Substances good yields of valuable liquefaction products are obtained when Calcium aluminate catalyst used. This will be finely divided, drier or, in suspended or dissolved form, added to the starting materials to be treated. It can also be used with other z. B. as catalysts, for pressure hydrogenation already proposed metal compounds, e.g. B. those of the metals of the 6th to B group of the periodic table. Has proven to be particularly advantageous the addition of nickel compounds, such as nickel carbonate, proved. The catalyst is added to the starting materials in an amount of 0.5 to 5%.
Als feste kohlenstoffhaltige Ausgangsstoffe kommen z. B. Braunkohle, Steinkohle oder Torf in Betracht. Besonders geeignet ist das Verfahren für sauerstoffreiche Kohlen, d. h. für solche, die mindestens 2o% Sauerstoff enthalten. Die Ausgangsstoffe können vor der Verwendung auf mechanische Weise oder durch Säurebehandlung von :der Gangart oder den in Säuren löslichen Bestandteilen befreit werden.As solid carbonaceous starting materials come z. B. lignite, Coal or peat into consideration. The process is particularly suitable for those who are oxygen-rich Coals, d. H. for those that contain at least 20% oxygen. The starting materials can be mechanically or acid treated before use of: the Gangart or the components soluble in acids are freed.
Die mit dem Katalysator versehenen festen kohlens.tofthaltigen Stoffe werden, zweckmäßig nach Vermischen mit einem Schweröl, der Druckhydrierung bei den hierfür üblichen Temperaturen (3oo bis 6oo°) und Drücken (2o bis 5oo at und mehr) unterworfen.The solid carbonaceous substances provided with the catalyst are, advantageously after mixing with a heavy oil, the pressure hydrogenation at the the usual temperatures (3oo to 6oo °) and pressures (2o to 5oo at and more) subject.
Der beanspruchte Katalysator stellt eine wertvolle Bereicherung der Katalysatoren auf dem Gebiet der Druckhydrierung fester kohlenstoffhaltiger Stoffe dar; er ist gut wirksam und hat den Vorzug, daß er billig und leicht zugänglich ist. Beispiel Junge . deutsche Braunkohle mit einem Sauerstoffgehalt von 250/0 wird fein gemahlen, mit 5 % Calciumaluminat gemischt, mit einem aus derselben Kohle stammenden Schweröl im Verhältnis r : t angepastet und zusammen mit Wasserstoff unter einem Druck von Zoo at durch einen gasbeheizter] Vorwärinergeleitet. Von hier aus gelange die-; Reaktionsteilnehmer in ein @erweite aktionsgefäß, in dem eine Tempremtur'O`@ #. ' 44o'aufrechterhalten wird. Die Kohlesu an wird zu 970/0 abgebaut. Das Verflüssigungsprodukt enthält 3% Asphalt und 32% bis 325' übergehende Anteile. Es besitzt ein spezifisches Gewicht von o,985.The claimed catalyst represents a valuable addition to the catalysts in the field of pressure hydrogenation of solid carbonaceous substances; it works well and has the merit of being cheap and easily available. Example boy. German lignite with an oxygen content of 250/0 is finely ground, mixed with 5% calcium aluminate, pasted with a heavy oil from the same coal in the ratio r: t and passed through a gas-heated preheater together with hydrogen under a pressure of Zoo at. From here get the-; Reaction participants in a @wide action vessel in which a tempremtur'O` @ #. '44o' is maintained. The coal consumption is reduced to 970/0. The liquefaction product contains 3% asphalt and 32% to 325 'overflowing parts. It has a specific gravity of 0.985.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1935I0060567 DE695276C (en) | 1935-11-22 | 1935-11-22 | Process for the production of hydrocarbons from solid carbonaceous substances |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1935I0060567 DE695276C (en) | 1935-11-22 | 1935-11-22 | Process for the production of hydrocarbons from solid carbonaceous substances |
Publications (1)
Publication Number | Publication Date |
---|---|
DE695276C true DE695276C (en) | 1940-08-21 |
Family
ID=7195277
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE1935I0060567 Expired DE695276C (en) | 1935-11-22 | 1935-11-22 | Process for the production of hydrocarbons from solid carbonaceous substances |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE695276C (en) |
-
1935
- 1935-11-22 DE DE1935I0060567 patent/DE695276C/en not_active Expired
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