DE421909C - Process for cleaning oils - Google Patents

Process for cleaning oils

Info

Publication number
DE421909C
DE421909C DEH95483D DEH0095483D DE421909C DE 421909 C DE421909 C DE 421909C DE H95483 D DEH95483 D DE H95483D DE H0095483 D DEH0095483 D DE H0095483D DE 421909 C DE421909 C DE 421909C
Authority
DE
Germany
Prior art keywords
oils
pressure
heated
atm
cleaning 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
Application number
DEH95483D
Other languages
German (de)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FRITZ HOFMANN DR
MANFRED DUNKEL DR ING
Original Assignee
FRITZ HOFMANN DR
MANFRED DUNKEL DR ING
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by FRITZ HOFMANN DR, MANFRED DUNKEL DR ING filed Critical FRITZ HOFMANN DR
Priority to DEH95483D priority Critical patent/DE421909C/en
Application granted granted Critical
Publication of DE421909C publication Critical patent/DE421909C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G31/00Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/06Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment

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)
  • Cleaning By Liquid Or Steam (AREA)

Description

Verfahren zur Reinigung von Ölen. Zur Reinigung von Handelsbenzolen, Erdölprodukten, Braunkohlen- und Steinkohlenurteeren ist bisher vorzugsweise Schwefelsäure oder Aluminiumchlorid verwendet worden. Hierbei gehen die Reinigungsmittel fast völlig verloren, die entfernten Verunreinigungen bilden unverwertbare saure Produkte, die sogenannten »Brandharze«.Process for cleaning oils. For cleaning commercial benzenes, For petroleum products, lignite and hard coal tares, sulfuric acid has so far been preferred or aluminum chloride has been used. Here the detergents almost go completely lost, the removed impurities form unusable acidic products, the so-called "fire resins".

Speziell zur Entschwefelung ist auch vorgeschlagen worden, die Öle mit Metalloxyden oder Hydroxyden unter dem Druck eines Gases, am besten Wasserstoff, zu behandeln (Patentschrift 29o563) oder die Öle mit Metallsulfiden in Reaktion zu bringen, die die Neigung haben, Schwefel aufzunehmen (Patentschrift 380059).The oils have also been proposed specifically for desulphurization with metal oxides or hydroxides under the pressure of a gas, preferably hydrogen, to treat (patent specification 29o563) or the oils with metal sulfides in reaction to bring that have a tendency to absorb sulfur (patent specification 380059).

Es war nicht bekannt, daß es gelingt, Benzole usw. weitgehend zu reinigen, wenn sie ohne Zusatz eines Katalysators mit oder ohne Druck eines Gases, am zweckmäßigsten Luft, kurze Zeit auf höhere Temperatur erhitzt werden. Durch dieses Verfahren wird Polymerisation und Kondensation der ungesättigten Bestandteile bewirkt. Schwefelkohlenstoff und Blausäure werden zerstört.It was not known that it was possible to largely purify benzene etc. when they are most expedient without the addition of a catalyst with or without the pressure of a gas Air, heated to a higher temperature for a short time. Through this procedure, Polymerization and condensation of the unsaturated components causes. Carbon disulfide and hydrogen cyanide are destroyed.

Nach dem Abdestillieren von de;i polyinerisierten Produkten ist der Waschverlust auf ein Drittel bis ein Viertel herabgedrückt. Von allen ungesättigten Teilen werden nur die Thiophene schwieriger angegriffen. Es ist aber zu bemerken, daß diese Verbindungen licht- und luftbeständig sind und nicht verharzen.After the de; i polymerized products have been distilled off, the Wash loss depressed to a third to a quarter. Of all unsaturated Parts only the thiophenes are more difficult to attack. But it should be noted that these compounds are light and air-resistant and do not resinify.

Durch Gegenwart von Wasser, Metallen, \letalh-erbindungen, Säuren und. Alkalien kann man die Art der Polymerisate weitgehend verändern. Von den Polymerisationsrückständen läßt sich durch Destillation unter einer der üblichen Bedingungen ein Teil in flüssiger Form gewinnen. Der Rest ist ein neutrales, stets verwertbares Pech.Due to the presence of water, metals, \ lethal compounds, acids and. Alkalis can largely change the nature of the polymers. From the polymerization residues a part can be converted into liquid by distillation under one of the usual conditions Gain shape. The rest is a neutral, always usable bad luck.

Beispiele. i. Rohbenzol mit einem Waschverlust von .4,65 Prozent wird 2 Stunden unter zo Atm. Druck auf i5o° erhitzt. Das tiefbraune Produkt wird destilliert. Das Destillat hat nur einen Waschverlust von 2,2 Prozent. Die verbleibenden Verunreinigungen Lestehen im wesentlichen au: Thiophen.Examples. i. Crude benzene with a wash loss of .4.65 percent will 2 hours under zo atm. Pressure heated to 150 °. The deep brown product is distilled. The distillate only has a washing loss of 2.2 percent. The remaining impurities Read essentially as follows: thiophene.

2. Dasselbe Rohbenzol wird 2 Stunden unter 75 Atm. Druck auf 2oo° erwärmt. Das gereinigte Öl hat einen Waschverlust von 1,6 Prozent, .der nur aus Thiophen besteht.2. The same crude benzene is under 75 atm for 2 hours. Pressure to 2oo ° warmed up. The cleaned oil has a washing loss of 1.6 percent, the only off Thiophene is made up.

3. Das Rohbenzol wird durch ein auf 300 bis d.00° geheiztes Rohr geleitet. Der Waschverlust im Kondensat ist auf etwa die Hälfte gesunken.3. The crude benzene is passed through a pipe heated to 300 to d.00 °. The washing loss in the condensate has dropped to about half.

In allen Fällen ist kein Schwefelkohlenstoff mehr nachzuweisen. Die so gereinigten Öle zeichnen sich durch größte Beständigkeit gegen Licht und Luft aus und bedürfen in den meisten Fällen der Schwefelsäurewäsche nicht mehr.In all cases no more carbon disulfide can be detected. the Oils cleaned in this way are extremely resistant to light and air and in most cases no longer require sulfuric acid washing.

Claims (2)

PATENTANSPRÜCHE: i. Verfahren zur Herstellung von licht- und haftbeständigen Ölen aus Rohölen, wie Handelsbenzolen, Erdölen, Braunkohlen- und Steinkohlenurteeren, dadurch gekennzeichnet, daß man diese bei Drucken unter ioo .Atm. oder ohne Druck erhitzt. PATENT CLAIMS: i. Process for the production of lightfast and adhesive resistant Oils from crude oils, such as commercial benzenes, petroleum, lignite and Coal tares, characterized in that they are printed under ioo .Atm. or heated without pressure. 2. Ausführungsform nach Anspruch i; gekennzeichnet durch Arbeiten in Gegenwart von Katalysatoren oder katalytisch wirkenden Gefäßwänden zur Verbesserung der Qualität der entstehenden Rückstände.2. Embodiment according to claim i; marked by working in the presence of catalysts or catalytically active vessel walls to improve the quality of the resulting residues.
DEH95483D 1923-12-12 1923-12-12 Process for cleaning oils Expired DE421909C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEH95483D DE421909C (en) 1923-12-12 1923-12-12 Process for cleaning oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEH95483D DE421909C (en) 1923-12-12 1923-12-12 Process for cleaning oils

Publications (1)

Publication Number Publication Date
DE421909C true DE421909C (en) 1925-11-20

Family

ID=7167298

Family Applications (1)

Application Number Title Priority Date Filing Date
DEH95483D Expired DE421909C (en) 1923-12-12 1923-12-12 Process for cleaning oils

Country Status (1)

Country Link
DE (1) DE421909C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE844440C (en) * 1949-11-29 1952-07-21 Scholven Chemie Ag Process for the catalytic pressure refining of benzene hydrocarbons
DE894397C (en) * 1942-10-11 1953-10-26 Koppers Gmbh Heinrich Process for the production of engine benzene from crude benzene
US2764524A (en) * 1951-09-18 1956-09-25 Huels Chemische Werke Ag Process for the recovery of light oil from cracking gases

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE894397C (en) * 1942-10-11 1953-10-26 Koppers Gmbh Heinrich Process for the production of engine benzene from crude benzene
DE844440C (en) * 1949-11-29 1952-07-21 Scholven Chemie Ag Process for the catalytic pressure refining of benzene hydrocarbons
US2764524A (en) * 1951-09-18 1956-09-25 Huels Chemische Werke Ag Process for the recovery of light oil from cracking gases

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