DE398322C - Process for the production of carbon oxysulfide and carbon disulfide - Google Patents

Process for the production of carbon oxysulfide and carbon disulfide

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Publication number
DE398322C
DE398322C DEB107684D DEB0107684D DE398322C DE 398322 C DE398322 C DE 398322C DE B107684 D DEB107684 D DE B107684D DE B0107684 D DEB0107684 D DE B0107684D DE 398322 C DE398322 C DE 398322C
Authority
DE
Germany
Prior art keywords
carbon
sulfur
oxysulfide
disulfide
production
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
DEB107684D
Other languages
German (de)
Inventor
Dr Alwin Mittasch
Dr Ernst Willfroth
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.)
BASF SE
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Priority to DEB107684D priority Critical patent/DE398322C/en
Application granted granted Critical
Publication of DE398322C publication Critical patent/DE398322C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/70Compounds containing carbon and sulfur, e.g. thiophosgene

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Catalysts (AREA)

Description

Verfahren zur Herstellung von Kohlenoxysulfid und Schwefelkohlenstoff. Von den verschiedenen Bildungsmöglichkeiten des Kohlenoxysulfids hat bisher keine eine technische Anwendung gefunden; entweder waren die Ausbeuten sehr gering oder die Ausgangsstoffe nur schwierig zu beschaffen. Andererseits wird Schwefelkohlenstoff technisch ausschließlich durch Einwirkung von Schwefeldampf auf glühende Kohle erzeugt.Process for the production of carbon oxysulfide and carbon disulfide. So far none of the various ways in which carbon oxysulphide can be formed found a technical application; either the yields were very low or the raw materials are difficult to obtain. On the other hand, it becomes carbon disulfide technically produced exclusively by the action of sulfur vapor on glowing coal.

Es wurde nun gefunden, daß man Kohlenoxvsulfid und Schwefelkohlenstoff aus Kohlenoxyd und Schwefel bei Gegenwart geeigneter Kontaktsubstanzen, wie z. B. Eisen, Holzkohle, aktiver Kohle u. dgl., leicht erhalten kann, wenn man bei höheren Temperaturen, insbesondere solchen zwischen etwa 4oo bis 6oo° C arbeitet. Statt des Schwefels kann man auch Schwefel liefernde Verbindungen, wie z. B. Schwefeldioxyd, verwenden.It has now been found that carbon oxysulfide and carbon disulfide can be used from carbon oxide and sulfur in the presence of suitable contact substances, such as. B. Iron, charcoal, active charcoal and the like, can easily be obtained if one at higher Temperatures, especially those between about 400 to 600 ° C., works. Instead of the sulfur can also be sulfur-yielding compounds, such as. B. sulfur dioxide, use.

Beispiel i.Example i.

Kohlenoxyd wird über oder durch nahe auf die Verdampfungstemperatur erhitzten Schwefel geleitet und das Kohlenoxyd-Schwefeldampfgemisch der Einwirkung eines aus Eisen bzw. Schwefeleisen bestehenden, auf .450° erhitzten Katalysators ausgesetzt. Es wird dabei eine weitgehende bis völlige @"erainigung des Schwefels mit dem Kohlenoxyd zu Kohlenoxysulfid und Schwefelkohlenstoff erreicht; als Nebenprodukt entsteht Kohlendioxyd. Das erhaltene Gasgemisch hat etwa folgende Zusammensetzung: io bis 15 Volumprozent Schwefelkohlenstoff, 65 bis 7o Volumprozent Kohlenoxy sulfid, 2o Volumprozent Kohlensäure.Carbon dioxide becomes above or through close to the vaporization temperature heated sulfur passed and the carbon oxide-sulfur vapor mixture of the action a catalyst made of iron or iron sulfur and heated to .450 ° exposed. There is an extensive to complete recovery of the sulfur reached with the carbon monoxide to carbon oxysulfide and carbon disulfide; as a by-product carbon dioxide is produced. The gas mixture obtained has approximately the following composition: 10 to 15 percent by volume carbon disulfide, 65 to 7o percent by volume carbon oxy sulfide, 2o volume percent carbonic acid.

Beispiel a.Example a.

Kohlenoxyd und Schwefeldioxyd werden im Verhältnis von etwa 3 Volumen Kohlenoxyd auf i Volumen Schwefeldioxyd über auf 4.0o bis 5oo° erhitzte Holzkohle geleitet; es entstehen in guter Ausbeute Kohlenoxysulfid und Schwefelkohlenstoff. Das erhaltene Gasgemisch eist aber reicher an Kohlendioxyd als in Beispiel i.Carbon dioxide and sulfur dioxide become in the proportion of about 3 volumes Carbon dioxide to one volume of sulfur dioxide over charcoal heated to 4.0o to 500o directed; carbon oxysulfide and carbon disulfide are formed in good yield. However, the gas mixture obtained is richer in carbon dioxide than in Example i.

Das aus Kohlenoxysulfid, Schwefelkohlenstoff und Kohlendioxyd bestehende Gasgemisch kann vielfach unmittelbar verwendet werden, oder man kann es durch fraktionierte Kondensation oder mittels Adsorption an geeigneten aktiven Stoffen, z. B. mittels aktiver Kohle, ohne Schwierigkeit in seine Bestandteile zerlegen oder von Kohlendioxyd befreien.That consisting of carbon oxysulfide, carbon disulfide and carbon dioxide Gas mixture can often be used directly, or it can be fractionated Condensation or by means of adsorption on suitable active substances, e.g. B. by means of active charcoal, decomposing into its constituent parts without difficulty, or of carbon dioxide to free.

Claims (1)

PATENTANSPRUCH: herfahren zur Gewinnung von Kohlenoxvsulfid und Schwefelkohlenstoff aus Kohlenoxyd und Schwefel bzw. Schwefel abscheidenden Verbindungen, dadurch gekennzeichnet, daß man Gemische dieser der Einwirkung eines geeigneten Katalysators bei erhöhter Temperatur aussetzt. PATENT CLAIM: a process for obtaining carbon oxysulphide and carbon disulfide from carbon oxide and sulfur or sulfur-separating compounds, characterized in that mixtures of these are exposed to the action of a suitable catalyst at elevated temperature.
DEB107684D 1922-12-17 1922-12-17 Process for the production of carbon oxysulfide and carbon disulfide Expired DE398322C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEB107684D DE398322C (en) 1922-12-17 1922-12-17 Process for the production of carbon oxysulfide and carbon disulfide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEB107684D DE398322C (en) 1922-12-17 1922-12-17 Process for the production of carbon oxysulfide and carbon disulfide

Publications (1)

Publication Number Publication Date
DE398322C true DE398322C (en) 1924-07-07

Family

ID=6991988

Family Applications (1)

Application Number Title Priority Date Filing Date
DEB107684D Expired DE398322C (en) 1922-12-17 1922-12-17 Process for the production of carbon oxysulfide and carbon disulfide

Country Status (1)

Country Link
DE (1) DE398322C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2935380A (en) * 1953-05-01 1960-05-03 Pan American Petroleum Corp Process for preparation of carbon disulfide and carbonyl sulfide
DE1136316B (en) * 1959-07-22 1962-09-13 Socony Mobil Oil Co Inc Process for the production of carbonyl sulfide
WO2004089824A1 (en) * 2003-04-10 2004-10-21 Winston David Fink The manufacture of carbonyl sulphide

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2935380A (en) * 1953-05-01 1960-05-03 Pan American Petroleum Corp Process for preparation of carbon disulfide and carbonyl sulfide
DE1136316B (en) * 1959-07-22 1962-09-13 Socony Mobil Oil Co Inc Process for the production of carbonyl sulfide
WO2004089824A1 (en) * 2003-04-10 2004-10-21 Winston David Fink The manufacture of carbonyl sulphide

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