AT89800B - Process for the concentration of aqueous acetic acids. - Google Patents

Process for the concentration of aqueous acetic acids.

Info

Publication number
AT89800B
AT89800B AT89800DA AT89800B AT 89800 B AT89800 B AT 89800B AT 89800D A AT89800D A AT 89800DA AT 89800 B AT89800 B AT 89800B
Authority
AT
Austria
Prior art keywords
concentration
acetic acid
aqueous acetic
acetic acids
ether
Prior art date
Application number
Other languages
German (de)
Original Assignee
Farbenfab Vorm Bayer F & Co
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 Farbenfab Vorm Bayer F & Co filed Critical Farbenfab Vorm Bayer F & Co
Application granted granted Critical
Publication of AT89800B publication Critical patent/AT89800B/en

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

  

   <Desc/Clms Page number 1> 
 



  Verfahren, zur Konzentrierung wässeriger Essigsäuren. 



   Ein rationell arbeitendes Verfahren zur Konzentrierung dünner Essigsäuren, wie Gärungsessigsäure,   Abfallessigsäure, isttrotzvielfacher Bemühungen   in dieser Richtung bisher nicht bekannt geworden. 



  Weder das Verfahren von Golodetz (vgl. Chemisches Zentralblatt, 1912, I, S. 69), nach welchem ein   Toluolessigsäuregemisch   destilliert wird, noch die in der "Zeitschrift für angewandte Chemie", 1916, S. 148, angeführten Verfahren liefern technisch befriedigende Resultate. 



   Es wurde nun die'Beobachtung gemacht, dass es in wirtschaftlich sehr günstiger Weise gelingt, derartige dünne Essigsäuren zu konzentrieren. Das Verfahren besteht darin, dass man in Essigsäure Bisulfat, wie es z. B. in der   Salpetersäurefabrikation   abfällt, löst und diese Lösung in einem geeigneten Apparat mit Äther extrahiert. Die Konzentration der Essigsäure in Äther ist im Gleichgewicht mit der mit Bisulfat versetzten   Lösung   mehr als doppelt so gross als ohne Anwendung von Bisulfat, auch nimmt die bisulfathaltige Abfallsäure nur Spuren von Äther auf.   Die Extraktionsgeschwindigkeit   ist ebenfalls gegenüber einer Essigsäure ohne Bisulfat wesentlich vergrössert.

   Man erhält überraschenderweise nach Abdestillieren des Äthers je nach der Konzentration der zu extrahierenden, dünnen Säure   70-bis 80% ige   Essigsäure, welche direkt auf Eisessig fraktioniert wird,   wobe der Vorlauf zur   Extraktion wieder zugeschlagen wird. 



   Beispiel : In einer   15% igen Abfallessigsäure werden 300 < /Natriumbisulfat im   Liter gelöst und diese Lösung in einem geeigneten Gegenstromapparat mit Äther extrahiert. Es gelingt leicht, etwa 95% der Essigsäure als 75% ige Säure aus dem Äther abzuscheiden. 

**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.



   <Desc / Clms Page number 1>
 



  Process for the concentration of aqueous acetic acids.



   A rationally working process for concentrating thin acetic acids, such as fermentation acetic acid or waste acetic acid, has not yet become known, despite numerous efforts in this direction.



  Neither the Golodetz process (see Chemisches Zentralblatt, 1912, I, p. 69), according to which a toluene acetic acid mixture is distilled, nor the processes cited in the "Zeitschrift für angewandte Chemie", 1916, p. 148, give technically satisfactory results .



   The observation has now been made that it is possible to concentrate such thin acetic acids in a very economical way. The method consists in that bisulfate in acetic acid, as it is e.g. B. falls in the nitric acid factory, dissolves and this solution is extracted in a suitable apparatus with ether. The concentration of acetic acid in ether in equilibrium with the solution mixed with bisulphate is more than twice as great as without the use of bisulphate, and the waste acid containing bisulphate only absorbs traces of ether. The extraction speed is also significantly higher than that of acetic acid without bisulfate.

   Surprisingly, after the ether has been distilled off, 70 to 80% acetic acid is obtained, depending on the concentration of the thin acid to be extracted, which is directly fractionated into glacial acetic acid, the first runnings being added again for the extraction.



   Example: 300% sodium bisulfate per liter are dissolved in 15% waste acetic acid and this solution is extracted with ether in a suitable countercurrent apparatus. It is easy to separate about 95% of the acetic acid as 75% acid from the ether.

** WARNING ** End of DESC field may overlap beginning of CLMS **.

 

Claims (1)

PATENT-ANSPRUCH : Verfahren zur Konzentration von wässeriger Essigsäure durch Extraktion, dadurch gekennzeichnet, dass man eine solche Säure, die Bisulfat in Lösung enthält, mit Äther extrahiert. **WARNUNG** Ende CLMS Feld Kannt Anfang DESC uberlappen**. PATENT CLAIM: Process for the concentration of aqueous acetic acid by extraction, characterized in that such an acid, which contains bisulfate in solution, is extracted with ether. ** WARNING ** End of CLMS field may overlap beginning of DESC **.
AT89800D 1916-08-25 1917-06-16 Process for the concentration of aqueous acetic acids. AT89800B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE89800X 1916-08-25

Publications (1)

Publication Number Publication Date
AT89800B true AT89800B (en) 1922-10-25

Family

ID=5642927

Family Applications (1)

Application Number Title Priority Date Filing Date
AT89800D AT89800B (en) 1916-08-25 1917-06-16 Process for the concentration of aqueous acetic acids.

Country Status (1)

Country Link
AT (1) AT89800B (en)

Similar Documents

Publication Publication Date Title
DE314943C (en)
DE2503610C3 (en) Process for the purification of sulfuric acid contaminated with methylsulfuric acid
DE2938424C2 (en) Process for the separation of acids and bases passing over with distillate vapors
DE1088063B (en) Process for the recovery of dicarboxylic acids and diamines from polyamides
DE3903661C2 (en) Process for processing waste acid containing nitric and sulfuric acid from cellulose nitrate production
DE962162C (en) Process for the production of concentrated formic acid from its alkali salts
DE2515084A1 (en) PROCESS FOR MANUFACTURING MONO-O-BETA-HYDROXYAETHYL-7 RUTIN
DE1768779A1 (en) Process for the production of pure dimethyl sulfoxide
DE2936416C2 (en)
DE960275C (en) Process for the production of aromatic carboxylic acids
DE631176C (en) Process for the preparation of aqueous solutions of medicines
DE1114177B (en) Process for the production of lactic acid
DE520922C (en) Process for the preparation of 2-phenylquinoline-4-carboxylic acid
DE1011411B (en) Process for obtaining pure tert. Butylbenzoic acids
DE652602C (en) Process for the production of condensation products
DE688336C (en) Rapid analytical method for the determination of acridine
AT241697B (en) Process for the preparation of the new N-allylnormorphine-6-nicotinic acid ester
AT114021B (en) Process for the treatment of acetic acid containing cellulose derivatives.
DE497908C (en) Process for the preparation of nitrogen-containing anthraquinone derivatives
DE491221C (en) Process for the preparation of soluble cholesterol compounds
DE875811C (en) Process for the production of lactams
AT33110B (en) Process for the preparation of alkyloxyacetyl compounds of alcohols of the hydroaromatic series.
DE901056C (en) Process for the isolation of amino acids
DE1112509B (en) Process for the enrichment of 2, 3, 6-trichlorobenzoic acid in mixtures of polychlorobenzoic acid
DE718951C (en) Process for the preparation of compounds of methyl-p-tolylcarbinol