DE1011865B - Process for the production of isobutanol in addition to isobutyric acid - Google Patents
Process for the production of isobutanol in addition to isobutyric acidInfo
- Publication number
- DE1011865B DE1011865B DEB40078A DEB0040078A DE1011865B DE 1011865 B DE1011865 B DE 1011865B DE B40078 A DEB40078 A DE B40078A DE B0040078 A DEB0040078 A DE B0040078A DE 1011865 B DE1011865 B DE 1011865B
- Authority
- DE
- Germany
- Prior art keywords
- isobutanol
- parts
- isobutyric acid
- addition
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/295—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with inorganic bases, e.g. by alkali fusion
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Verfahren zur Herstellung von Isobutanol neben Isobuttersäure Es wurde gefunden, daß man Isobutanol neben Isobuttersäure auf einfache Weise herstellen kann, wenn man 2, 2, 4-Trimethylpentandiol-(1, 3) mit Ätzalkalien erhitzt. Die Reaktion wird im allgemeinen bei Normaldruck ohne Anwendung von Lösungsmitteln bei Temperaturen oberhalb 1000, insbesondere bei 120 bis 1500, ausgeführt. Man kann auch bei erhöhtem Druck arbeiten, desgleichen ist die Anwendung von I,ösungsmitt,ein möglich. Hierzu besonders geeignet sind gewisse Alkohole, z. B. Iso- und n-Butanol. Bei drucklosem Arbeiten müssen die Lösungsmittel einen genügend hohen Siedepunkt besitzen, so daß die erforderliche Reaktionstemperatur erreicht werden kann. Man kann aber auch niedrigersiedende Lösungsmittel, z. B. Methanol, unter Druck anwenden.Process for the production of isobutanol in addition to isobutyric acid It has been found that isobutanol can be produced in a simple manner in addition to isobutyric acid can if you heated 2, 2, 4-trimethylpentanediol- (1, 3) with caustic alkalis. The reaction is generally at normal pressure without the use of solvents at temperatures above 1000, in particular at 120 to 1500, carried out. One can also with increased Working under pressure, it is also possible to use I, solvent, on. For this Particularly suitable are certain alcohols, e.g. B. iso- and n-butanol. With unpressurized Work the solvents must have a sufficiently high boiling point so that the required reaction temperature can be reached. But you can also use lower boiling points Solvents, e.g. B. methanol, apply under pressure.
Die Reaktion ist unter Ausschluß von H2O durchführbar, da bei der Erwärmung-des Gemisches von Ätzalkali und 2, 2, 4-Trimethylpentandiol-(1, 3) die Ätzalkalien bei 110 bis 1200 gelöst werden. Man verwendet in der Regel wasserfreies Ätzkali und/oder Ätznatron und Verbindungen, die bei 100 bis 140° in Ätzalkalien übergehen, in einer Menge von mindestens 1 Mol Alkali auf 2 Mol Trimethylpentandiol, zweckmäßig aber im Überschuß. Die Anwendung von konzentrierter Alkalilauge an Stelle von trockenen Ätzalkalien ist weniger vorteilhaft, weil man bis zum Eintreten der Reaktion die Hauptmenge des Wassers abdampfen muß. The reaction can be carried out with the exclusion of H2O, since the Heating-the mixture of caustic alkali and 2, 2, 4-trimethylpentanediol- (1, 3) the Caustic alkalis can be dissolved at 110 to 1200. Usually anhydrous is used Caustic potash and / or caustic soda and compounds that at 100 to 140 ° in caustic alkalis pass, in an amount of at least 1 mole of alkali to 2 moles of trimethylpentanediol, useful but in excess. The application of concentrated alkali in place of dry caustic alkalis is less beneficial because you get up to the occurrence of the Reaction, most of the water must evaporate.
Die in den Beispielen genannten Teile sind Gevichtsteile. The parts mentioned in the examples are weight parts.
Beispiel 1 1460 Teile 2, 2, 4-Trimethylpentandiol-(1, 3) werden in einem Kolben, der mit Rührer und Riickflußkühler versehen ist, mit 450 Teilen Ätzkali in einem Ölbad von 1450 erhitzt. Die Temperatur steigt im Reaktionsgemisch zunächst auf 1350 und fällt, sowie die Bildung von Isobutanol einsetzt, wieder ab. Die Reaktionsmischung wird dabei völlig homogen. Man ersitzt dann noch 5 Stunden am Rückfluß und destilliert anschließend 545 Teile Isobutanol ab. Dann gibt man 1000 Teile Wasser zu dem fest gewordenen Rückstand und destilliert weiter Isobutanol als Azeotrop über und trennt im Destillat die Isobutanolschicht von der unteren wäßrigen Schicht, die in die Destillation zurückgeführt wird. Auf diese Weise werden nochmals 548 Teile Isobutanol (wasserfrei) gewonnen. Die Gesamtmenge an Isobutanol beträgt somit 1093 Teile. Example 1 1460 parts of 2, 2, 4-trimethylpentanediol- (1, 3) are in a flask equipped with a stirrer and reflux condenser with 450 parts of caustic potash heated in a 1450 oil bath. The temperature initially rises in the reaction mixture to 1350 and falls again as soon as isobutanol begins to form. The reaction mixture becomes completely homogeneous. It is then refluxed for a further 5 hours and distilled then 545 parts of isobutanol. Then 1000 parts of water are added to the solid become residue and isobutanol distilled over further as an azeotrope and separates in the distillate the isobutanol layer from the lower aqueous layer that goes into distillation is returned. In this way, another 548 parts of isobutanol (anhydrous) won. The total amount of isobutanol is thus 1093 parts.
Aus dem alkalischen wäßrigen Rückstand im Kolben kann man nun durch Ausäthern 50 Teile nicht umgesetztes 2, 2, 4-Trimethylpentandiol-(1, 3) isolieren.From the alkaline aqueous residue in the flask you can now through Ethereal 50 parts of unreacted 2, 2, 4-trimethylpentanediol- (1, 3) to isolate.
Danach wird mit 500/oiger Schwefelsäure unter Kühlung angesäuert und die freie Isobuttersäure ausgeäthert. Die Destillation der Isobuttersäure ergibt dabei insgesamt 425 Teile, einschließlich des Gehaltes der geringen wasserhaltigen Vorfraktion, der durch Säurezahlbestimmung ermittelt wird.It is then acidified with 500% sulfuric acid with cooling and the free isobutyric acid is etherified. The distillation of the isobutyric acid gives thereby a total of 425 parts, including the content of the low hydrous Pre-fraction, which is determined by determining the acid number.
Beispiel 2 1460 Teile 2, 2, 4-Trimethylpentandiol- (1, 3) und 330 Teile Ätznatron werden, wie im Beispiel 1 beschrieben, 7 Stunden lang erhitzt und aufgearbeitet. Example 2 1460 parts of 2, 2, 4-trimethylpentanediol- (1, 3) and 330 Parts of caustic soda are, as described in Example 1, heated for 7 hours and worked up.
Man erhält 974 Teile Isobutanol und 485 Teile Isobuttersäure.974 parts of isobutanol and 485 parts of isobutyric acid are obtained.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB40078A DE1011865B (en) | 1956-04-30 | 1956-04-30 | Process for the production of isobutanol in addition to isobutyric acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB40078A DE1011865B (en) | 1956-04-30 | 1956-04-30 | Process for the production of isobutanol in addition to isobutyric acid |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1011865B true DE1011865B (en) | 1957-07-11 |
Family
ID=6965980
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEB40078A Pending DE1011865B (en) | 1956-04-30 | 1956-04-30 | Process for the production of isobutanol in addition to isobutyric acid |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE1011865B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5006585A (en) * | 1989-09-05 | 1991-04-09 | Huls America Inc. | Stain-resistant plasticizer compositions and method of making same |
US5039728A (en) * | 1989-09-05 | 1991-08-13 | Huls America Inc. | Stain-resistant plasticizer compositions and method of making same |
-
1956
- 1956-04-30 DE DEB40078A patent/DE1011865B/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5006585A (en) * | 1989-09-05 | 1991-04-09 | Huls America Inc. | Stain-resistant plasticizer compositions and method of making same |
US5039728A (en) * | 1989-09-05 | 1991-08-13 | Huls America Inc. | Stain-resistant plasticizer compositions and method of making same |
EP0673916A1 (en) | 1989-09-05 | 1995-09-27 | Velsicol Chemical Corporation | Preparation of 2,2,4-trimethyl-1,3-pentanediol dibenzoate and di(alkyl-substituted) benzoates |
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