DE2854195A1 - Di:propyl:acetic acid prodn. for pharmaceuticals etc. - by thermal decarboxylation of di:propyl-malonic acid in suspension in toluene - Google Patents
Di:propyl:acetic acid prodn. for pharmaceuticals etc. - by thermal decarboxylation of di:propyl-malonic acid in suspension in tolueneInfo
- Publication number
- DE2854195A1 DE2854195A1 DE19782854195 DE2854195A DE2854195A1 DE 2854195 A1 DE2854195 A1 DE 2854195A1 DE 19782854195 DE19782854195 DE 19782854195 DE 2854195 A DE2854195 A DE 2854195A DE 2854195 A1 DE2854195 A1 DE 2854195A1
- Authority
- DE
- Germany
- Prior art keywords
- toluene
- propyl
- acid
- suspension
- prodn
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
- C07C51/377—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups
- C07C51/38—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups by decarboxylation
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Verfahren zur Herstellung von DipropylessigsäureProcess for the production of dipropyl acetic acid
Dipropylessigsäure ist ein wertvolles Produkt für die pharmazeutische Industrie.Dipropylacetic acid is a valuable product for the pharmaceutical Industry.
Zu ihrer Herstellung kann man die bei 156 bis 1580 C schmelzende Dipropylmalonsaure über diesen Schmelzpunkt erhitzen. Hierbei wird aus einer Carboxylgruppe Kohlendioxid abgespalten und die gewünschte Dipropylessigsãure gebildet. Einer Ausführung in technischem Masstab stehen jedoch mancherlei Schwierigkeiten entgegen. Ein zweckentsprechendes Rühren würde für die Bewegung der zähen Schmelze Spezialruhrwerke erfordern, man musste besondere Massnahmen für den gleichmässigen Warmedurchgang und die Abführung von Wärme treffen, sowie auch für die Ableitung des dabei sich bildenden Kohlendioxids sorgen. Nun könnte man zwar der Schmelze ein hochsiedendes Lösungsmittel zugeben und auf diese Weise die genannten Schwierigkeiten zu vermeiden suchen. Ein solches Lösungsmittel müsse jedoch stark polar sein, weil sonst die Abspaltung des Kohlendioxids nur langsam oder garnicht in Gang kommt. Auch wäre die Abtrennung des Lösungsmittels nicht einfach und erforderte jedenfalls einen besonderen Arbeitsgang. Es ist sehr fraglich, ob ein derartiges Lõsungsmittel, das aus technischen und wirtschaftlichen Gründen gut zugänglich sein musste, überhaupt gefunden werden könnte.Dipropylmalonic acid, which melts at 156 to 1580 C, can be used for their preparation Heat above this melting point. Here, a carboxyl group becomes carbon dioxide split off and the desired DipropylessigsÄure formed. An execution in however, there are various difficulties on the technical scale. An appropriate one Stirring would require special agitators to move the viscous melt special measures had to be taken to ensure the even passage of heat and its dissipation of heat, as well as for the dissipation of the carbon dioxide that forms in the process care for. Now you could add a high-boiling solvent to the melt and in this way seek to avoid the difficulties mentioned. One such However, the solvent must be very polar, because otherwise the carbon dioxide is split off starts slowly or not at all. Separation of the solvent would also be necessary not simple and in any case required a special operation. It is very questionable whether such a solvent, which for technical and economic reasons had to be easily accessible, could be found at all.
Die Erfindung besteht darin, dass feste Dipropylmalonsäure in Toluol aufgeschlämmt und die Aufschlämmung unter Rückflusskühlung destillativ allmählich von Toluol und etwa der Dipropylmalonsaure noch anhaftendem Wasser befreit wird, worauf man nach Beginn der hierbei einsetzenden Abspaltung von Kohlendioxid die Temperatur langsam erhöht und das Erhitzen bis zur Beendigung der Gasentwicklung fortführt. Die gebildete Dipropylessigsäure wird zur Reingewinnung abdestilliert. Man erhält sie in nahezu quantitativer Ausbeute und in einer Reinheit von über 99%.The invention is that solid dipropylmalonic acid in toluene slurried and gradually reflux the slurry by distillation toluene and any water still adhering to it is freed from, for example, dipropylmalonic acid, whereupon after the start of the splitting off of carbon dioxide that begins here, the Temperature slowly increased and heating until the evolution of gas has ceased continues. The formed dipropyl acetic acid is distilled off for pure recovery. They are obtained in almost quantitative yield and in a purity of over 99%.
Beispiel: 500 Gewichtsteile feste kristallisierte Di-n-propyl-malonsãure werden in 500 Raumteilen Toluol suspendiert. Unter gleichmässigem Rühren wird das Gemisch erhitzt bis Toluol abzudestillieren beginnt. Beim Erreichen einer Innentemperatur von 1400 C, bei der das Reaktionsgemisch einen gut rührfähigen Brei bildet, beginnt die Bildung von Kohlendioxid. Die Temperatur wird allmählich 0 auf 160 C gesteigert und solange beibehalten, bis keinerlei Lösungsmittel mehr überdestilliert und die Gasentwicklung beendet ist. Danach wird auf 1200 C abgekühlt. In das nunmehr flüssige Reaktionsgemisch werden weitere 500 Gewichtsteile Di-n-propylmalonsãure eingetragen. Der Aufheizvorgang auf 1600 C wird, wie oben beschrieben, wiederholt, danach wird wiederum abgekühlt und die Restmenge von 1049 Gewichtsteilen kristallisierter Di-n-propylmalonsäure zugegeben.Example: 500 parts by weight of solid crystallized di-n-propyl-malonic acid are suspended in 500 parts by volume of toluene. While stirring evenly, the Mixture heated until toluene begins to distill off. When an internal temperature is reached of 1400 ° C., at which the reaction mixture forms an easily stirrable paste, begins the formation of carbon dioxide. The temperature is gradually increased from 0 to 160.degree and maintained until no more solvent distilled over and the Gas evolution has ended. It is then cooled to 1200.degree. In the now liquid A further 500 parts by weight of di-n-propylmalonic acid are added to the reaction mixture. The heating process to 1600 C is repeated as described above, then is cooled again and the remaining amount of 1049 parts by weight of crystallized di-n-propylmalonic acid admitted.
Nach Erhitzen auf 1600 C bis zum Aufhören der Kohlendioxidentwicklung wird das nunmehr flüssige Gemisch auf etwa 1000 c abgekühlt und aus diesem unmittelbar bei vermindertem Druck das gebildete Reaktionsprodukt abdestilliert.After heating to 1600 C until the evolution of carbon dioxide ceases the now liquid mixture is cooled to about 1000 c and from this immediately the reaction product formed is distilled off under reduced pressure.
0 Man erhält 1487 Gewichtsteile einer zwischen 117 - 124 C (bei 12 - 15 Torr} siedenden, farblosen, wasserklaren Fraktion, die aus über 99%-iger Di-n-propylessigsäure besteht. Dies entspricht einer Ausbeute von 97,4 %, bezogen auf eingesetzte 100%-ige Di-n-propylmalonsäure. 0 1487 parts by weight of a temperature between 117 - 124 C (at 12 - 15 Torr} boiling, colorless, water-clear fraction, which consists of over 99% di-n-propyl acetic acid consists. This corresponds to a yield of 97.4%, based on 100% used Di-n-propylmalonic acid.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19782854195 DE2854195A1 (en) | 1978-12-15 | 1978-12-15 | Di:propyl:acetic acid prodn. for pharmaceuticals etc. - by thermal decarboxylation of di:propyl-malonic acid in suspension in toluene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19782854195 DE2854195A1 (en) | 1978-12-15 | 1978-12-15 | Di:propyl:acetic acid prodn. for pharmaceuticals etc. - by thermal decarboxylation of di:propyl-malonic acid in suspension in toluene |
Publications (1)
Publication Number | Publication Date |
---|---|
DE2854195A1 true DE2854195A1 (en) | 1980-06-26 |
Family
ID=6057288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19782854195 Withdrawn DE2854195A1 (en) | 1978-12-15 | 1978-12-15 | Di:propyl:acetic acid prodn. for pharmaceuticals etc. - by thermal decarboxylation of di:propyl-malonic acid in suspension in toluene |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE2854195A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4417073A (en) * | 1980-11-29 | 1983-11-22 | Dynamit Nobel A.G. | Process for the preparation of substituted acetic acids and derivatives thereof |
WO1994006743A1 (en) * | 1992-09-12 | 1994-03-31 | Heinz Nau | Analogues of vpa used as anti-epileptica |
WO2008062471A2 (en) * | 2006-10-19 | 2008-05-29 | Calyx Chemicals And Pharmaceuticals Ltd. | A mild method for the production of di-n-propylacetic acid (valproic acid) |
-
1978
- 1978-12-15 DE DE19782854195 patent/DE2854195A1/en not_active Withdrawn
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4417073A (en) * | 1980-11-29 | 1983-11-22 | Dynamit Nobel A.G. | Process for the preparation of substituted acetic acids and derivatives thereof |
WO1994006743A1 (en) * | 1992-09-12 | 1994-03-31 | Heinz Nau | Analogues of vpa used as anti-epileptica |
WO2008062471A2 (en) * | 2006-10-19 | 2008-05-29 | Calyx Chemicals And Pharmaceuticals Ltd. | A mild method for the production of di-n-propylacetic acid (valproic acid) |
WO2008062471A3 (en) * | 2006-10-19 | 2008-07-10 | Calyx Chemicals And Pharmaceut | A mild method for the production of di-n-propylacetic acid (valproic acid) |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
8139 | Disposal/non-payment of the annual fee |