DE2853732A1 - Prepn. of di:propyl-acetic acid - by reacting di;ethyl malonate with propyl bromide and heating the resulting di:propyl-malonic acid - Google Patents
Prepn. of di:propyl-acetic acid - by reacting di;ethyl malonate with propyl bromide and heating the resulting di:propyl-malonic acidInfo
- Publication number
- DE2853732A1 DE2853732A1 DE19782853732 DE2853732A DE2853732A1 DE 2853732 A1 DE2853732 A1 DE 2853732A1 DE 19782853732 DE19782853732 DE 19782853732 DE 2853732 A DE2853732 A DE 2853732A DE 2853732 A1 DE2853732 A1 DE 2853732A1
- Authority
- DE
- Germany
- Prior art keywords
- propyl
- acid
- resulting
- acetic acid
- reacting
- 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- Withdrawn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
- C07C51/09—Preparation of carboxylic acids or their salts, halides or anhydrides from carboxylic acid esters or lactones
-
- 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)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Verfahren zur Herstellung von Di-n-propylessigsäureProcess for the preparation of di-n-propyl acetic acid
Die Erfindung betrifft ein neues Verfahren zur Herstellung der für pharmazeutische Zwecke dienenden Di-n-propylessigsäure. Sie ist dadurch gekennzeichnet, dass man Malonsäurediäthylester in Gegenwart von Natriumäthylat mit n-Propylbromid umsetzt, den hierbei erhaltenen Dipropylmalonester mittels Alkali verseift, die entstandene Dipropylmalonsäure abtrennt und diese durch Erhitzen unter Abspaltung von Kohlendioxid in Di-n-propylessigsäure überführt.The invention relates to a new method for producing the for Di-n-propyl acetic acid for pharmaceutical purposes. It is characterized by that diethyl malonate in the presence of sodium ethylate with n-propyl bromide converts, the resulting dipropylmalonic ester saponified by means of alkali, the resulting dipropylmalonic acid is separated off and this is split off by heating converted from carbon dioxide into di-n-propyl acetic acid.
Für die geschilderten Stufen des Verfahrens kann man beispielsweise den nachstehend beschriebenen Weg benutzen.For the steps of the process outlined, one can, for example use the route described below.
Malonsäurediäthylester und n-Propylbromid werden im erforderlichen Molverhältnis mit der im wesentlichen äquivalenten Menge Natriumäthylat in Äthanol bei erhohter Temperatur umgesetzt.Malonic acid diethyl ester and n-propyl bromide are required Molar ratio with the essentially equivalent amount of sodium ethylate in ethanol implemented at elevated temperature.
Nach beendeter Reaktion wird der überschüssige Alkohol abdestilliert und der Rückstand mit wässrigem Alkali bei erhöhter Temperatur behandelt. Nach Entfernen der restlichen Lösungsmittelmengen wird mit Mineralsäure angesäuert und das Reaktionsprodukt durch Abkühlen zur Kristallisation gebracht.When the reaction has ended, the excess alcohol is distilled off and treating the residue with aqueous alkali at an elevated temperature. After removal the remaining amount of solvent is acidified with mineral acid and the reaction product brought to crystallization by cooling.
Die kristalline Dipropylmalonsäure wird abgetrennt und unter 0 Rühren allmählich auf Temperaturen über 160 C erhitzt. Der Vorgang wird solange fortgesetzt, bis die Abspaltung von Kohlendioxid beendet ist. Der verbleibende Rückstand wird destilliert, wobei man sehr reine Dipropylessigsäure in hoher Ausbeute erhält.The crystalline dipropylmalonic acid is separated off and stirring is carried out gradually heated to temperatures above 160 C. The process continues until until the splitting off of carbon dioxide has ended. The remaining residue will distilled, very pure dipropylacetic acid being obtained in high yield.
Das erhaltene Produkt ist völlig frei von Nebenprodukten, wie sie von einer Monosubstitution des Malonesters herrühren können.The product obtained is completely free of by-products like them can result from monosubstitution of the malonic ester.
Beispiel: 0 Zu einer auf 60 - 62 C erwärmten Mischung von 4,81 Gewichtsteilen Malonsäurediäthylester und 7,38 Gewichtsteilen n-Propylbromid lässt man eine Lösung von 3,24 Gewichtsteilen Na-methylat (100 %ig) in 30 Raumteilen Äthanol innerhalb von 4 - 5 Stunden zufliessen. Anschliessend wird solange unter Rückfluss, bei etwa 740 C, erhitzt, bis der pH-Wert des Reaktionsgemisches bei etwa 9 liegt. Nach dem Abdestillieren von 27 Raumteilen Alkohol werden 11,5 Gewichtsteile einer konzentrierten (44,3 %eigen), wässrigen Kalilauge zugegeben.Example: 0 For a mixture of 4.81 parts by weight heated to 60 - 62 ° C Diethyl malonate and 7.38 parts by weight of n-propyl bromide are allowed to form a solution of 3.24 parts by weight of sodium methylate (100%) in 30 parts by volume of ethanol within flow from 4 - 5 hours. Then as long as reflux, at about 740 C, heated until the pH of the reaction mixture is about 9. After this Distilling off 27 parts by volume of alcohol becomes 11.5 parts by weight of a concentrated (44.3% own), aqueous potassium hydroxide solution added.
Das Gemisch wird 4 Stunden bei Rückflusstemperatur gehalten, dann abgekühlt und nach Zugabe von 13 Raumteilen Wasser so lange auf 1000 c erhitzt, bis 15 - 16 Raumteile Destillat erhalten werden.The mixture is kept at reflux temperature for 4 hours, then cooled and, after adding 13 parts by volume of water, heated to 1000 c for as long as up to 15-16 parts by volume of distillate are obtained.
Zu dem auf etwa 800 C abgekühlten Rückstand werden 9,93 Gewichtsteile konzentrierte Salzsäure (37,5 %ig) zugegeben. Der pH-Wert muss im stark sauren Bereich (bei etwa 1) liegen. Unter allmählich zunehmender Kühlung wird bis auf + io0 c abgekühlt.9.93 parts by weight are added to the residue, which has been cooled to about 800 ° C. concentrated hydrochloric acid (37.5%) was added. The pH must be in strongly acidic range (around 1). Under gradually increasing cooling will cooled down to + io0 c.
Dabei tritt die Kristallisation des Reaktionsproduktes ein.The reaction product then crystallizes.
Nach längerem Nachrühren bei loOC wird zentrifugiert und mit kaltem Wasser nachgewaschen. Nach dem Trocknen erhält man 2,56 Gewichtsteile reine Di-n-propylmalonsäure. Sie ist nahezu rein weiss, grobkristallin, zeigt einen Schmelzpunkt von 154 - 1560 C und einen Gehalt (titriert) von 99,5 %.After prolonged stirring at loOC, it is centrifuged and with cold Washed with water. After drying, 2.56 parts by weight of pure di-n-propylmalonic acid are obtained. It is almost pure white, coarsely crystalline, has a melting point of 154 - 1560 C and a content (titrated) of 99.5%.
Der Gehalt an Monopropylmalonsäure (gaschromatographisch bestimmt) liegt unter 0,2 %.The content of monopropylmalonic acid (determined by gas chromatography) is below 0.2%.
Das trockene Produkt wird nun unter Rühren und allmählicher 0 Temperatursteigerung auf 160 - 165 C erhitzt. Wenn unter Aufschäumen die Kohlendioxidentwicklung einsetzt, dann wird die Reaktionstemperatur durch vorsichtige Wärmezufuhr mög-0 lichst konstant bei 165 - 170 C gehalten, bis die Gasentwicklung beendet ist. Das erhaltene, flüssige Reaktionsprodukt wird unmittelbar danach unter vermindertem Druck abdestilliert. Die zwischen 117 - 1240 C (bei 12 - 15 Torr) übergehende Hauptfraktion besteht aus über 99%iger farbloser, wasserklarer Di-propyl-essigsäure.The dry product is now with stirring and a gradual increase in temperature heated to 160 - 165 C. If the development of carbon dioxide starts with foaming, then the reaction temperature is kept as constant as possible by careful supply of heat held at 165-170 ° C. until the evolution of gas has ceased. The obtained, liquid Immediately thereafter, the reaction product is distilled off under reduced pressure. The main fraction passing between 117 - 1240 C (at 12 - 15 Torr) consists of Over 99% colorless, water-clear di-propyl-acetic acid.
Man erhält 1,86 Gewichtsteile, entsprechend einer Ausbeute von 95 %, bezogen auf Dipropylmalonsäure, bzw. 42,9% bezogen auf eingesetzten Malonsäurediäthylester.1.86 parts by weight are obtained, corresponding to a yield of 95 %, based on dipropylmalonic acid, or 42.9% based on diethyl malonate used.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19782853732 DE2853732A1 (en) | 1978-12-13 | 1978-12-13 | Prepn. of di:propyl-acetic acid - by reacting di;ethyl malonate with propyl bromide and heating the resulting di:propyl-malonic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19782853732 DE2853732A1 (en) | 1978-12-13 | 1978-12-13 | Prepn. of di:propyl-acetic acid - by reacting di;ethyl malonate with propyl bromide and heating the resulting di:propyl-malonic acid |
Publications (1)
Publication Number | Publication Date |
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DE2853732A1 true DE2853732A1 (en) | 1980-07-03 |
Family
ID=6057006
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19782853732 Withdrawn DE2853732A1 (en) | 1978-12-13 | 1978-12-13 | Prepn. of di:propyl-acetic acid - by reacting di;ethyl malonate with propyl bromide and heating the resulting di:propyl-malonic acid |
Country Status (1)
Country | Link |
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DE (1) | DE2853732A1 (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 |
EP0729936A1 (en) * | 1995-03-03 | 1996-09-04 | Societe Civile Bioprojet | Process for the synthesis of alpha substituted acrylic acids and their application |
CN103183599A (en) * | 2011-12-30 | 2013-07-03 | 北大方正集团有限公司 | Method for preparing 2-valproic acid |
-
1978
- 1978-12-13 DE DE19782853732 patent/DE2853732A1/en not_active Withdrawn
Cited By (5)
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 |
EP0729936A1 (en) * | 1995-03-03 | 1996-09-04 | Societe Civile Bioprojet | Process for the synthesis of alpha substituted acrylic acids and their application |
FR2731219A1 (en) * | 1995-03-03 | 1996-09-06 | Bioprojet Soc Civ | PROCESS FOR THE SYNTHESIS OF ALPHA-SUBSTITUTED ACRYLIC ACIDS AND THEIR APPLICATION |
CN103183599A (en) * | 2011-12-30 | 2013-07-03 | 北大方正集团有限公司 | Method for preparing 2-valproic acid |
CN103183599B (en) * | 2011-12-30 | 2015-04-01 | 北大方正集团有限公司 | Method for preparing 2-valproic acid |
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Legal Events
Date | Code | Title | Description |
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8139 | Disposal/non-payment of the annual fee |