CH493475A - Process for purifying malononitrile - Google Patents
Process for purifying malononitrileInfo
- Publication number
- CH493475A CH493475A CH905968A CH905968A CH493475A CH 493475 A CH493475 A CH 493475A CH 905968 A CH905968 A CH 905968A CH 905968 A CH905968 A CH 905968A CH 493475 A CH493475 A CH 493475A
- Authority
- CH
- Switzerland
- Prior art keywords
- diels
- malononitrile
- alder
- reaction
- acid dinitrile
- Prior art date
Links
- CUONGYYJJVDODC-UHFFFAOYSA-N malononitrile Chemical compound N#CCC#N CUONGYYJJVDODC-UHFFFAOYSA-N 0.000 title claims description 17
- 238000000034 method Methods 0.000 title claims description 9
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 18
- 238000005698 Diels-Alder reaction Methods 0.000 claims description 14
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 10
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 10
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims description 10
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims description 7
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims description 7
- 239000011976 maleic acid Substances 0.000 claims description 7
- 150000001875 compounds Chemical class 0.000 claims description 6
- QPJDMGCKMHUXFD-UHFFFAOYSA-N cyanogen chloride Chemical compound ClC#N QPJDMGCKMHUXFD-UHFFFAOYSA-N 0.000 claims description 5
- KYPOHTVBFVELTG-OWOJBTEDSA-N (e)-but-2-enedinitrile Chemical compound N#C\C=C\C#N KYPOHTVBFVELTG-OWOJBTEDSA-N 0.000 claims description 4
- JXPDNDHCMMOJPC-UHFFFAOYSA-N 2-hydroxybutanedinitrile Chemical compound N#CC(O)CC#N JXPDNDHCMMOJPC-UHFFFAOYSA-N 0.000 claims description 3
- 238000004821 distillation Methods 0.000 claims description 3
- 238000002844 melting Methods 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 238000005119 centrifugation Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 230000001419 dependent effect Effects 0.000 claims 2
- 239000011541 reaction mixture Substances 0.000 description 8
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 5
- 239000006227 byproduct Substances 0.000 description 3
- 239000001530 fumaric acid Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- YLQBMQCUIZJEEH-UHFFFAOYSA-N Furan Chemical compound C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 125000002080 perylenyl group Chemical group C1(=CC=C2C=CC=C3C4=CC=CC5=CC=CC(C1=C23)=C45)* 0.000 description 2
- CSHWQDPOILHKBI-UHFFFAOYSA-N peryrene Natural products C1=CC(C2=CC=CC=3C2=C2C=CC=3)=C3C2=CC=CC3=C1 CSHWQDPOILHKBI-UHFFFAOYSA-N 0.000 description 2
- SDJHPPZKZZWAKF-UHFFFAOYSA-N 2,3-dimethylbuta-1,3-diene Chemical compound CC(=C)C(C)=C SDJHPPZKZZWAKF-UHFFFAOYSA-N 0.000 description 1
- QISOBCMNUJQOJU-UHFFFAOYSA-N 4-bromo-1h-pyrazole-5-carboxylic acid Chemical compound OC(=O)C=1NN=CC=1Br QISOBCMNUJQOJU-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- CJSBUWDGPXGFGA-UHFFFAOYSA-N dimethyl-butadiene Natural products CC(C)=CC=C CJSBUWDGPXGFGA-UHFFFAOYSA-N 0.000 description 1
- BEFDCLMNVWHSGT-UHFFFAOYSA-N ethenylcyclopentane Chemical compound C=CC1CCCC1 BEFDCLMNVWHSGT-UHFFFAOYSA-N 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- -1 piperylenes Chemical compound 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 239000004334 sorbic acid Substances 0.000 description 1
- 229940075582 sorbic acid Drugs 0.000 description 1
- 235000010199 sorbic acid Nutrition 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C255/00—Carboxylic acid nitriles
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Verfahren zur Reinigung von Malonsäuredinitril Die Erfindung betrifft ein Verfahren zur Reinigung von Malonsäuredinitril durch Entfernung des bei der Herstellung von Malonsäuredinitril aus Acetonitril und Chlorcyan anfallenden Fumarsäure- und Maleinsäuredinitrils aus dem Reaktionsgemisch.
Es ist bekannt, Malonsäuredinitril durch Umsatz von Acetonitril und Chlorcyan bei höheren Temperaturen, gegebenenfalls in Gegenwart von gasförmigem Chlor als Katalysator herzustellen. Bei dieser Reaktion fallen als Nebenprodukt grössere Mengen an Fumar- und Maleinsäuredinitril an. Die Entfernung dieser Nebenprodukte aus dem Reaktionsgemisch ist infolge der Ähnlichkeit der physikalischen Konstanten mit erheblichen Schwierigkeiten verbunden.
Der Erfindung liegt die Aufgabe zugrunde, auf einfache Weise eine Abtrennung des Fumarsäure- und Maleinsäuredinitrils von Malonsäuredinitril durchzuführen.
Erfindungsgemäss wird dies dadurch erreicht, dass man das im Reaktionsgemisch befindliche Maleinsäureund Fumarsäuredinitril durch eine Diels-Alder-Reaktion in die entsprechenden Diels-Alder-Anlagerungsverbindungen überführt und letztere vom Malonsäuredinitril abtrennt.
Als Reaktionskomponente für die Diels-Alder-Reaktion kommen Verbindungen mit konjugierter Doppelbindung in Betracht. Solche sind beispielsweise Butadien, Isopren, Dimethylbutadien, Piperylene, Anthracen, Perylen, Furan, Sorbinsäure. Vorzungsweise werden Butadien und Anthracen verwendet.
Je nach Diels-Alder-Reaktionskomponenten entstehen Anlagerungsverbindungen, die bei Temperaturen oberhalb des Schmelzpunktes von Malonsäuredinitril feste oder flüssige Produkte darstellen. Fallen feste Anlagerungsprodukte an, wie z.B. im Falle der Verwendung von Anthracen oder Perylen, so kann die Abtrennung der Diels-Alder-Anlagerungsverbindungen durch einfaches Filtrieren oder Zentrifugieren bei Temperaturen oberhalb des Schmelzpunktes des Malonsäuredinitrils, vorteilhaft bei Temperaturen von 35-400C, durchgeführt werden.
Fallen flüssige Anlagerungsprodukte an, wie z.B. bei Anwendung von Butadien, kann die Trennung durch einfaches Abdestillieren des Malonsäuredinitrils im Vakuum erfolgen.
Die Diels-Alder-Reaktion wird in einem bei der Umsetzung von Acetonnitril und Chlorcyan anfallenden und gegebenenfalls anschliessend an Malonitril angereicherten Reaktionsgemisch durchgeführt. Bevorzugte Reaktionstemperaturen liegen bei 40 bis 1500C, wobei unter Umständen die Reaktion in einem Autoklaven durchgeführt wird. Vorteilhaft ist es jedoch, zuerst durch Destillation noch nicht umgesetztes Ausgangsprodukt zu entfernen und anschliessend das Reaktionsgemisch vor der Diels-Alder-Umsetzung noch einer Destillation im Vakuum bei 5 bis 30 mm Hg zu unterwerfen, um noch andere in geringen Mengen vorhandene Verunreinigungen, wie z.B. p-Chlorpropionitril, abzuziehen.
Das Verfahren der Erfindung kann sowohl diskontinuierlich als auch kontinuierlich durchgeführt werden.
Im letzteren Fall ist es zweckmässig, die Umsetzung in einem Röhrenreaktor mit entsprechender Verweilzeit durchzuführen.
Beispiele
1. 100 g eines Reaktionsgemisches, bestehend aus 97 g Malonsäuredinitril, 2 g Maleinsäuredinitril und 1 Fumarsäuredinitril wurden in einem Reaktionsgefäss aus Glas unter Rühren mit 7 g Anthracen versetzt und während zwei Stunden auf 1400C gehalten. Anschliessend wurde auf 350C abgekühlt und bei dieser Temperatur die Diels-Alder-Anlagerungsverbindung abfiltriert.
Das Filtrat wurde noch einmal bei 12 mm Hg destilliert.
Es resultierten 92g Malonsäuredinitril in einer Reinheit von über 99%. Die Ausbeute betrug 95%.
2. Aus einem durch Umsatz von Acetonitril und Chlorcyan anfallenden Reaktionsgemisch wurde durch Destillation noch vorhandenes Ausgangsmaterial (Acetonitril) abgezogen, anschliessend wurden im Vakuum (13 mm Hg) noch vorhandene Nebenprodukte (z.B. ,8- Chlorpropionitril) entfernt. 80 g dieses nun 96% Malonsäuredinitril enthaltenden Reaktionsgemisches wurden in einem Autoklaven mit 4 g Butadien versetzt und 10 Stunden bei 100-110 C erwärmt. Anschliessend wurde destilliert (13 mm Hg). Es wurden so 74,7 g reines Malonsäuredinitril (99,8%) erhalten, entsprechend einer Ausbeute von 97%.
Process for purifying malononitrile The invention relates to a process for purifying malononitrile by removing from the reaction mixture the fumaric acid and maleic acid dinitrile obtained in the production of malononitrile from acetonitrile and cyanogen chloride.
It is known that malononitrile can be prepared by reacting acetonitrile and cyanogen chloride at elevated temperatures, optionally in the presence of gaseous chlorine as a catalyst. In this reaction, large amounts of fumaric and maleic acid dinitrile are produced as by-products. The removal of these by-products from the reaction mixture is associated with considerable difficulties due to the similarity of the physical constants.
The invention is based on the object of separating the fumaric acid and maleic acid dinitrile from malonic acid dinitrile in a simple manner.
According to the invention, this is achieved by converting the maleic acid and fumaric acid dinitrile present in the reaction mixture into the corresponding Diels-Alder addition compounds by a Diels-Alder reaction and separating the latter from the malonic acid dinitrile.
Compounds with conjugated double bonds can be used as reaction components for the Diels-Alder reaction. Such are, for example, butadiene, isoprene, dimethylbutadiene, piperylenes, anthracene, perylene, furan, sorbic acid. Butadiene and anthracene are preferably used.
Depending on the Diels-Alder reaction components, addition compounds are formed which, at temperatures above the melting point of malononitrile, represent solid or liquid products. Are solid addition products produced, such as If anthracene or perylene is used, the Diels-Alder addition compounds can be separated off by simple filtration or centrifugation at temperatures above the melting point of the malononitrile, advantageously at temperatures of 35-40 ° C.
If there are liquid addition products, e.g. If butadiene is used, the separation can be carried out by simply distilling off the malononitrile in vacuo.
The Diels-Alder reaction is carried out in a reaction mixture obtained in the reaction of acetonitrile and cyanogen chloride and optionally subsequently enriched in malonitrile. Preferred reaction temperatures are from 40 to 1500 ° C., the reaction being carried out in an autoclave under certain circumstances. However, it is advantageous to first remove unreacted starting product by distillation and then to subject the reaction mixture to a vacuum distillation at 5 to 30 mm Hg before the Diels-Alder reaction in order to remove other impurities present in small amounts, such as e.g. p-chloropropionitrile.
The process of the invention can be carried out either batchwise or continuously.
In the latter case, it is advisable to carry out the reaction in a tubular reactor with an appropriate residence time.
Examples
1. 100 g of a reaction mixture consisting of 97 g of malonic acid dinitrile, 2 g of maleic acid dinitrile and 1 g of fumaric acid dinitrile were mixed with 7 g of anthracene while stirring in a reaction vessel and kept at 1400 ° C. for two hours. It was then cooled to 350 ° C. and the Diels-Alder addition compound was filtered off at this temperature.
The filtrate was distilled again at 12 mm Hg.
92 g of malononitrile resulted in a purity of over 99%. The yield was 95%.
2. Starting material (acetonitrile) still present was removed from a reaction mixture obtained through the conversion of acetonitrile and cyanogen chloride by distillation, then by-products (e.g. 8-chloropropionitrile) still present were removed in vacuo (13 mm Hg). 80 g of this reaction mixture, which now contained 96% malononitrile, were mixed with 4 g of butadiene in an autoclave and heated at 100-110 ° C. for 10 hours. It was then distilled (13 mm Hg). In this way 74.7 g of pure malononitrile (99.8%) were obtained, corresponding to a yield of 97%.
Claims (1)
Priority Applications (21)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH905968A CH493475A (en) | 1968-06-18 | 1968-06-18 | Process for purifying malononitrile |
| DE19691921662 DE1921662C3 (en) | 1968-05-09 | 1969-04-28 | Process for purifying malononitrile |
| CS308669A CS157061B2 (en) | 1968-05-09 | 1969-04-30 | |
| ES366851A ES366851A1 (en) | 1968-05-09 | 1969-05-06 | Process for the production of malonic acid dinitrile and purification thereof |
| RO59900A RO56619A (en) | 1968-05-09 | 1969-05-06 | |
| US822724A US3655721A (en) | 1968-05-09 | 1969-05-07 | Process for the production of malonic acid dinitrile and purification thereof |
| YU1127/69A YU32949B (en) | 1968-05-09 | 1969-05-07 | Postupak za proizvodnju cistog dinitrila malonske kiseline |
| BE732687D BE732687A (en) | 1968-05-09 | 1969-05-07 | |
| AT437369A AT292660B (en) | 1968-05-09 | 1969-05-07 | Process for the production of pure malononitrile |
| FR6914577A FR2008128A1 (en) | 1968-05-09 | 1969-05-07 | |
| SE7115883A SE385473B (en) | 1968-05-09 | 1969-05-08 | MAKE PURE PROPANDINITRIL BY REMOVAL OF THE CIS- AND TRANSBUTENDINITRILE FROM THE REACTION MIXTURE BY PROPANDINITRIL FROM ACETONNITRIL AND CHLORCYAN |
| SE7115884A SE385474B (en) | 1968-05-09 | 1969-05-08 | PLEASE PROVIDE PURE PROPANDINITRIL BY DISPOSING OF THE ACTONITRIL AND CHLOROCYAN TO PROPANDINITRIL AS A BY-PRODUCT OBTAINING THE CIS AND TRANSBUTENDINITRIL BY SELECTIVE HYDRATION |
| PL15712469A PL78197B1 (en) | 1968-06-18 | 1969-05-08 | |
| NO1898/69A NO130584C (en) | 1968-05-09 | 1969-05-08 | |
| JP44034898A JPS50646B1 (en) | 1968-05-09 | 1969-05-08 | |
| NL6907129.A NL164553C (en) | 1968-05-09 | 1969-05-09 | METHOD FOR PROCESSING A MALONIC ACID DINITRILE PRODUCT. |
| GB23712/69A GB1222343A (en) | 1968-05-09 | 1969-05-09 | Process for the production of pure malonic acid dinitrile |
| US05/137,592 US4105688A (en) | 1968-05-09 | 1971-04-26 | Process for the production of malonic acid dinitrile and purification thereof |
| US00137593A US3742020A (en) | 1968-05-09 | 1971-04-26 | Process for the production of malonic acid dinitrile and purification thereof |
| DK114479A DK114479A (en) | 1968-05-09 | 1979-03-20 | PROCEDURE FOR PROPANDINITRIL PURIFICATION |
| NL8004516A NL8004516A (en) | 1968-05-09 | 1980-08-07 | Prepn malonic dinitrile from acetonitrile and cyan - ogen chloride |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH905968A CH493475A (en) | 1968-06-18 | 1968-06-18 | Process for purifying malononitrile |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH493475A true CH493475A (en) | 1970-07-15 |
Family
ID=4347872
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH905968A CH493475A (en) | 1968-05-09 | 1968-06-18 | Process for purifying malononitrile |
Country Status (2)
| Country | Link |
|---|---|
| CH (1) | CH493475A (en) |
| PL (1) | PL78197B1 (en) |
-
1968
- 1968-06-18 CH CH905968A patent/CH493475A/en not_active IP Right Cessation
-
1969
- 1969-05-08 PL PL15712469A patent/PL78197B1/pl unknown
Also Published As
| Publication number | Publication date |
|---|---|
| PL78197B1 (en) | 1975-04-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PL | Patent ceased |