EP1210337A1 - Method for producing 4,6-dichloropyrimidine with sulfur compounds and phosphorous compounds - Google Patents

Method for producing 4,6-dichloropyrimidine with sulfur compounds and phosphorous compounds

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Publication number
EP1210337A1
EP1210337A1 EP00948019A EP00948019A EP1210337A1 EP 1210337 A1 EP1210337 A1 EP 1210337A1 EP 00948019 A EP00948019 A EP 00948019A EP 00948019 A EP00948019 A EP 00948019A EP 1210337 A1 EP1210337 A1 EP 1210337A1
Authority
EP
European Patent Office
Prior art keywords
sulfur
chloro
dichloropyrimidine
methoxypyrimidine
mol
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Withdrawn
Application number
EP00948019A
Other languages
German (de)
French (fr)
Inventor
Franz-Josef Mais
Alexander Klausener
Günther Cramm
Guido Steffan
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bayer Chemicals AG
Original Assignee
Bayer AG
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 Bayer AG filed Critical Bayer AG
Publication of EP1210337A1 publication Critical patent/EP1210337A1/en
Withdrawn legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D239/00—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings
    • C07D239/02—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings
    • C07D239/24—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings having three or more double bonds between ring members or between ring members and non-ring members
    • C07D239/28—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings having three or more double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, directly attached to ring carbon atoms
    • C07D239/30—Halogen atoms or nitro radicals

Definitions

  • the present invention relates to a process for the preparation of 4,6-dichloropyrimidine from 4-chloro-6-methoxypyrimidine.
  • 4,6-dichloropyrimidine is a valuable intermediate for the production of crop protection products.
  • Ci-Ci Q- alkyl or Cg-Ci Q- aryl which may be substituted by up to 5 identical or different substituents from the group fluorine, chlorine, bromine, C 1 -C 4 -alkyl and C ⁇ -C ⁇ alkoxy can,
  • n stand for zero or 1.
  • Preferred sulfur-containing chlorinating agents are SOCI2 and SO2CI2, preferred phosphorus compounds triphenylphosphine and triphenylphosphine oxide.
  • phosphorus compounds of the formula (I) Based on 1 mol of sulfur-containing chlorinating agents, for example 0.01 to 1 mol of phosphorus compounds of the formula (I) can be used. This amount is preferably 0.02 to 0.25, particularly preferably 0.05 to 0.1 mol.
  • the process according to the invention is preferably carried out in the presence of a solvent.
  • a solvent for example, aromatic solvents such as toluene, xylenes, chlorobenzene, dichlorobenzenes, chlorotoluenes, benzonitrile and benzotrifluoride, nitrogen-containing solvents such as N-methylpyrrolidone, dimethylformamide, dimethylacetamide and cyclic ureas and oxygen-containing solvents such as ethers, in particular higher-boiling ethers, are suitable. Mixtures of solvents can also be used.
  • the process according to the invention can be carried out, for example, at temperatures in the range from 50 to 200.degree. 75 to 175 ° C., in particular 100 to 150 ° C., are preferred.
  • the pressure is not critical. Only if you want to use solvents that boil at normal pressure below the desired reaction temperature, it is advisable to work under increased pressure so that the solvent is at least partially in liquid form.
  • the pressure can range, for example, from 0.1 to 5 bar.
  • the process is preferably carried out at atmospheric pressure, particularly preferably with a solvent which boils under reflux at the desired reaction temperature under atmospheric pressure.
  • the process according to the invention can be carried out batchwise and continuously.
  • 4-chloro-6-methoxypyrimidine, the phosphorus compound and a solvent are introduced, the mixture is heated to the reaction temperature and then the sulfur-containing chlorinating agent is metered in, if appropriate in several portions.
  • the reaction mixture present after the reaction can be e.g. work up by distilling it over a column, if necessary under reduced pressure.
  • the process according to the invention can be used to convert 4-chloro-6-methoxypyrimidine into 4,6-dichloropyrimidine in a simple manner.
  • the conversion succeeds in
  • Example 1 was repeated, but 200 ml of a mixture of isomeric xylenes were used instead of chlorobenzene and the process was carried out at 135.degree.
  • the HPLC analysis showed a yield of 4,6-dichloropyrimidine of 93.6% and unreacted 4-chloro-6-methoxypyrimidine in an amount of 2.6% of the feed.
  • Example 1 was repeated, but instead of thionyl chloride, 49.2 g of a mixture of 3 mols of SOO2 and 1 mol of SO2Cl2 were added dropwise in 1 hour and after 6

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Pyridine Compounds (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Plural Heterocyclic Compounds (AREA)

Abstract

According to the invention, 4,6-dichloropyrimidine is advantageously produced from 4-chlorine-6-methoxypyrimidine by using at least one chlorinating agent containing sulfur and in the presence of at least one phosphorous compound.

Description

Verfahren zur Herstellung von 4,6-Dichlorpyrimidin mit Schwefel- und Phosphorverbindungen Process for the preparation of 4,6-dichloropyrimidine with sulfur and phosphorus compounds
Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung von 4,6-Dichlor- pyrimidin aus 4-Chlor-6-methoxypyrimidin. 4,6-Dichlorpyrimidin ist ein wertvolles Zwischenprodukt zur Herstellung von Pflanzenschutzmitteln.The present invention relates to a process for the preparation of 4,6-dichloropyrimidine from 4-chloro-6-methoxypyrimidine. 4,6-dichloropyrimidine is a valuable intermediate for the production of crop protection products.
Es sind eine Reihe Verfahren zur Herstellung von 4,6-Dichlorpyrimidin bekannt, bei denen von 4,6-Dihydroxypyrimidin ausgegangen wird.A number of processes for the preparation of 4,6-dichloropyrimidine are known, starting from 4,6-dihydroxypyrimidine.
Es ist auch bekannt (siehe Res. Discl. n 391, 690-691 (1996)), dass man 4,6-Dichlor- pyrimidin durch Umsetzung von 4-Chlor-6-methoxypyrimidin mit einem Chlorier- agenz der Formel R3PCI2 umsetzen kann. Das Chlorieragenz kann als solches einge- setzt werden oder in situ aus einer Verbindung der Formel R3P=O und Phosgen hergestellt werden. Weiterhin wird dort beschrieben, dass 4-Chlor-6-methoxypyrimi- din mit Phosphoroxychlorid nicht reagiert. Nachteilig bei diesem Verfahren ist, dass in der Regel nur eine sehr unvollständige Umsetzung erzielt werden kann und somit 4,6-Dichlorpyrimidin nur in geringen Ausbeuten und geringen Reinheitsgraden erhältlich ist.It is also known (see Res. Discl. N 391, 690-691 (1996)) that 4,6-dichloropyrimidine can be reacted with a chlorinating agent of the formula R3PCI2 by reacting 4-chloro-6-methoxypyrimidine , The chlorination agent can be used as such or can be prepared in situ from a compound of the formula R 3 P = O and phosgene. It also describes that 4-chloro-6-methoxypyrimidine does not react with phosphorus oxychloride. A disadvantage of this process is that, as a rule, only a very incomplete conversion can be achieved and therefore 4,6-dichloropyrimidine can only be obtained in low yields and low degrees of purity.
Es wurde nun ein Verfahren zur Herstellung von 4,6-Dichlorpyrimidin aus 4-Chlor- 6-methoxypyrimidin gefunden, das dadurch gekennzeichnet ist, dass man 4-Chlor-6- methoxypyrimidin mit mindestens einem schwefelhaltigen Chloriermittel ausgewählt aus der Gruppe SCI2, SOCI2 und SO2CI2 und in Gegenwart mindestens einer Phosphorverbindung der FormelA process has now been found for the preparation of 4,6-dichloropyrimidine from 4-chloro-6-methoxypyrimidine, which is characterized in that 4-chloro-6-methoxypyrimidine is selected from the group SCI2, SOCI2 and SO2CI2 and in the presence of at least one phosphorus compound of the formula
R3P=Yn (i),R 3 P = Yn (i),
in der R für Ci-CiQ-Alkyl oder Cg-CiQ-Aryl stehen, die gegebenenfalls durch bis zu 5 gleiche oder verschiedene Substituenten aus der Gruppe Fluor, Chlor, Brom, Cι-C4-Alkyl und C\ -C^Alkoxy substituiert sein können,in the R represents Ci-Ci Q- alkyl or Cg-Ci Q- aryl, which may be substituted by up to 5 identical or different substituents from the group fluorine, chlorine, bromine, C 1 -C 4 -alkyl and C \ -C ^ alkoxy can,
Y für Sauerstoff oder SchwefelY for oxygen or sulfur
undand
n für Null oder 1 stehen.n stand for zero or 1.
Bevorzugte schwefelhaltige Chloriermittel sind SOCI2 und SO2CI2, bevorzugte Phosphorverbindungen Triphenylphosphin und Triphenylphosphinoxid.Preferred sulfur-containing chlorinating agents are SOCI2 and SO2CI2, preferred phosphorus compounds triphenylphosphine and triphenylphosphine oxide.
Bezogen auf 1 Mol 4-Chlor-6-methoxypyrimidin kan man beispielsweise mindestens 1 Mol schwefelhaltiges Chloriermittel einsetzen. Vorzugsweise liegt diese Menge beiBased on 1 mole of 4-chloro-6-methoxypyrimidine, for example, at least 1 mole of sulfur-containing chlorinating agent can be used. This amount is preferably included
1 bis 2 Mol.1 to 2 moles.
Bezogen auf 1 Mol schwefelhaltige Chloriermittel kann man beispielsweise 0,01 bis 1 Mol Phosphorverbindungen der Formel (I) einsetzen. Vorzugsweise liegt diese Menge bei 0,02 bis 0,25, besonders bevorzugt bei 0,05 bis 0,1 Mol.Based on 1 mol of sulfur-containing chlorinating agents, for example 0.01 to 1 mol of phosphorus compounds of the formula (I) can be used. This amount is preferably 0.02 to 0.25, particularly preferably 0.05 to 0.1 mol.
Vorzugsweise führt man das erfmdungsgemäße Verfahren in Gegenwart eines Lösungsmittels durch. In Frage kommen beispielsweise aromatische Lösungsmittel wie Toluol, Xylole, Chlorbenzol, Dichlorbenzole, Chlortoluole, Benzonitril und Benzo- trifluorid, stickstoffhaltige Lösungsmittel wie N-Methylpyrrolidon, Dimethylform- amid, Dimethylacetamid und cyclische Harnstoffe und sauerstoffhaltige Lösungsmittel wie Ether, insbesondere höhersiedende Ether und Polyether. Auch Gemische von Lösungsmitteln sind einsetzbar. Das erfindungsgemäße Verfahren kann z.B. bei Temperaturen im Bereich 50 bis 200°C durchgeführt werden. Bevorzugt sind 75 bis 175°C, insbesondere 100 bis 150°C.The process according to the invention is preferably carried out in the presence of a solvent. For example, aromatic solvents such as toluene, xylenes, chlorobenzene, dichlorobenzenes, chlorotoluenes, benzonitrile and benzotrifluoride, nitrogen-containing solvents such as N-methylpyrrolidone, dimethylformamide, dimethylacetamide and cyclic ureas and oxygen-containing solvents such as ethers, in particular higher-boiling ethers, are suitable. Mixtures of solvents can also be used. The process according to the invention can be carried out, for example, at temperatures in the range from 50 to 200.degree. 75 to 175 ° C., in particular 100 to 150 ° C., are preferred.
Der Druck ist im Prinzip unkritisch. Lediglich wenn man Lösungsmittel einsetzen will, die bei Normaldruck unterhalb der gewünschten Reaktionstemperatur sieden, ist es angezeigt, unter erhöhtem Druck zu arbeiten, damit das Lösungsmittel zumindest teilweise in flüssiger Form vorliegt.In principle, the pressure is not critical. Only if you want to use solvents that boil at normal pressure below the desired reaction temperature, it is advisable to work under increased pressure so that the solvent is at least partially in liquid form.
Unter der Voraussetzung, dass bei gegebener Temperatur keine Edukte, Produkte undProvided that at a given temperature no starting materials, products and
Lösungsmittel aus dem Reaktionsgefäß entweichen, kann der Druck beispielsweise im Bereich 0,1 bis 5 bar liegen. Vorzugsweise wird bei Normaldruck gearbeitet, besonders bevorzugt mit einem Lösungsmittel, das bei der gewünschten Reaktionstemperatur unter Normaldruck am Rückfluss siedet.If the solvent escapes from the reaction vessel, the pressure can range, for example, from 0.1 to 5 bar. The process is preferably carried out at atmospheric pressure, particularly preferably with a solvent which boils under reflux at the desired reaction temperature under atmospheric pressure.
Das erfindungsgemäße Verfahren kann diskontinuierlich und kontinuierlich durchgeführt werden.The process according to the invention can be carried out batchwise and continuously.
Bei einer bevorzugten Ausfuhrungsform des erfindungsgemäßen Verfahrens legt man 4-Chlor-6-methoxypyrimidin, die Phosphorverbindung und ein Lösungsmittel vor, erhitzt das Gemisch auf Reaktionstemperatur und dosiert dann das schwefelhaltige Chloriermittel gegebenenfalls in mehreren Teilmengen dazu.In a preferred embodiment of the process according to the invention, 4-chloro-6-methoxypyrimidine, the phosphorus compound and a solvent are introduced, the mixture is heated to the reaction temperature and then the sulfur-containing chlorinating agent is metered in, if appropriate in several portions.
Das nach der Umsetzung vorliegende Reaktionsgemisch kann man z.B. aufarbeiten, indem man es über eine Kolonne, gegebenenfalls bei vermindertem Druck, destilliert.The reaction mixture present after the reaction can be e.g. work up by distilling it over a column, if necessary under reduced pressure.
Mit dem erfmdungsgemäßen Verfahren kann man in einfacher Weise 4-Chlor-6- methoxypyrimidin in 4,6-Dichlorpyrimidin umwandeln. Die Umwandlung gelingt imThe process according to the invention can be used to convert 4-chloro-6-methoxypyrimidine into 4,6-dichloropyrimidine in a simple manner. The conversion succeeds in
Gegensatz zum Stand der Technik nahezu vollständig. Dies ermöglicht die einfache Herstellung eines Produktes mit einem hohen Gehalt an 4,6-Dichlorpyrimidin. Dies ist wünschenswert, da nicht umgesetztes 4-Chlor-6-methoxypyrimidin destillativ nur schwer abtrennbar ist. In contrast to the prior art, almost completely. This enables the easy manufacture of a product with a high content of 4,6-dichloropyrimidine. This is desirable because unreacted 4-chloro-6-methoxypyrimidine is difficult to remove by distillation.
BeispieleExamples
Beispiel 1example 1
29,0 g 4-Chlor-6-methoxypyrimidin und 5,6 g Triphenylphosphinoxid wurden in29.0 g of 4-chloro-6-methoxypyrimidine and 5.6 g of triphenylphosphine oxide were added in
150 g Chlorbenzol vorgelegt und unter Rühren auf 140°C erhitzt. In diese Lösung tropfte man im Verlaufe von 1 Stunde 35,7 g Thionylchlorid ein. Danach rührte man bei 140°C nach. Nach 6 Stunden tropfte man weitere 11,9 g Thionylchlorid ein und rührte weitere 6 Stunden nach. Danach wurde auf 25 °C abgekühlt. Man erhielt eine Auswaage von 304,1 g. Die HPLC- Analyse ergab einen Gehalt von 9,34 % 4,6-Di- chlorpyrimidin (das entspricht einer Ausbeute von 95,3 % der Theorie). Das Reaktionsgemisch enthielt nur 0,1 % 4-Chlor-6-methoxypyrimidin (das entspricht 1,05 % vom Einsatz).150 g of chlorobenzene are introduced and heated to 140 ° C. with stirring. 35.7 g of thionyl chloride were added dropwise to this solution over the course of 1 hour. The mixture was then stirred at 140 ° C. After 6 hours, a further 11.9 g of thionyl chloride were added dropwise and stirring was continued for a further 6 hours. The mixture was then cooled to 25 ° C. A weight of 304.1 g was obtained. The HPLC analysis showed a content of 9.34% 4,6-dichloropyrimidine (this corresponds to a yield of 95.3% of theory). The reaction mixture contained only 0.1% 4-chloro-6-methoxypyrimidine (this corresponds to 1.05% from use).
Beispiel 2Example 2
Beispiel 1 wurde wiederholt, jedoch wurden 200 ml eines Gemisches isomerer Xylole statt Chlorbenzol eingesetzt und bei 135°C gearbeitet. Die HPLC-Analyse ergab eine Ausbeute an 4,6-Dichlorpyrimidin von 93,6 % und unumgesetztem 4-Chlor- 6-methoxypyrimidin in einer Menge von 2,6 % des Einsatzes.Example 1 was repeated, but 200 ml of a mixture of isomeric xylenes were used instead of chlorobenzene and the process was carried out at 135.degree. The HPLC analysis showed a yield of 4,6-dichloropyrimidine of 93.6% and unreacted 4-chloro-6-methoxypyrimidine in an amount of 2.6% of the feed.
Beispiel 3Example 3
Beispiel 1 wurde wiederholt, jedoch wurden statt Thionylchlorid 49,2 g eines Ge- misches aus 3 Molen SOO2 und 1 Mol SO2CI2 in 1 Stunde zugetropft und nach 6Example 1 was repeated, but instead of thionyl chloride, 49.2 g of a mixture of 3 mols of SOO2 and 1 mol of SO2Cl2 were added dropwise in 1 hour and after 6
Stunden kein weiteres Chloriermittel mehr zugefügt. Die HPLC-Analyse ergab eine Ausbeute von 89,3 % der Theorie an 4,6-Dichloφyrimidin. No more chlorinating agent added for hours. The HPLC analysis showed a yield of 89.3% of theory of 4,6-dichloφyrimidine.

Claims

Patentansprüche claims
1. Verfahren zur Herstellung von 4,6-Dichloφyrimidin aus 4-Chlor-6-methoxy- pyrimidin, dadurch gekennzeichnet, dass man 4-Chlor-6-methoxypyrimidin mit mindestens einem schwefelhaltigen Chloriermittel ausgewählt aus der Gruppe SCI2, SOCI2 und SO2CI2 und in Gegenwart mindestens einer Phosphorverbindung der Formel1. A process for the preparation of 4,6-dichloφyrimidine from 4-chloro-6-methoxy-pyrimidine, characterized in that 4-chloro-6-methoxypyrimidine with at least one sulfur-containing chlorinating agent selected from the group SCI2, SOCI2 and SO2CI2 and in Presence of at least one phosphorus compound of the formula
R^P=Y. (I),R ^ P = Y. (I)
in derin the
R für C Cio-Alkyl oder Cg-Cio-Aryl stehen, die gegebenenfalls durch bis zu 5 gleiche oder verschiedene Substituenten aus der Gruppe Fluor, Chlor, Brom, Cι-C4-Alkyl und substituiert sein können,R is C Cio-alkyl or Cg-Cio-aryl, which may be substituted by up to 5 identical or different substituents from the group fluorine, chlorine, bromine, C 1 -C 4 -alkyl and can be substituted
Y für Sauerstoff oder SchwefelY for oxygen or sulfur
undand
n für Null oder 1 stehen.n stand for zero or 1.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass man als schwefel- haltige Chloriermittel SOCI2 und/oder SO2CI2 verwendet.2. The method according to claim 1, characterized in that SOCI2 and / or SO2CI2 is used as the sulfur-containing chlorinating agent.
3. Verfahren nach Ansprüchen 1 und 2, dadurch gekennzeichnet, dass man als Phosphorverbindungen Triphenylphosphin und/oder Triphenylphosphinoxid verwendet. 3. Process according to Claims 1 and 2, characterized in that triphenylphosphine and / or triphenylphosphine oxide are used as phosphorus compounds.
4. Verfahren nach Ansprüchen 1 bis 3, dadurch gekennzeichnet, dass man auf 1 Mol 4-Chlor-6-methoxypyrimidin mindestens 1 Mol schwefelhaltige Chloriermittel einsetzt.4. Process according to Claims 1 to 3, characterized in that at least 1 mol of sulfur-containing chlorinating agent is used per 1 mol of 4-chloro-6-methoxypyrimidine.
5. Verfahren nach Ansprüchen 1 bis 4, dadurch gekennzeichnet, dass man bezogen auf 1 Mol schwefelhaltige Chloriermittel 0,01 bis 1 Mol Phosphorverbindungen der Formel (I) einsetzt.5. Process according to Claims 1 to 4, characterized in that 0.01 to 1 mol of phosphorus compounds of the formula (I) are used, based on 1 mol of sulfur-containing chlorinating agent.
6. Verfahren nach Ansprüchen 1 bis 5, dadurch gekennzeichnet, dass man es in Gegenwart eines Lösungsmittels durchführt.6. The method according to claims 1 to 5, characterized in that it is carried out in the presence of a solvent.
7. Verfahren nach Anspruch 6, dadurch gekennzeichnet, dass man aromatische Lösungsmittel, stickstoffhaltige Lösungsmittel oder sauerstoffhaltige Lösungsmittel einsetzt.7. The method according to claim 6, characterized in that one uses aromatic solvents, nitrogen-containing solvents or oxygen-containing solvents.
Verfahren nach Ansprüchen 1 bis 7, dadurch gekennzeichnet, dass man die Reaktion bei 50 bis 200°C durchführt. Process according to Claims 1 to 7, characterized in that the reaction is carried out at 50 to 200 ° C.
EP00948019A 1999-08-13 2000-07-31 Method for producing 4,6-dichloropyrimidine with sulfur compounds and phosphorous compounds Withdrawn EP1210337A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19938500 1999-08-13
DE19938500A DE19938500A1 (en) 1999-08-13 1999-08-13 Process for the preparation of 4,6-dichloropyrimidine with sulfur and phosphorus compounds
PCT/EP2000/007401 WO2001012610A1 (en) 1999-08-13 2000-07-31 Method for producing 4,6-dichloropyrimidine with sulfur compounds and phosphorous compounds

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EP1210337A1 true EP1210337A1 (en) 2002-06-05

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EP (1) EP1210337A1 (en)
JP (1) JP2003507370A (en)
AU (1) AU6161200A (en)
CA (1) CA2388607A1 (en)
DE (1) DE19938500A1 (en)
WO (1) WO2001012610A1 (en)

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CN103073505B (en) * 2013-01-28 2015-11-18 泰州百力化学股份有限公司 The method of 4-chloro-6-methoxylpyrimidin synthesis 4,6-dichloro pyrimidine
CN103242236B (en) * 2013-04-26 2014-11-19 扬州大学 Preparation method for synthesizing substituted benzimidazole by taking acrylonitrile as nitrogen source

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GB9408270D0 (en) 1994-04-26 1994-06-15 Zeneca Ltd Chemical process
AT402818B (en) 1995-06-02 1997-09-25 Chemie Linz Gmbh METHOD FOR PRODUCING PURE 4,6-DICHLORPYRIMIDINE

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See references of WO0112610A1 *

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AU6161200A (en) 2001-03-13
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JP2003507370A (en) 2003-02-25
WO2001012610A1 (en) 2001-02-22

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