NO137235B - PROCEDURE FOR THE PREPARATION OF 3,4-EPOXY-4-METHYL-PENTANON-2 - Google Patents

PROCEDURE FOR THE PREPARATION OF 3,4-EPOXY-4-METHYL-PENTANON-2 Download PDF

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Publication number
NO137235B
NO137235B NO1678/72A NO167872A NO137235B NO 137235 B NO137235 B NO 137235B NO 1678/72 A NO1678/72 A NO 1678/72A NO 167872 A NO167872 A NO 167872A NO 137235 B NO137235 B NO 137235B
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NO
Norway
Prior art keywords
epoxy
methyl
preparation
pentanon
procedure
Prior art date
Application number
NO1678/72A
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Norwegian (no)
Other versions
NO137235C (en
Inventor
Carlo Neri
Emilio Perrotti
Original Assignee
Anic Spa
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 Anic Spa filed Critical Anic Spa
Publication of NO137235B publication Critical patent/NO137235B/en
Publication of NO137235C publication Critical patent/NO137235C/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D303/00Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
    • C07D303/02Compounds containing oxirane rings
    • C07D303/12Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
    • C07D303/32Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by aldehydo- or ketonic radicals

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Plural Heterocyclic Compounds (AREA)
  • Catalysts (AREA)

Description

Foreliggende oppfinnelse angår en fremgangsmåte for fremstilling The present invention relates to a method for production

av 3,4-epoksy-4-m.etyl - pentanon -2. of 3,4-epoxy-4-m.ethyl - pentanone -2.

Det er kjent fremgangsmåter for fremstilling av substituerte eller ikke-substituerte epoksy-forbindelser. Disse er basert på flertrinnsreaksjoner, og anvender vanskelig tilgjengelige reagenser som merkbart influerer på prosessens Skonomi. There are known methods for producing substituted or unsubstituted epoxy compounds. These are based on multi-step reactions, and use hard-to-find reagents that noticeably influence the economy of the process.

Det er nå funnet at det er mulig å syntetisere en substituert, epoksy-forbindelse på en enkel og billig måte i henhold til en fremgangsmåte som er meget interessant ut fra et industrielt synspunkt. It has now been found that it is possible to synthesize a substituted epoxy compound in a simple and cheap way according to a method which is very interesting from an industrial point of view.

Oppfinnelsen vedrbrer således en fremgangsmåte for fremstilling The invention thus relates to a method for production

av 3, 4-epoks:y-4-metylpentanon-2 med formel of 3,4-epoxy:γ-4-methylpentanone-2 with formula

og det særegne ved fremgangsmåten i henhold til oppfinnelsen er at en alkohol.med formel. oiksyderes i væskefase med molekylært oksygen i nærvær av kobber(I)-klorid som katalysator. Reaksjonen forer til dannelse av det substituerte epoksyd etter fblgende skjema and the peculiarity of the method according to the invention is that an alcohol.with formula. is oxidized in the liquid phase with molecular oxygen in the presence of copper(I) chloride as a catalyst. The reaction leads to the formation of the substituted epoxide according to the following scheme

For oppnåelse av en bedre løselighet og følgelighbyere reaksjons-hastighet kan kuprokloridet fordelaktig anvendes i komplekser med en koordinerende base som kan være enkel eller substituert og valgt fra fenantroliner, dipyridylér, pyridiner, dimetylsulfoksyd (DMSO), dimetylformamid (DMF), fosfiner, arsiner, stibiner, imidazol, piperidin osv. Fortrinnsvis anvendes kuprokloridet i form av et kuproklorid-pyridinkompleks. To achieve a better solubility and consequently a higher reaction rate, the cupric chloride can advantageously be used in complexes with a coordinating base which can be simple or substituted and selected from phenanthrolines, dipyridyls, pyridines, dimethylsulfoxide (DMSO), dimethylformamide (DMF), phosphines, arsines, stibines, imidazole, piperidine, etc. The cupric chloride is preferably used in the form of a cupric chloride-pyridine complex.

En fordel ved fremgangsmåten i henhold til oppfinnelsen består i muligheten av ved slutten av oksydasjonsreaksjonen å gjennvinne kobber-utgangsforbindelsen som kan brukes om igjen, og den katalytiske cyklus gjennomfbres uten vesentlig tap av katalysatoren. An advantage of the method according to the invention consists in the possibility of recovering the starting copper compound at the end of the oxidation reaction, which can be used again, and the catalytic cycle is carried out without significant loss of the catalyst.

Oksydasjonen i henhold til oppfinnelsen kan utfores på en enkel måte, den gir gode utbytter og kan gjennomfbres innen et bredt område av trykk og temperatur. Det er mulig å operere både i nærvær og i fravær av losningsmidler eller fortynningsmidler. The oxidation according to the invention can be carried out in a simple way, it gives good yields and can be carried out within a wide range of pressure and temperature. It is possible to operate both in the presence and in the absence of solvents or diluents.

I sistnevnte tilfelle tjener alkoholen selv som reaksjonsmedium. In the latter case, the alcohol itself serves as the reaction medium.

På den annen side kan det i fbrstnevnte tilfelle gjbres bruk av løsningsmidler valgt fra enkle eller substituerte alkyl-, aromatiske og cykloalifatiske hydrokarboner, etere og andre, eller fra de foran nevnte baser. On the other hand, in the first-mentioned case, it is possible to use solvents selected from simple or substituted alkyl, aromatic and cycloaliphatic hydrocarbons, ethers and others, or from the aforementioned bases.

Reaksjonstemperaturen kan variere innen et bredt område. Med hensyn til arbeidstrykket må dette sbrge for opprettholdelse 'av en flytende fase. Anvendbare områder for temperatur er fra 15°C til 150°c og for trykk fra 1 til 30 atmosfærer. The reaction temperature can vary within a wide range. With regard to the working pressure, this must ensure the maintenance of a liquid phase. Usable ranges for temperature are from 15°C to 150°c and for pressure from 1 to 30 atmospheres.

Hvis kuprokloridet anvendes i form av et kuproklorid-pyridinkompleks, fremstilles dette ved kjent teknikk og kan innfores som sådant i reaktoren, eller fremstilles fra CuCl og pyridin under selve oksydasjonsreaksjonen. If the cuprochloride is used in the form of a cuprochloride-pyridine complex, this is produced by known techniques and can be introduced as such into the reactor, or produced from CuCl and pyridine during the oxidation reaction itself.

Noen andre spesielle arbeidsbetingelser vil bli nevnt i det fblgende eksempel som skal illustrere oppfinnelsen. Some other special working conditions will be mentioned in the following example to illustrate the invention.

Eksempel - Fremstilling av 4-me:tyl -3/4-epoksy-pentanpn-2 Example - Preparation of 4-methyl-3/4-epoxy-pentanpn-2

fra diaceton (4-hydroksy-4-me-tyl- pentarion-2) . from diacetone (4-hydroxy-4-methylpentarion-2).

Det ble fremstilt en blanding bestående av 48 gram diacetonalkohol og 3,5 gram pyridin. Deri ble lost 2 gram CuCl og det hele ble underkastet oksydasjon ved gjennombobling av oksygen (2 l/h) ved 70°C. A mixture consisting of 48 grams of diacetone alcohol and 3.5 grams of pyridine was prepared. 2 grams of CuCl were dissolved in it and the whole was subjected to oxidation by bubbling through oxygen (2 l/h) at 70°C.

Etter 12 timer ble 2,5 gram CuCl-pyridin fraskilt ved filtrering After 12 hours, 2.5 grams of CuCl-pyridine were separated by filtration

i nitrogenatmosfære. Reaksjonsproduktene ble analysert i lbsningen ved gasskromatografi. Omdannelsen av diacetonalkohol var 28% ved en selektivitet av 95% til epoksyd og 5% til aceton. in a nitrogen atmosphere. The reaction products were analyzed in the solution by gas chromatography. The conversion of diacetone alcohol was 28% at a selectivity of 95% to epoxide and 5% to acetone.

Det ble oppnådd 12,5 gram epoksyd og 0,7 gram aceton. 12.5 grams of epoxide and 0.7 grams of acetone were obtained.

Claims (2)

1. Fremgangsmåte for fremstilling av 3,4-epoksy-4-metyl-pentanon-2 med formel karakterisert ved at en aUtohol med formel oksyderes i væskefase med molekylært oksygen i. nærvær av kobber(I)-klorid som katalysator.1. Method for the preparation of 3,4-epoxy-4-methyl-pentanone-2 with formula characterized in that an aUtohol with formula oxidized in the liquid phase with molecular oxygen in the presence of copper(I) chloride as a catalyst. 2. Fremgangsmåte som angitt i krav lt karakterisert ved at kobber(I)-kloridet anvendes i form av et kobber(I)-kloridpyridinkompleks.2. Method as stated in claim 1t characterized in that the copper (I) chloride is used in the form of a copper (I) chloride pyridine complex.
NO1678/72A 1971-05-13 1972-05-10 PROCEDURE FOR THE PREPARATION OF 3,4-EPOXY-4-METHYL-PENTANON-2 NO137235C (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT2449971 1971-05-13

Publications (2)

Publication Number Publication Date
NO137235B true NO137235B (en) 1977-10-17
NO137235C NO137235C (en) 1978-01-25

Family

ID=11213758

Family Applications (1)

Application Number Title Priority Date Filing Date
NO1678/72A NO137235C (en) 1971-05-13 1972-05-10 PROCEDURE FOR THE PREPARATION OF 3,4-EPOXY-4-METHYL-PENTANON-2

Country Status (15)

Country Link
AT (1) AT316574B (en)
AU (1) AU466536B2 (en)
BE (1) BE783339A (en)
CA (1) CA996125A (en)
CH (1) CH553774A (en)
DD (1) DD97883A5 (en)
DE (1) DE2223299C3 (en)
DK (1) DK132274C (en)
FR (1) FR2147922B1 (en)
GB (1) GB1381012A (en)
LU (1) LU65336A1 (en)
NL (1) NL144270B (en)
NO (1) NO137235C (en)
SE (1) SE386176B (en)
ZA (1) ZA722962B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8516744D0 (en) * 1985-07-02 1985-08-07 British Petroleum Co Plc Preparation of epoxides

Also Published As

Publication number Publication date
NO137235C (en) 1978-01-25
CH553774A (en) 1974-09-13
DK132274C (en) 1976-05-10
DE2223299B2 (en) 1974-02-14
SE386176B (en) 1976-08-02
FR2147922A1 (en) 1973-03-11
FR2147922B1 (en) 1974-09-27
LU65336A1 (en) 1972-08-23
CA996125A (en) 1976-08-31
AU4162872A (en) 1973-11-01
AU466536B2 (en) 1975-10-30
DE2223299A1 (en) 1972-11-23
GB1381012A (en) 1975-01-22
AT316574B (en) 1974-07-25
DD97883A5 (en) 1973-05-20
NL7206500A (en) 1972-11-15
BE783339A (en) 1972-09-01
ZA722962B (en) 1973-02-28
NL144270B (en) 1974-12-16
DK132274B (en) 1975-11-17
DE2223299C3 (en) 1974-10-03

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