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NO120572B - - Google Patents

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Publication number
NO120572B
NO120572B NO67167981A NO16798167A NO120572B NO 120572 B NO120572 B NO 120572B NO 67167981 A NO67167981 A NO 67167981A NO 16798167 A NO16798167 A NO 16798167A NO 120572 B NO120572 B NO 120572B
Authority
NO
Norway
Prior art keywords
methyl
phenylmaleic
methylamine
anhydride
carried out
Prior art date
Application number
NO67167981A
Other languages
Norwegian (no)
Inventor
A Lowry
Original Assignee
Gillette Co
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 Gillette Co filed Critical Gillette Co
Publication of NO120572B publication Critical patent/NO120572B/no

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D83/00Containers or packages with special means for dispensing contents
    • B65D83/14Containers for dispensing liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant
    • B65D83/72Containers for dispensing liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant with heating or cooling devices, e.g. heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/10Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
    • F28C3/12Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
    • AHUMAN NECESSITIES
    • A45HAND OR TRAVELLING ARTICLES
    • A45DHAIRDRESSING OR SHAVING EQUIPMENT; EQUIPMENT FOR COSMETICS OR COSMETIC TREATMENTS, e.g. FOR MANICURING OR PEDICURING
    • A45D27/00Shaving accessories
    • A45D27/02Lathering the body; Producing lather

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Containers And Packaging Bodies Having A Special Means To Remove Contents (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Pyrrole Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Confectionery (AREA)
  • Coating Apparatus (AREA)

Description

Fremgangsmåte til fremstilling av N-metyl-«-fenylsuccinimid. Process for the preparation of N-methyl-«-phenylsuccinimide.

N-metyl-a-succinimid er blitt et meget verdifullt middel ved behandling av den mildere form for epilepsi (petit mal). Etter amerikansk patent nr. 2 643 258 kan denne forbindelse fremstilles av fenylravsyre eller fenylravsyreanhydrid, ved å la den reagere med metylamin og ved opp-varming av det dannede produkt. Fremgangsmåten lider av den mangel at den krever bruk av fenylravsyre eller fenylravsyreanhydrid, begge meget dyre utgangsmaterialer. Ved hjelp av fremgangsmåten ifølge oppfinnelsen kan N-metyl-a-fenylsuccinimid fremstilles av lett tilgjengelige, billige utgangsmaterialer. N-methyl-a-succinimide has become a very valuable agent in the treatment of the milder form of epilepsy (petit mal). According to US Patent No. 2,643,258, this compound can be prepared from phenylsuccinic acid or phenylsuccinic anhydride, by allowing it to react with methylamine and by heating the product formed. The process suffers from the shortcoming that it requires the use of phenylsuccinic acid or phenylsuccinic anhydride, both very expensive starting materials. By means of the method according to the invention, N-methyl-a-phenylsuccinimide can be produced from readily available, cheap starting materials.

I henhold til oppfinnelsen kan denne forbindelse og andre forbindelser som er omtalt i det følgende, fremstilles ved å la fenylmaleinsyreanhydrid reagere med metylamin ved en temperatur mellom 80 og 110° C. Derved dannes N-metyl-a-fenylmaleinsyreimid. Derpå reduserer man den alifatiske dobbeltbinding som finnes i N-metyl-a-fenylmaleinsyreimidet. According to the invention, this compound and other compounds mentioned below can be prepared by allowing phenylmaleic anhydride to react with methylamine at a temperature between 80 and 110° C. N-methyl-a-phenylmaleic imide is thereby formed. The aliphatic double bond found in the N-methyl-α-phenylmaleic acid imide is then reduced.

Ved utførelsen av reaksjonen mellom fenyl-maleinsyreanhydrid og metylamin anvendes en ekvivalent mengde, eller fortrinsvis et lite overskudd av den beregnede mengde .metylamin. Reaksjonen kan ut-føres i vann, et organisk oppløsningsmid-del eller en blanding av vann og et med vann blandbart organisk oppløsningsmid-del. Andre brukbare oppløsningsmidler enn vann er lavere alifatiske alkoholer When carrying out the reaction between phenylmaleic anhydride and methylamine, an equivalent amount, or preferably a small excess of the calculated amount of methylamine, is used. The reaction can be carried out in water, an organic solvent or a mixture of water and a water-miscible organic solvent. Other usable solvents than water are lower aliphatic alcohols

som metanol, etanol og isopropanol, cykli-ske etere så som dioksan, estere som etylacetat, vandige blandinger av de her nevn-te stoffer og lignende. Av hensyn til om- such as methanol, ethanol and isopropanol, cyclic ethers such as dioxane, esters such as ethyl acetate, aqueous mixtures of the substances mentioned here and the like. For reasons of re-

kostningene er vann å foretrekke. Den foretrukne temperatur for reaksjonens ut-førelse er 95—100° C. Reaksjonen forløper hurtig og er vanligvis ferdig etter y2—2 timer. costs are water preferred. The preferred temperature for carrying out the reaction is 95-100° C. The reaction proceeds rapidly and is usually completed after y2-2 hours.

Reduksjonen av den alifatiske dobbeltbinding i N-metyl-rt-fenylmaleinsyreami-det blir fortrinsvis utført ved hjelp av hydrogengass og en metallisk hydrerings-katalysator. Som hydreringskatalysatorer gir Raney-nikkel og edelmetallkatalysa-torer som platinaoksyd særlig godt resul-tat. Reduksjonen kan utføres ved en temperatur mellom 15—100° C. Hydrogen-trykket er ikke særlig avgjørende og kan varieres fra en til et hundre atmosfærer eller mere. Gode resultater er oppnådd med et hydrogengasstrykk på ca. 2,5—6 atm., og følgelig er det ikke nødvendig med høyere trykk. Som oppløsningsmiddel kan brukes estere, som etylacetat, lavere alifatiske alkoholer, som metanol, etanol, isopropanol, og blandinger av estere og lavere alifatiske alkoholer. The reduction of the aliphatic double bond in the N-methyl-rt-phenylmaleic acid amide is preferably carried out with the aid of hydrogen gas and a metallic hydrogenation catalyst. As hydrogenation catalysts, Raney nickel and noble metal catalysts such as platinum oxide give particularly good results. The reduction can be carried out at a temperature between 15-100° C. The hydrogen pressure is not particularly decisive and can be varied from one to one hundred atmospheres or more. Good results have been achieved with a hydrogen gas pressure of approx. 2.5-6 atm., and consequently a higher pressure is not necessary. As a solvent, esters, such as ethyl acetate, lower aliphatic alcohols, such as methanol, ethanol, isopropanol, and mixtures of esters and lower aliphatic alcohols can be used.

I det følgende beskrives som eksempel en utførelsesform for oppfinnelsen. In the following, an embodiment of the invention is described as an example.

Eksempel: Example:

En blanding som består av 4 g fenyl-maleinsyreanhydrid og 3,5 ml av en 23 pst. oppløsning av metylamin i vann oppvar-mes på dampbad i en time. 10 ml koldt vann tilsettes, blandingen kjøles, og det utfelte N-metyl-a-fenylmaleinsyreimid fil-treres fra. Utbytte 2 g, smeltepunkt 145— 147° C. A mixture consisting of 4 g of phenyl-maleic anhydride and 3.5 ml of a 23% solution of methylamine in water is heated on a steam bath for one hour. 10 ml of cold water are added, the mixture is cooled, and the precipitated N-methyl-α-phenylmaleic acid imide is filtered off. Yield 2 g, melting point 145-147° C.

100 mg platinaoksyd som hydrerings- 100 mg platinum oxide as hydration

katalysator tilsettes til en oppløsning av 4 g N-metyl-a-feny!lmaleinsyreimld i en blanding av 100 ml absolutt etanol og 100 ml etylacetat. Blandingen rystes i et luk-ket kar med vannstoffgass ved et trykk på 3,45 kg/cm2 inntil den teoretiske mengde hydrogen er absorbert. Trykket avblåses, og karet åpnes, katalysatoren frafiltreres, og filtratet indampes til et volum på ca. 15 ml. Oppløsningen filtre-res, filtratet avkjøles, og det utfelte N-metyl-a-fenylsuccinimid frafiltreres. Utbytte 3 g, smeltepunkt 70—72° C. catalyst is added to a solution of 4 g of N-methyl-α-phenylmaleic acid imld in a mixture of 100 ml of absolute ethanol and 100 ml of ethyl acetate. The mixture is shaken in a closed vessel with hydrogen gas at a pressure of 3.45 kg/cm2 until the theoretical amount of hydrogen has been absorbed. The pressure is released, and the vessel is opened, the catalyst is filtered off, and the filtrate is evaporated to a volume of approx. 15 ml. The solution is filtered, the filtrate is cooled, and the precipitated N-methyl-α-phenylsuccinimide is filtered off. Yield 3 g, melting point 70-72° C.

Om ønskes kan de 100 mg platinaok-sydkatalysator som er brukt i ovennevnte forsøk erstattes med ca. 0,5 g Raney-nik-kelkatalysator. If desired, the 100 mg of platinum oxide catalyst used in the above experiment can be replaced with approx. 0.5 g of Raney nickel-nickel catalyst.

Fenylmaleinsyreanhydrid som brukes som et av utgangsstoffene ved utførelsen av oppfinnelsen, kan fremstilles billig og lett ved å la maleinsyreanhydrid reagere med benzen og klor under innvirkning av ultraviolett lys. Phenylmaleic anhydride, which is used as one of the starting materials in carrying out the invention, can be produced cheaply and easily by allowing maleic anhydride to react with benzene and chlorine under the influence of ultraviolet light.

Claims (3)

1. Fremgangsmåte til fremstilling av N-metyl-ct-fenylsuccinimid, karakterisert ved at man lar fenylmaleinsyreanhydrid reagere med metylamin ved en temperatur mellom 80—110° C, og reduserer den alifatiske dobbeltbinding i det dannede N-metyl-a-fenylmaleinsyreimid.1. Process for the production of N-methyl-ct-phenylsuccinimide, characterized by allowing phenylmaleic anhydride to react with methylamine at a temperature between 80-110° C, and reducing the aliphatic double bond in the formed N-methyl-a-phenylmaleic imide. 2. Fremgangsmåte ifølge påstand 1, karakterisert ved at man anvender litt mere enn en ekvivalent av metylaminet for hver ekvivalent av fenylmaleinsyrean-hydridet og utfører reaksjonen i vandig miljø.2. Method according to claim 1, characterized in that a little more than one equivalent of the methylamine is used for each equivalent of the phenylmaleic anhydride and the reaction is carried out in an aqueous environment. 3. Fremgangsmåte ifølge påstand 1 og 2, karakterisert ved at reduksjonen ut-føres under bruk av vannstoffgass og Raney-nikkel eller et edelmetall som hydre-ringskatalysator.3. Method according to claims 1 and 2, characterized in that the reduction is carried out using hydrogen gas and Raney nickel or a precious metal as a hydrogenation catalyst.
NO67167981A 1966-05-05 1967-05-03 NO120572B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US547898A US3373904A (en) 1966-05-05 1966-05-05 Heater for material dispensed from a container

Publications (1)

Publication Number Publication Date
NO120572B true NO120572B (en) 1970-11-02

Family

ID=24186597

Family Applications (1)

Application Number Title Priority Date Filing Date
NO67167981A NO120572B (en) 1966-05-05 1967-05-03

Country Status (12)

Country Link
US (1) US3373904A (en)
AT (1) AT283184B (en)
BE (1) BE698058A (en)
CH (1) CH469512A (en)
DK (1) DK119942B (en)
ES (1) ES340102A1 (en)
FR (1) FR1522672A (en)
GB (1) GB1149599A (en)
GR (1) GR33084B (en)
NL (1) NL6706370A (en)
NO (1) NO120572B (en)
SE (1) SE335407B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3917121A (en) * 1973-09-17 1975-11-04 Warner Lambert Co Spout for dispensing a foamable product
US6405898B1 (en) 2000-11-16 2002-06-18 The Gillette Company Dispenser for a foaming product
USD456654S1 (en) 2000-11-27 2002-05-07 S. C. Johnson & Son, Inc. Dispenser for shaving product
US6415957B1 (en) * 2000-11-27 2002-07-09 S. C. Johnson & Son, Inc. Apparatus for dispensing a heated post-foaming gel

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2962221A (en) * 1959-05-12 1960-11-29 United Aircraft Corp Rocket nozzle construction with cooling means
US3095122A (en) * 1959-12-09 1963-06-25 Gillette Co Aerosol dispensers
NL285511A (en) * 1961-11-17
US3240396A (en) * 1963-06-11 1966-03-15 Robert M Friedenberg Aerosol dispenser
US3292823A (en) * 1964-09-01 1966-12-20 Eversharp Inc Dispenser with heat exchanger at its discharge outlet
US3263744A (en) * 1965-03-08 1966-08-02 Graeme J Mackeown Shave cream heaters

Also Published As

Publication number Publication date
NL6706370A (en) 1967-11-06
US3373904A (en) 1968-03-19
DK119942B (en) 1971-03-15
ES340102A1 (en) 1968-06-01
GB1149599A (en) 1969-04-23
GR33084B (en) 1967-10-31
BE698058A (en) 1967-11-06
AT283184B (en) 1970-07-27
SE335407B (en) 1971-05-24
FR1522672A (en) 1968-04-26
CH469512A (en) 1969-03-15

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