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NO151715B - PROCEDURE FOR ELECTRO-CHEMICAL PREPARATION OF 2- (2-AMINOETHYL) THIOPHEN - Google Patents

PROCEDURE FOR ELECTRO-CHEMICAL PREPARATION OF 2- (2-AMINOETHYL) THIOPHEN Download PDF

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Publication number
NO151715B
NO151715B NO790231A NO790231A NO151715B NO 151715 B NO151715 B NO 151715B NO 790231 A NO790231 A NO 790231A NO 790231 A NO790231 A NO 790231A NO 151715 B NO151715 B NO 151715B
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Prior art keywords
thiophene
organic
aminoethyl
medium
nitrovinyl
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NO790231A
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Norwegian (no)
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NO151715C (en
NO790231L (en
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Emile Henri Urbain Braye
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Parcor
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Publication of NO790231L publication Critical patent/NO790231L/en
Publication of NO151715B publication Critical patent/NO151715B/en
Publication of NO151715C publication Critical patent/NO151715C/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D333/00Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom
    • C07D333/02Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings
    • C07D333/04Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom
    • C07D333/06Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to the ring carbon atoms
    • C07D333/14Radicals substituted by singly bound hetero atoms other than halogen
    • C07D333/20Radicals substituted by singly bound hetero atoms other than halogen by nitrogen atoms
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00Electrolytic production of organic compounds
    • C25B3/20Processes
    • C25B3/25Reduction

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Heterocyclic Compounds Containing Sulfur Atoms (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

FREMGANGSMÅTE FOR ELEKTROKJEMISK FREMSTILLING AV 2-(2-AMINOETHYL)-THIOFEN.PROCEDURE FOR ELECTROCHEMICAL PREPARATION OF 2- (2-AMINOETHYL) THIOFEN.

Description

Foreliggende oppfinnelse angår en fremgangsmåte for elektrokjemisk fremstilling av 2-(2-aminoethyl)-thiofen. The present invention relates to a method for the electrochemical production of 2-(2-aminoethyl)-thiophene.

2-(2-aminoethyl)-thiofen er et mellomprodukt som anvendes ved fremstilling av thienopyridinderivater som i sær-deleshet utviser en inhiberende virkning på blodplateaggregering, anti-inflammatorisk aktivitet og vasodilatoraktivitet og som er beskrevet i fransk patentskrift 2 215 948 og tilleggspatent 2 345 150. 2-(2-aminoethyl)-thiophene is an intermediate used in the production of thienopyridine derivatives which, in particular, exhibit an inhibitory effect on platelet aggregation, anti-inflammatory activity and vasodilator activity and which is described in French patent document 2 215 948 and supplementary patent 2 345 150.

Oppfinnelsen angår således en fremgangsmåte ved fremstilling av 2-(2-aminoethyl)-thiofen av formel: hvilken fremgangsmåte er kjennetegnet ved at 2-(2-nitrovinyl)-thiofen av formel: The invention thus relates to a process for the production of 2-(2-aminoethyl)-thiophene of formula: which process is characterized in that 2-(2-nitrovinyl)-thiophene of formula:

i et organisk eller vandig-organisk medium reduseres elektrokjemisk ved et potensial på 1,10-1,30 V, fortrinnsvis ved 1,15 V, målt i forhold til en mettet calomel referanseelektrode, i nærvær av et alkalimetallklorid i en konsentrasjon på in an organic or aqueous-organic medium is reduced electrochemically at a potential of 1.10-1.30 V, preferably at 1.15 V, measured relative to a saturated calomel reference electrode, in the presence of an alkali metal chloride in a concentration of

0,2-0,7 mol/l, fortrinnsvis 0,5 mol/l, som elektrolytt, og til-stedeværende ved en pH på 2 og en temperatur mellom 5 og 40°C, hvoretter det ønskede produkt utvinnes fra reaksjonsmediet. 0.2-0.7 mol/l, preferably 0.5 mol/l, as electrolyte, and present at a pH of 2 and a temperature between 5 and 40°C, after which the desired product is recovered from the reaction medium.

Det organiske medium skal være slik at det tillater oppløsning av utgangsmaterialet, dvs. 2-(2-nitrovinyl)-thiofen, og kan f.eks. være eddiksyre, dioxan eller methanol. The organic medium must be such that it allows dissolution of the starting material, i.e. 2-(2-nitrovinyl)-thiophene, and can e.g. be acetic acid, dioxane or methanol.

Ifølge en foretrukken utførelsesform av oppfinnelsen anvendes det et vandig-alkoholisk medium omfattende 20 - 70 vekt% organisk løsningsmiddel og fortrinnsvis en blanding omfattende 50% organisk løsningsmiddel, slik som en vann-eddiksyreblanding (50:50). According to a preferred embodiment of the invention, an aqueous-alcoholic medium is used comprising 20-70% by weight organic solvent and preferably a mixture comprising 50% organic solvent, such as a water-acetic acid mixture (50:50).

Den elektrokjemiske reduksjon utføres ved et potensial på 1,10 - 1,30 V i forhold til en mettet calomel referanseelektrode, og fortrinnsvis ved et potensial på ca. 1,15 V. The electrochemical reduction is carried out at a potential of 1.10 - 1.30 V in relation to a saturated calomel reference electrode, and preferably at a potential of approx. 1.15V.

pH på reaksjonsmediet skal være ved en verdi på 2. The pH of the reaction medium must be at a value of 2.

Denne pH kan oppnås ved tilsetning av en sterk uorganisk syre This pH can be achieved by adding a strong inorganic acid

slik som saltsyre eller ved hjelp av en egnet buffer (eksempelvis citrat-HCl). such as hydrochloric acid or by means of a suitable buffer (for example citrate-HCl).

Elektrolytten tilsettes til det organiske eller vandig-organiske medium for å bevirke den elektrokjemiske reaksjon og er typisk et alkalimetallklorid slik som natrium eller lithiumklorid, ved en egnet konsentrasjon på 0,2 - 0,7 mol/liter, og fortrinnsvis 0,5 mol/liter. The electrolyte is added to the organic or aqueous-organic medium to effect the electrochemical reaction and is typically an alkali metal chloride such as sodium or lithium chloride, at a suitable concentration of 0.2 - 0.7 mol/litre, and preferably 0.5 mol/ litres.

En egnet reaksjonstemperatur på reaksjonsmediet er mellom 5 og 40°C, fortrinnsvis 15 - 25°C. A suitable reaction temperature of the reaction medium is between 5 and 40°C, preferably 15 - 25°C.

Konsentrasjonen av 2-(2-nitrovinyl)-thiofen i reaksjonsmediet er mellom 1 g/l og 10 g/l, og fortrinnsvis mellom 1 g/l og 3 g/l. The concentration of 2-(2-nitrovinyl)-thiophene in the reaction medium is between 1 g/l and 10 g/l, and preferably between 1 g/l and 3 g/l.

Som arbeidselektrode for den elektrokjemiske celle anvendes et materiale med en høy hydrogenoverspenning, slik som kvikksølv, sink eller bly, og et kvikksølvlag foretrekkes. A material with a high hydrogen overvoltage, such as mercury, zinc or lead, is used as the working electrode for the electrochemical cell, and a mercury layer is preferred.

Andre trekk ved oppfinnelsen fremgår fra den etterføl-gende beskrivelse under henvisning til den medfølgende tegning. Other features of the invention appear from the following description with reference to the accompanying drawing.

Den elektrokjemiske reduksjon av 2-(2-nitrovinyl)-thiofen kan utføres i en celle slik som den som er vist på tegningen. The electrochemical reduction of 2-(2-nitrovinyl)-thiophene can be carried out in a cell such as that shown in the drawing.

Cellen 1 er oppdelt i et elektrolysekammer 2 og et ano-dekammer 3 som er adskilt av en porøs vegg 4, eksempelvis av sintret glass, for å sikre elektrisk ledning. En platina-eller grafittelektrode 5 tjener som en anode, mens elektroden 6 (eller arbeidselektroden) er anordnet ved bunnen eller nær bunnen i elektrolysekammeret. Cellen 1 er i dets kammer 2 utstyrt med en omrøringsanordning for reaksjonsmediet, som i den viste utførel-sesform er en magnetstav 7 anordnet i umiddelbar nærhet av bunnen av cellen. The cell 1 is divided into an electrolysis chamber 2 and an anode chamber 3 which are separated by a porous wall 4, for example of sintered glass, to ensure electrical conduction. A platinum or graphite electrode 5 serves as an anode, while the electrode 6 (or working electrode) is arranged at or near the bottom of the electrolysis chamber. The cell 1 is equipped in its chamber 2 with a stirring device for the reaction medium, which in the embodiment shown is a magnetic rod 7 arranged in the immediate vicinity of the bottom of the cell.

Cellen er også utstyrt med et inertgassinnløp 8 neden-for nivået av elektrolyttløsningen, og med et utløp 9 for gassen i lokket 10 av cellen. The cell is also equipped with an inert gas inlet 8 below the level of the electrolyte solution, and with an outlet 9 for the gas in the lid 10 of the cell.

En referanseelektrode 11 er plassert på utsiden av cellen for å forhindre forurensning med reduksjonsproduktene, idet den elektriske forbindelse skjer gjennom en bro 12 omfattende en treveisventil 13 og et rør 14 lukket med sintret glass som er dyppet ned i katodekammeret 2. A reference electrode 11 is placed on the outside of the cell to prevent contamination with the reduction products, the electrical connection being through a bridge 12 comprising a three-way valve 13 and a tube 14 closed with sintered glass which is immersed in the cathode chamber 2.

Det etterfølgende eksempel illustrerer oppfinnelsen. The following example illustrates the invention.

Eksempel Example

Den elektrokjemiske reduksjon av 2-(2-nitrovinyl)-thio-fen utføres i en celle inneholdende en platinaanode og arbeidselektroden eller katoden er et kvikksølvlag. The electrochemical reduction of 2-(2-nitrovinyl)-thiophene is carried out in a cell containing a platinum anode and the working electrode or cathode is a layer of mercury.

Reaksjonsmediet er en eddiksyre-vann (50:50) blanding og 0,5 molar lithiumklorid anvendes som elektrolytt. The reaction medium is an acetic acid-water (50:50) mixture and 0.5 molar lithium chloride is used as electrolyte.

Reduksjonspotensialet holdes ved 1,150 V i forhold til en mettet calomel elektrode, og reaksjonen utføres ved romtempe-ratur . The reduction potential is kept at 1.150 V in relation to a saturated calomel electrode, and the reaction is carried out at room temperature.

2-(2-nitrovinyl)-thiofenet tilsettes til det vandig-organiske medium ved en begynnelseskonsentrasjon på 2,5 g/l. The 2-(2-nitrovinyl)-thiophene is added to the aqueous-organic medium at an initial concentration of 2.5 g/l.

Cellen holdes under nitrogenatmosfære og reduksjonen utføres under omrøring ved å føre strømmen ved den på forhånd bestemte spenning. The cell is kept under a nitrogen atmosphere and the reduction is carried out with stirring by passing the current at the predetermined voltage.

Ved endt elektrolyse (etter passasje av 2500 coulomb) nøytraliseres elektrolytten i katodekammeret, ekstraheres med kloroform og vaskes deretter med vann og tørkes over vannfritt I^CO^. Det ønskede amin gjenvinnes som hydrokloridet eller oxa-latet i ethanol. At the end of electrolysis (after passage of 2500 coulombs), the electrolyte in the cathode chamber is neutralized, extracted with chloroform and then washed with water and dried over anhydrous I^CO^. The desired amine is recovered as the hydrochloride or oxalate in ethanol.

Utbyttet av 2-(2-aminoethyl)-thiofen er 47% på basis The yield of 2-(2-aminoethyl)-thiophene is 47% on a basis

av utgangsmaterialet. Dette utbytte svarer til Faradays utbytte, of the starting material. This yield corresponds to Faraday's yield,

da mengden av passert elektrisitet er den som svarer til en 100% overføring. as the amount of electricity passed is the one that corresponds to a 100% transfer.

Claims (8)

1. Fremgangsmåte ved fremstilling av 2-(2-aminoethyl)-thiofen av formel: karakterisert ved at 2-(2-nitrovinyl)-thiofen av formel: i et organisk eller vandig-organisk medium reduseres elektrokjemisk ved et potensial på 1,10-1,30 V, fortrinnsvis ved 1,15 V, målt i forhold til en mettet calomel referanseelektrode, i nærvær av et alkalimetallklorid i en konsentrasjon på1. Procedure for the production of 2-(2-aminoethyl)-thiophene of formula: characterized in that 2-(2-nitrovinyl)-thiophene of formula: in an organic or aqueous-organic medium is reduced electrochemically at a potential of 1.10-1.30 V, preferably at 1.15 V, measured relative to a saturated calomel reference electrode, in the presence of an alkali metal chloride at a concentration of 0,2-0,7 mol/l, fortrinnsvis 0,5 mol/l, som elektrolytt, og til-stedeværende ved en pH på 2 og en temperatur mellom 5 og 40°C, hvoretter det ønskede produkt utvinnes fra reaksjonsmediet.0.2-0.7 mol/l, preferably 0.5 mol/l, as electrolyte, and present at a pH of 2 and a temperature between 5 and 40°C, after which the desired product is recovered from the reaction medium. 2. Fremgangsmåte ifølge krav 1, karakterisert ved at 2-(2-aminoethyl)-thio-fenet utvinnes fra reaksjonsmediet ved hjelp av et organisk løs-ningsmiddel etter nøytralisering av elektrolytten.2. Method according to claim 1, characterized in that the 2-(2-aminoethyl)-thiophene is recovered from the reaction medium by means of an organic solvent after neutralization of the electrolyte. 3. Fremgangsmåte ifølge krav 1 eller 2, karakterisert ved at det som organisk eller vandig-organisk medium anvendes enten eddiksyre, methanol, dioxan eller blandinger derav med vann i en mengde på 20-70 vekt%.3. Method according to claim 1 or 2, characterized in that either acetic acid, methanol, dioxane or mixtures thereof with water in an amount of 20-70% by weight are used as organic or aqueous-organic medium. 4. Fremgangsmåte ifølge krav 3, karakterisert ved at det som medium anvendes en vann-eddiksyreblanding (50:50).4. Method according to claim 3, characterized in that a water-acetic acid mixture (50:50) is used as medium. 5. Fremgangsmåte ifølge hvilket som helst av de fore-gående krav, karakterisert ved at det som elektrode anvendes en kvikksølv-, sink- eller blykatode og en platina- eller grafittanode.5. Method according to any one of the preceding claims, characterized in that a mercury, zinc or lead cathode and a platinum or graphite anode are used as electrode. 6. Fremgangsmåte ifølge hvilket som helst av de fore-gående krav, karakterisert ved at det som ekstraksjonsløsningsmiddel anvendes kloroform.6. Method according to any one of the preceding claims, characterized in that chloroform is used as the extraction solvent. 7. Fremgangsmåte ifølge krav 1, karakterisert ved at reaksjonen utføres ved 15-25°C.7. Method according to claim 1, characterized in that the reaction is carried out at 15-25°C. 8. Fremgangsmåte ifølge krav 1, karakterisert ved at begynnelseskonsentrasjonen av 2-(2-nitrovinyl)-thiofen er 1-10 g/liter.8. Method according to claim 1, characterized in that the initial concentration of 2-(2-nitrovinyl)-thiophene is 1-10 g/litre.
NO790231A 1978-01-25 1979-01-24 PROCEDURE FOR ELECTRO-CHEMICAL PREPARATION OF 2- (2-AMINOETHYL) THIOPHEN. NO151715C (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7801992A FR2415671A1 (en) 1978-01-25 1978-01-25 PROCESS FOR PREPARING 2-AMINO 2-ETHYL-2-THIOPHENE BY ELECTROCHEMICAL METHOD

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NO790231L NO790231L (en) 1979-07-26
NO151715B true NO151715B (en) 1985-02-11
NO151715C NO151715C (en) 1985-05-22

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EP (1) EP0003446B1 (en)
JP (1) JPS6046190B2 (en)
AR (1) AR220736A1 (en)
AT (1) AT364839B (en)
BE (1) BE873677A (en)
CH (1) CH635618A5 (en)
DE (1) DE2960070D1 (en)
DK (1) DK151904C (en)
ES (1) ES476659A1 (en)
FI (1) FI62684C (en)
FR (1) FR2415671A1 (en)
GB (1) GB2013196B (en)
GR (1) GR65325B (en)
IE (1) IE47783B1 (en)
IT (1) IT1115135B (en)
LU (1) LU80772A1 (en)
MX (1) MX5460E (en)
NO (1) NO151715C (en)
PT (1) PT69105A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5191090A (en) * 1990-01-25 1993-03-02 Syntex (U.S.A.) Inc. Preparation of 2-(2'-thienyl)ethylamine derivatives and synthesis of thieno[3,2-c]pyridine derivatives therefrom
JP7229710B2 (en) 2018-09-26 2023-02-28 本田技研工業株式会社 VEHICLE CONTROL DEVICE, VEHICLE CONTROL METHOD, AND PROGRAM

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FR2299332A1 (en) * 1975-01-31 1976-08-27 Parcor PROCESS FOR PREPARING (THIENYL-2) -2-ETHYLAMINE AND ITS DERIVATIVES

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ATA38379A (en) 1981-04-15
CH635618A5 (en) 1983-04-15
AR220736A1 (en) 1980-11-28
FR2415671A1 (en) 1979-08-24
JPS54117462A (en) 1979-09-12
IE790112L (en) 1979-07-25
GB2013196B (en) 1982-06-23
ES476659A1 (en) 1979-05-16
JPS6046190B2 (en) 1985-10-15
AT364839B (en) 1981-11-25
DK151904B (en) 1988-01-11
LU80772A1 (en) 1979-05-16
PT69105A (en) 1979-02-01
IE47783B1 (en) 1984-06-13
FI62684C (en) 1983-02-10
FI62684B (en) 1982-10-29
EP0003446A1 (en) 1979-08-08
EP0003446B1 (en) 1980-11-26
GB2013196A (en) 1979-08-08
FI790121A (en) 1979-07-26
FR2415671B1 (en) 1981-11-20
GR65325B (en) 1980-08-11
NO151715C (en) 1985-05-22
DK151904C (en) 1988-06-06
DK13879A (en) 1979-07-26
BE873677A (en) 1979-07-24
IT7947735A0 (en) 1979-01-23
DE2960070D1 (en) 1981-02-12
IT1115135B (en) 1986-02-03
NO790231L (en) 1979-07-26
MX5460E (en) 1983-08-11

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