SK105998A3 - Method for producing aminoalkyl chlorides - Google Patents

Method for producing aminoalkyl chlorides Download PDF

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SK105998A3
SK105998A3 SK105998A SK105998A SK105998A3 SK 105998 A3 SK105998 A3 SK 105998A3 SK 105998 A SK105998 A SK 105998A SK 105998 A SK105998 A SK 105998A SK 105998 A3 SK105998 A3 SK 105998A3
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hydrochloride
thionyl chloride
chloride
chlorides
aminoalcohol
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SK105998A
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SK283256B6 (en
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Jozef Mokry
Vladimir Camaj
Jozef Pafco
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Novacke Chemicke Z A S
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Abstract

Disclosed is a production of amino alkyl chlorides and hydrochlorides thereof by the reaction of aminoalcohols, N-aminoalcohols, N,N-dialkyl aminoalcohols with thionylchloride and by thermic decomposition of the chloro sulfinic acid alkylester so that at first aminoalcohol hydrochloride is prepared and then by the effect of the thionylchloride the chloro sulfinic acid ester.

Description

Spôsob výroby aminoai koholev—y vA process for the production of amino acids

Oblasť technikyTechnical field

Vynález sa týka spôsobu prípravy aminoaikylchloridov, N-alky laminochloridov a/alebo N,N-dialkylaminochloridov a/alebo ich hydrochloridov substitúciou hydroxylovej skupiny aminoalkoholov, N-alkylaminoalkoholov a N,N-dialkylaminoalkoholov tionylchloridom pri miernych reakčných podmienkach.The invention relates to a process for the preparation of aminoalkyl chlorides, N-alkylaminochlorides and / or N, N-dialkylaminochlorides and / or their hydrochlorides by substituting the hydroxyl group of amino alcohols, N-alkylaminoalcohols and N, N-dialkylaminoalcohols with thionyl chloride under mild reaction conditions.

Dateraiží stav technikyThe prior art

Je známe, že príprava N,N-dietylaminoetylchloridu sa uskutočňuje reakciou N,N-dietylaminoetanolu s mólovým nadbytkom tionylchloridu v pomere 2 až 2,5 : 1, v prostredí toluénu za účinného chladenia, pri teplote 0 až 10°C , pričom po nadávkovaní tionylchloridu v priebehu 2 hodín nasleduje -kľudová fáza v časovom intervale 13 až 15 hodín pri teplote 10 až 30°C. Potom nasleduje fáza rozkladu pri teplote 75 až SO°C, vydestilovanie nezreagovaného tionylchloridu s časťou toluénu a nakoniec izolácia N,N-dietylaminoetylchloridu hydrochloridu (Rum.pat. 67572 (197?)).It is known that the preparation of N, N-diethylaminoethyl chloride is carried out by reacting N, N-diethylaminoethanol with a molar excess of thionyl chloride in the ratio of 2 to 2.5: 1, in toluene under efficient cooling, at 0 to 10 ° C. thionyl chloride over a period of 2 hours followed by a resting phase of 13-15 hours at 10-30 ° C. This is followed by a decomposition phase at 75 to 50 ° C, distillation of unreacted thionyl chloride with some toluene, and finally isolation of N, N-diethylaminoethyl chloride hydrochloride (Rum. Pat. 67572 (197?)).

Iný spôsob uprednostňuje prípravu aminochlórderivátov cez hydrochloridy, reakciou aminoalkoholov s kyselinou chlorovodíkovou o koncentrácii 25 až 36X hmôt., v prostredí vody a toluénu a po následnom azeotropickom vydestilovaní vody pokračuje chloráciou s malým nadbytkom 0,2 mol.tionylchloridu, potrebného na krytie strát v dôsledku úniku s plynnými splodinami, predovšetkým oxidom siričitým (Rum.pat. 55946 (1973)).Another method favors the preparation of aminochloro derivatives via hydrochlorides, by reacting amino alcohols with hydrochloric acid at a concentration of 25 to 36X by weight, in water and toluene, and then azeotropically distilling off the water followed by chlorination with a small excess of 0.2 mol of thionyl chloride needed to cover losses releases with gaseous fumes, in particular sulfur dioxide (Rum.pat. 55946 (1973)).

Chloráciu alkoholov možno uskutočniť aj priamo chlorovodíkom avšak za podstatne tvrdších podmienok a s obmedzením použitia hlavne pre nízke primárne alkoholy Ci až C4 (USA pat. 4935564 (1990)).Chlorination of alcohols can also be carried out directly with hydrogen chloride, but under considerably tougher conditions and with limited use mainly for C 1 -C 4 primary alcohols (U.S. Pat. No. 4,935,564 (1990)).

Podstata vynálezuSUMMARY OF THE INVENTION

Podľa tohto vynálezu sa spôsob prípravy aminoalkylchloridov a/alebo ich hydrochloridov všeobecného vzorcaAccording to the invention, a process for the preparation of aminoalkyl chlorides and / or their hydrochlorides of the general formula

Ri*».Ri ».

N - ft3- Cl N - R3- C1.HC1N - ft 3 - Cl N - R 3 - C1.HCl

Ra ftZRa ftZ

Kde Ria Ra môže byť —H, —CH3 , —Carls, izo-Cs(-17 , — C3H7 a R3 môže byťWhere R 1a R a can be —H, —CH 3, —Carls, iso-C 8 (-17, -C 3 H 7, and R 3 can be

-CHa-, -Cal-U-, -C3Hô- z. aminoalkoholov, N-alkylaminoalkohlov, N,N -dialkylaminoalkoholov a tionylchloridu uskutočňuje tak, že z aminoalkoholu sa najprv reakciou v bezvodom prostredí so suchým plynným chlorovodíkom do slabokyslej reakcie, na pH 5,5 až 6,5 , pri mólovom pomere aminoalkohol : chlorovodík í : 1,002 až 1,3 , pri teplote 25 až 35°C a atmosférickom tlaku a v intenzívne miešanej sústave s počtom otáčok 400 až 600 /min pripraví hydrochlorid aminoalkoholu, a až potom nasleduje reakcia s tionylchloridom na komplex alkylester kyseliny chlórsulfínovej a jeho termický rozklad na aminoalkylchlorid a/alebo aminoalkylchlorid hydrochlorid.-CHa-, -Cal-U-, -C3H6- z. of aminoalcohols, N-alkylaminoalcohols, N, N-dialkylaminoalcohols and thionyl chloride is carried out by first reacting from the aminoalcohol in an anhydrous medium with dry hydrogen chloride gas to a weakly acidic reaction, to a pH of 5.5 to 6.5, at a molar ratio of aminoalcohol: hydrogen chloride; : 1.002 to 1.3, at 25 to 35 ° C and atmospheric pressure and in a vigorously stirred system at 400 to 600 rpm, prepares the amino alcohol hydrochloride, followed by reaction with thionyl chloride to form the chlorosulfinic acid alkyl ester complex and its thermal decomposition to give aminoalkyl chloride and / or aminoalkyl chloride hydrochloride.

Výhodou postupu prípravy chlórderivátov z aminoalkoholov a/alebo N-substituovaných aminoalkoholov podľa tohto vynálezu je predovšetkým jednoduché uskutočnenie reakcie pri miernych reakčných podmienkach spočívajúce v tom, že všetky reakčné stupne sa realizujú jednofázovo, bez izolácie medziproduktov, s takmer stechiometrickým pomerom reagujúcich zložiek. Ďaľšou výhodou je podstatné skrátenie reakčnej doby, vysoká výťažnosť produktu 97Z t 2 a šetrenie východiskového tionylchloridu. V neposlednom rade je to vysoká kvalita produktu bez vedľajších látok a farebných nečistôt, dosiahnutá aj bez zaradenia zdĺhavých a nákladných separačných a Čistiacich operácii.The advantage of the process for preparing chloro derivatives from amino alcohols and / or N-substituted amino alcohols according to the invention is, in particular, that the reaction can be carried out under mild reaction conditions in that all reaction steps are carried out in a single phase without isolation of intermediates with almost stoichiometric ratios. Another advantage is a substantial reduction in the reaction time, a high yield of the product 97Z t 2 and the saving of the starting thionyl chloride. Last but not least, it is the high quality of the product without any side-effects and color impurities, achieved even without the inclusion of lengthy and costly separation and cleaning operations.

V prvom stupni reakcie aminoalkoholu na hydrochlorid je dôležité zabezpečiť nielen iOOX-nú konverziu, ale súčasne zamedziť nežiadúcemu nadbytku chlorovodíka nad môlový pomer aminoalkohol : plynný chlorovodík 1,3 : 1, s výhodou 1,005 až 1,075 : 1. Nedostatok chlorovodíka zapríčiňuje nárast teploty v druhom stupni reakcie aminoalkoholu hydrochloridu s tionylchloridom v dôsledku exotermickej reakcie HCL in situ na volný aminoalkohol, čím sa, v krajnom prípade, môže dosiahnúť až teplota rozkladu komplexu kyseliny chlórsulfínovej. Naopak, nadbytok chlorovodíka vyšší ako 0,3 mólu vedie k tvorbe polyhydrochloridov a silno kyslé prostredie má negatívny vplyv na priebeh termického rozkladu a tiež na kvalitu produktu, predovšetkým na obsah farebných nečistôt, kryštalinitu a výťažnosť.In the first stage of the reaction of the aminoalcohol to the hydrochloride, it is important to ensure not only a 100X conversion, but at the same time avoid undesired excess hydrogen chloride above the molar ratio of aminoalcohol: hydrogen chloride of 1.3: 1, preferably 1.005 to 1.075: 1. of the reaction of the aminoalcohol hydrochloride with thionyl chloride as a result of the exothermic reaction of HCL in situ to the free aminoalcohol so that, as a last resort, the decomposition temperature of the chlorosulphonic acid complex can be reached. Conversely, excess hydrogen chloride above 0.3 mole leads to the formation of polyhydrochlorides and the strongly acidic environment has a negative effect on the course of thermal decomposition and also on the quality of the product, especially the content of color impurities, crystallinity and yield.

Z hydroxyzlúčenín sú na prípravu chlórderivátov podľa tohto vynálezu vhodné predovšetkým aminoalkoholy napr. etanolamín, izopropanolamín, butanolamín, ďalej N-alkylsubstituované a N,N-dialkylsubstituované aminoalkoholy, napr. N-metylaminoetanol, N-etylaminoetanol, N-etylaminopropanol, N,N-dimetylaminoetanol, N,N-dietylaminoetanol a mnohé ďaľšie.Of the hydroxy compounds, aminoalcohols, e.g. ethanolamine, isopropanolamine, butanolamine, further N-alkyl substituted and N, N-dialkyl substituted amino alcohols, e.g. N-methylaminoethanol, N-ethylaminoethanol, N-ethylaminopropanol, N, N-dimethylaminoethanol, N, N-diethylaminoethanol and many others.

Ako chloračné činidlo sa používa predovšetkým tionylchlorid alebo chlorid fosforitý v nevodnom prostredí inertného média ako je benzén, toluén, chlorid uhličitý, dichloretán a iné v takom množstve, aby vzniknutá suspenzia hydrochloridu obsahovala 8,0 až 30,0Z hmôt. pevnej fázy.The chlorinating agent used is preferably thionyl chloride or phosphorus trichloride in a non-aqueous medium of an inert medium such as benzene, toluene, carbon tetrachloride, dichloroethane and others in an amount such that the resulting hydrochloride suspension contains 8.0 to 30.0% by weight. solid phase.

Príklady, uskutočnenia vynálezuExamples, embodiments of the invention

Príklad 1Example 1

Do štvorhrdlovej sulfonačnej banky objemu 2 Súúcm3 , opatrenej miešadlom, prívodom chlorovodíka, spätným chladičom a teplomerom sa nadávkuje 700cm3 toluénu a 89, lg dimetylaminoetanolu. Do zmesi sa za chladenia privádza cez okalibrovanú kapiláru suchý plynný chlorovodík v množstve 39,5g na výsledné pH ó,5 pri teplote 31°C ±2 v priebehu 1 hodiny. Potom sa zvýši teplota na 52QC a v priebehu 25 min. sa nadávkuje 132g tionylchloridu tak,aby občasným chladením teplota neprestúpila 56°C. Po ukončení dávkovania tionylchloridu sa obsah postupne vyhreje v priebehu l,2h na teplotu llO^C, pričom termický rozklad komplexu je sprevádzaný búrlivým vývojom plynných splodín oxidu siričitého a chlorovodíka, ktoré sa odvádzajú do odplynu. Rozkladná teplota komplexu je 60*C ±2. V priebehu rozkladu sa vytvára suspenzia kryštálov dimetylaminoetylchlorid hydrochloridu (DMAEC.HC1), ktorý sa po ochladení na 30°C izoluje filtráciou, dvojnásobnou dekantáciou 30 cm3 toluénu a vysušením v sušiarni pri teplote 70<>C. Výťažok DMAEC.HC1 je 141,5g, čo predstavuje 98,3% teórie, má obsah 99,5Xhmôt.hydrochloridu a teplotu topenia 208,6°C.700 cm @ 3 of toluene and 89 .mu.g of dimethylaminoethanol are metered into a 4 -neck 2-inch 3- volume sulfonation flask equipped with a stirrer, hydrogen inlet, reflux condenser and thermometer. While cooling, dry hydrogen chloride gas (39.5 g) is passed through the calibrated capillary to a final pH of 6.5 at 31 ° C ± 2 over 1 hour. Then increase the temperature to 52 Q C and over 25 minutes. 132 g of thionyl chloride are metered in so that the temperature does not exceed 56 ° C by occasional cooling. Upon completion of the thionyl chloride feed, the contents were gradually heated to 110 ° C over a period of 1.2 hours, the thermal decomposition of the complex being accompanied by a vigorous evolution of the gaseous fumes of sulfur dioxide and hydrogen chloride, which were vented to the off-gas. The decomposition temperature of the complex is 60 ° C ± 2. During the decomposition, a suspension of crystals of dimethylaminoethyl chloride hydrochloride (DMAEC.HCl) is formed which, after cooling to 30 ° C, is isolated by filtration, twice decanting 30 cm 3 of toluene and drying in an oven at 70 ° C. The yield of DMAEC.HCl is 141.5 g, which is 98.3% of theory, and has a content of 99.5% by weight of hydrochloride and a melting point of 208.6 ° C.

Príklad 2Example 2

Postupom, uvedeným v príklade 1, sa diétylaminoetanol hydrochlorid pripraví zo 117,2g diétylaminoetanolu v 600cm3 toluénu, sýtením 47,5g plynného chlorovodíka do dosiahnutia hodnoty pH 5,5 pri teplote 32 ±3°C v priebehu l,3h. Potom sa teplota zvýši na 60°C a v priebehu 30 min. sa pridá 144g tionylchloridu. Postupným vyhriatím na teplotu 115°C v priebehu 2h sa uskutoční termický rozklad komplexu na DEAEC.HC1. Získa sa 154,9g, čo predstavuje 90,01% teórie. Diétylaminoetylchlorid hydrochlorid (DEAEC.HC1) je slabo žltá kryštalická látka, obsahujúca 97,1% hmôt. hydrochloridu a teplotu topenia má 207,3°C.Using the procedure described in Example 1, diethylaminoethanol hydrochloride is prepared from 117.2 g of diethylaminoethanol in 600 cm @ 3 of toluene, saturated with 47.5 g of hydrogen chloride gas until a pH of 5.5 is reached at 32 ± 3 ° C over 1.3 h. The temperature is then raised to 60 ° C and within 30 min. 144 g of thionyl chloride are added. Gradual heating to 115 ° C over 2h provides thermal decomposition of the complex to DEAEC.HCl. 154.9 g is obtained, which is 90.01% of theory. Diethylaminoethyl chloride hydrochloride (DEAEC.HCl) is a pale yellow crystalline substance containing 97.1% by weight. hydrochloride and melting point 207.3 ° C.

Príklad 3Example 3

- Do 61,ú8g monoetanolamínu v 500 cm3toluénu sa privádza 40,15g plynného chlorovodíka v priebehu lh pri teplote 28 až 32°C, do dosiahnutia hodnoty pH 6,0. Potom sa zvýši teplota na 45<*C · a v priebehu 15 min. sa nadávkuje 132g tionylchloridu.Termický rozklad sa uskutoční postupným zvyšovaním teploty na 105oC v priebehu l,3h. Získaný aminoetylchlorid hydrochlorid je bezfarebná kryštalická látka, s obsahom 97,6% hydrochloridu, s teplotou topenia 144,5^8. Výťažok je IQB.feg, čo predstavuje 93,6% teórie.61.15 g of monoethanolamine in 500 cm @ 3 of toluene are charged with 40.15 g of hydrogen chloride gas over a period of 1 h at a temperature of 28 to 32 DEG C., until a pH of 6.0 is reached. The temperature is then raised to 45 ° C and within 15 min. The thermal decomposition is carried out by gradually raising the temperature to 105 ° C over a period of 1.3 hours. The aminoethyl chloride hydrochloride obtained is a colorless crystalline substance, containing 97.6% hydrochloride, m.p. 144.5-8. Yield: IQB.feg, which represents 93.6% of theory.

Priemyselná využiteľnostíIndustrial usability

Aminoalkylchloridy sa pouäívajú vo farmaceutickom priemysle na výrobu liečiv.Aminoalkyl chlorides are used in the pharmaceutical industry for the manufacture of pharmaceuticals.

Claims (2)

PATENTOVÉ NÁROKYPATENT CLAIMS 1 Spôsob výroby aminoalky lch'loridov, všeobecného vzorca1 A process for the preparation of aminoalkyl chlorides of general formula N - Rs - C1 , kde R± a Ra sú -H, -CHs, -C2H5, -C3H7 alebo RsN - R 5 - C 1 where R 5 and R a are -H, -CH 3, -C 2 H 5, -C 3 H 7 or R 5 ÍZO-C3H7 a Rs je -CHa-, -CbHa-, alebo -C3H*-, alebo ich hydRix rochloridov ^N - R3- C1.HC1, reakciou aminoalkoholov, N-alRa kylaminoalkoholov alebo N,N-dialkylaminoalkoholov s tionylchloridom a termickým rozkladom alkylesteru kyseliny chlorsul f í novej vyznačujúci sa tým, že v bezvodom prostredí sa najskôr pripraví hydrochlorid aminoalkoholu,a potom, pôsobením tionylchloridu, alkylester kyseliny chlorsulfínovej.IsO-C3H7 and R5 is -CH and -, -CbHa-, or -C3H * -, or their HydRix chlorides N-R3-C1HCl, by reaction of amino alcohols, N-alRa-cylaminoalcohols or N, N-dialkylaminoalcohols with thionyl chloride and by thermal decomposition of the chlorosulfinic acid alkyl ester, characterized in that the aminoalcohol hydrochloride is first prepared in an anhydrous medium, and then, by treatment with thionyl chloride, an alkyl chlorosulphonic acid ester. 2 Spôsob výroby podľa bodu 1 vyznačujúci sa tým,Se sa uskutočňuje pri intenzívnom miešaní, teplote 25 až 35°C a pH 5,5 až 6,5 so suchým plynným chlorovodíkom, pričom mólový pomer aminoalkohol : chlorovodík je 1 : 1,002 až 1,3.2. The process according to claim 1, wherein Se is carried out with vigorous stirring, at a temperature of 25-35 [deg.] C. and a pH of 5.5-6.5 with dry hydrogen chloride gas, wherein the molar ratio of aminoalcohol: hydrogen chloride is 1: 1.002-1. third
SK1059-98A 1998-08-06 1998-08-06 Process for production of amino alkyl chlorides SK283256B6 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103408432A (en) * 2013-07-01 2013-11-27 昆山三友医药原料有限公司 Synthetic process of 2-dimethylaminoethyl chloride hydrochloride

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103408432A (en) * 2013-07-01 2013-11-27 昆山三友医药原料有限公司 Synthetic process of 2-dimethylaminoethyl chloride hydrochloride

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