SK283256B6 - Process for production of amino alkyl chlorides - Google Patents
Process for production of amino alkyl chlorides Download PDFInfo
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- SK283256B6 SK283256B6 SK1059-98A SK105998A SK283256B6 SK 283256 B6 SK283256 B6 SK 283256B6 SK 105998 A SK105998 A SK 105998A SK 283256 B6 SK283256 B6 SK 283256B6
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Abstract
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Oblasť technikyTechnical field
Vynález sa týka spôsobu prípravy aminoalkylchloridov, N-alkylaminochloridov a/alebo Ν,Ν-dialkylaminochIoridov, 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 Ν, Ν-dialkylamino chlorides, 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.
Doterajší stav technikyBACKGROUND OF THE INVENTION
Je známe, že príprava Ν,Ν-dietylaminoetylchloridu sa uskutočňuje reakciou Ν,Ν-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 „pokojová fáza“ v časovom intervale 13 až 15 hodín pri teplote 10 až 30 °C. Potom nasleduje fáza rozkladu pri teplote 75 až 80 °C, vydestilovanie nezreagovaného tionylchloridu s časťou toluénu a nakoniec izolácia Ν,Ν-dietylaminoetylchloridu hydrochloridu (rum. pat. 67572 (1979)). Iný spôsob uprednostňuje prípravu aminochlórderivátov cez hydrochloridy, reakciou aminoalkoholov s kyselinou chlorovodíkovou s koncentráciou 25 až 36 % hmotn., 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)).It is known that the preparation of Ν, Ν-diethylaminoethyl chloride is carried out by reacting Ν, etan-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 "quiescent phase" of 13-15 hours at 10-30 ° C. This is followed by a decomposition phase at 75-80 ° C, distillation of unreacted thionyl chloride with some toluene, and finally isolation of Ν, Ν-diethylaminoethyl chloride hydrochloride (rum. Pat. 67572 (1979)). Another method favors the preparation of aminochloro derivatives via hydrochlorides, by reacting amino alcohols with hydrochloric acid at a concentration of 25 to 36% by weight, in a water / toluene medium, and following azeotropic distillation of water, proceeds with chlorination with a small excess of 0.2 mol. thionyl chloride required to cover losses due to leakage with gaseous products, in particular sulfur dioxide (rum. pat. 55946 (1973)).
Chloráciu alkoholov možno uskutočniť aj priamo chlorovodíkom, ale za podstatne tvrdších podmienok a s obmedzením použitia hlavne pre nízke primárne alkoholy C, 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, especially for low primary alcohols C 1 to C 4 (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
Rt'. RixR '. Rix
N - Rj- Cl N - R3- C1.HC1N - R 1 - Cl N - R 3 - C 1 .HCl
Ra R/ kde R1 a R2 môže byť -H, -CH3, -C2H5, izo-C3H7,-C3H7 a R3 môže byť -CH2-, -C2H4-, -C3H6- z aminoalkoholov, N-alkylaminoalkoholov, Ν,Ν-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 1 : 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.R a where R 1 and R 2 can be -H, -CH 3, -C 2 H 5, iso-C 3 H 7 , -C 3 H 7, and R 3 can be -CH 2 -, -C 2 H 4 -, -C 3 H 6 - from amino alcohols , N-alkylaminoalcohols, Ν, dial-dialkylaminoalcohols and thionyl chloride are 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 an amino alcohol: hydrogen chloride molar ratio of 1: 1,002 to 1,3, at a temperature of 25 to 35 ° C and atmospheric pressure and in a vigorously stirred system with a speed of 400 to 600 / min. to prepare the aminoalcohol hydrochloride, followed by reaction with thionyl chloride to form the chlorosulphonic acid alkyl ester complex and its thermal decomposition to 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 jednorázovo, bez izolácie medziproduktov, s takmer stechiometrickým pomerom reagujúcich zložiek. Ďalšou výhodou je podstatné skrátenie reakčnej doby, vysoká výťažnosť produktu 97 % +2 a šetrenie východiskového tionylchloridu. V neposled nom rade je to vysoká kvalita produktu bez vedľajších látok a farebných nečistôt, dosiahnutá aj bez zaradenia zdĺhavých a nákladných separačných a čistiacich operácií.An advantage of the process for the preparation of 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 step without isolation of intermediates with almost a stoichiometric ratio of reactants. Another advantage is a substantial reduction in the reaction time, a high yield of the product of 97% +2 and the saving of the starting thionyl chloride. Last but not least, it is the high quality of the product, free of by-products and color impurities, also achieved without the inclusion of lengthy and costly separation and cleaning operations.
V prvom stupni reakcie aminoalkoholu na hydrochlorid je dôležité zabezpečiť nielen 100 %-nú konverziu, ale súčasne zamedziť nežiadúcemu nadbytku chlorovodíka nad mólový pomer aminoalkohol : plynný chlorovodík 1,3 : 1, výhodne 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 voľný aminoalkohol, čím sa, v krajnom prípade, môže dosiahnuť 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. 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, Ν,Ν-dietylaminoetanol a mnohé ďalšie.In the first stage of the reaction of the aminoalcohol to the hydrochloride, it is important to ensure not only 100% conversion, but at the same time avoid undesirable excess of 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 HCL reaction "in situ" to the free aminoalcohol, whereby, as a last resort, the decomposition temperature of the chlorosulfic 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. Of the hydroxy compounds, amino alcohols, 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, Ν, Ν-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, dichlóretán a iné v takom množstve, aby vzniknutá suspenzia hydrochloridu obsahovala 8,0 až 30,0 % hmotn. 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 wt. solid phase.
Príklady uskutočnenia vynálezuDETAILED DESCRIPTION OF THE INVENTION
Príklad 1Example 1
Do štvorhrdlovej sulfonačnej banky objemu 2500 cm3, vybavenej miešadlom, prívodom chlorovodíka, spätným chladičom a teplomerom sa nadávkuje 700 cm3 toluénu a 89,1 g dimetylaminoetanolu. Do zmesi sa za chladenia privádza cez okalibrovanú kapiláru suchý plynný chlorovodík v množstve 39,5 g na výsledné pH 6,5 pri teplote 31 °C ±2 v priebehu 1 hodiny. Potom sa zvýši teplota na 52 °C a v priebehu 25 min. sa nadávkuje 132 g tionylchloridu tak, aby občasným chladením teplota neprestúpila 56 °C. Po ukončení dávkovania tionylchloridu sa obsah postupne vyhreje v priebehu 1,2 h na teplotu 110 °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 . HCI), ktorý sa po ochladení na 30 °C izoluje filtráciou, dvojnásobnou dekantáciou 30 cm3 toluénu a vysušením v sušiarni pri teplote 70 °C. Výťažok DMAEC . HCI je 141,5 g, čo predstavuje 98,3 % teórie, má obsah 99,5 % hmotn. hydrochloridu a teplotu topenia 208,6 °C.700 cm 3 of toluene and 89.1 g of dimethylaminoethanol are metered into a 2500 ml 3 four-necked sulphonation 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. The temperature is then raised to 52 ° C and within 25 min. 132 g of thionyl chloride are metered in so that the temperature does not exceed 56 ° C by occasional cooling. Upon completion of thionyl chloride dosing, the contents were gradually heated to 110 ° C over a period of 1.2 h, the thermal decomposition of the complex being accompanied by a vigorous evolution of gaseous sulfur dioxide and hydrogen chloride gas, 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. DMAEC yield. HCl is 141.5 g, which represents 98.3% of theory, has a content of 99.5% by weight. hydrochloride, m.p. 208.6 ° C.
Príklad 2Example 2
Postupom uvedeným v príklade 1 sa dietylaminoetanol hydrochlorid pripraví zo 117,2 g dietylaminoetanolu v 600 cm3 toluénu, sýtením 47,5 g plynného chlorovodíka do dosiahnutia hodnoty pH 5,5 pri teplote 32 ±3 °C v priebehu 1,3 h. Potom sa teplota zvýši na 60 °C a v priebehu 30 min. sa pridá 144 g tionylchloridu. Postupným vyhriatím na teplotu 115 °C v priebehu 2 h sa uskutoční termický rozklad komplexu na DEAEC . HCI. Získa sa 154,9 g, čo predstavuje 90,01 % teórie. Dietylaminoetylchlorid hydrochlorid (DEAEC . HC1) je slabožltá kryštalická látka, obsahujúca 97,1 % hmotn. hydrochloridu a teplotu topenia má 207,3 °C.Using the procedure of 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 2 h provides thermal decomposition of the complex to DEAEC. HCI. 154.9 g (90.01% of theory) are obtained. Diethylaminoethyl chloride hydrochloride (DEAEC, HCl) is a pale yellow crystalline substance containing 97.1 wt. hydrochloride and melting point 207.3 ° C.
Príklad 3Example 3
Do 61,08 g monoetanolamínu v 500 cm3 toluénu sa privádza 40,15 g plynného chlorovodíka v priebehu 1 h 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 132 g tionylchloridu. Termický rozklad sa uskutoční postupným zvyšovaním teploty na 105 °C v priebehu 1,3 h. Získaný aminoetylchlorid hydrochlorid je bezfarebná kryštalická látka s obsahom 97,6 % hydrochloridu, s teplotou topenia 144,5 °C. Výťažok je 108,6 g, čo predstavujeTo 61.08 g of monoethanolamine in 500 cm @ 3 of toluene is added 40.15 g of hydrogen chloride gas over a period of 1 hour 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. 132 g of thionyl chloride are metered in. Thermal decomposition is carried out by gradually raising the temperature to 105 ° C over 1.3 h. The aminoethyl chloride hydrochloride obtained is a colorless crystalline substance with a 97.6% hydrochloride content, m.p. 144.5 ° C. Yield: 108.6 g
93,6 % teórie.93.6% of theory.
Priemyselná využiteľnosťIndustrial usability
Aminoalkylchloridy sa používajú vo farmaceutickom priemysle na výrobu liečiv.Aminoalkyl chlorides are used in the pharmaceutical industry for the manufacture of pharmaceuticals.
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