CS253429B1 - Process for preparing 2-isopropylamino-4-ethylamino-6-chlor-s-triazine - Google Patents
Process for preparing 2-isopropylamino-4-ethylamino-6-chlor-s-triazine Download PDFInfo
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Abstract
Rieši sa výroba 2-izopropylamíno-4-etylamíno-6-chlór-s-triazínu kondenzáciou kyanurchloridu s etylamínom, izopropylamínom a hydroxidom sodným. Kondenzácia sa prevádza vo vodnom prostředí s prídavkom chloridu alkalického kovu, najčastejšie chloridu sodného. Po ukončení reakcie sa trazín z reákčnej zmesi odfiltruje a spracuje běžným sposobom. 2-izopropylamíno-4-etylamíno-6-chlór-s- -triazín sa používá ako herbicid v pofnohospodárstve.Production of 2-isopropylamino-4-ethylamino-6-chloro-s-triazine is solved condensation of cyanuric chloride with ethylamine, isopropylamine and sodium hydroxide. Condensation is carried out in an aqueous medium with addition of alkali metal chloride, most commonly sodium chloride. After completion of The reaction was filtered to remove trazine from the reaction mixture and processed by conventional means. 2-isopropylamino-4-ethylamino-6-chloro- -triazine is used as a herbicide in agriculture.
Description
Vynález rieši výrobu 2-izopropylamíno-4-etylamíno-6-chlór-s-triazínu reakciou kyanurchloridu s etylamínom, izopropylamínom a hydroxidom sodným vo vúdnom prostředí s prídavkom chloridu alkalického kovu.The present invention provides the preparation of 2-isopropylamino-4-ethylamino-6-chloro-s-triazine by reacting cyanuric chloride with ethylamine, isopropylamine and sodium hydroxide in an aqueous medium with the addition of an alkali metal chloride.
Medzi najznámejšie a najviac vyrábané s-triazínové herbicidy patří 2-izopropylamíno-4-etylamíno-6-chlór-s-triazín (atrazín). Herbicídne účinky boli objavené v roku 1954 vo Švajčiarsku a sú popísané v švajčiarskom patente 229 227. Příprava atrazínu reakciou kyanurchloridu, etylaminů, izopropylamínu a hydroxidu sodného vo vodnochlórbenzénovo-m prostředí je popísaná v československom patente 110 352. Příprava atrazínu reakciou kyanurchloridu a etylaminů, izopropylamínu v prostředí bezvodého organického rozpúšťadla, pričom na viazanie vzniklého chlorovodíka sa použije bezvodého amoniaku popisuje švajčiarsky patent 508 640. Získaný produkt obsahuje 92 % atrazínu. Vplyv hodnoty pH na výťažok atrazínu popisujú patentové spisy NDR a NSR. Podlá NDR pat. 51 646 sa najlepší výťažok d-osiahne vtedy, ak v prvom reakčnom stupni, t. j. po- přidaní prvého aminu a hydroxidu alkalického kovu sa udržuje hodnota pH 6 až 8, v druhom reakčnom stupni, t. j. po přidaní druhého aminu a hydroxidu alkalického kovu sa udržuje hodnota pH na 8,5 — 9. Výťažok atrazínu je 96 °/o. V NSR patente čísloAmong the best known and most widely produced s-triazine herbicides are 2-isopropylamino-4-ethylamino-6-chloro-s-triazine (atrazine). Herbicidal effects were discovered in Switzerland in 1954 and are described in Swiss Patent 229 227. The preparation of atrazine by reaction of cyanuric chloride, ethylamines, isopropylamine and sodium hydroxide in aqueous chlorobenzene is described in Czechoslovak patent 110,352. in anhydrous organic solvent, wherein anhydrous ammonia is used to bind the resulting hydrogen chloride. Swiss Patent 508,640 is disclosed. The product obtained contains 92% atrazine. The effect of pH on atrazine yield is described in the patents NDR and NSR. According to the GDR Pat. 51,646, the best yield d-is obtained if, in the first reaction step, i.e.. j. by adding the first amine and the alkali metal hydroxide, a pH of 6 to 8 is maintained in the second reaction stage, i.e. the reaction is carried out at a pH of 6 to 8; j. after addition of the second amine and alkali metal hydroxide, the pH is maintained at 8.5-9. The atrazine yield is 96%. In the German patent no
032 861 sa udává hodnota pH v prvom stupni 6,5 — 10. V USA pat. 3 328 399 a číslo032 861 gives a pH of 6.5-10 in the first stage. U.S. Pat. No. 3 328 399 and no
586 679 je popísaný sposob přípravy atrazínu z kyanurchloridu, etylaminů, izopropylamínu v bezvodno-m prostředí pri teplote 120 — 170 °C za oddestilovania vzniknutého chlorovodíka. Výhoda spůsobu je, že odpadne problém odpadných vod s obsahom minerálnych solí. V švajčiarskom patente č. 546 247 sa popisuje adiobotický sposob výroby atrazínu vo vodonerozpustnom rozpúšťadle reakciou etylaminů, izopropylamínu, alkalického hydroxidu s kyanurchloridom. Vo franeúzkom patente 2 296 628, rumunském patente 68 016, japonskom patente č. 131 592 (1977) sa doporučuje pri dávkovaní amínov pri výrobě atrazínu dávkovat prvý izopropylamín. Banks C. a spo-1 J. Am. Chem. Soc. BB, 1771 (1944) a Friedheim E., J. Am. Chem. Soc. 6B 1725 (1944) doporučujú pri prvom reakčnom stupni výroby atrazínu teplotu okolo 0 °C a druhý reakčný stupeň pri teplotách 30 až 50 °C. Pri prvom reakčnom stupni sa ako reakčné prostredie používá zmes vody a 1'adu, připadne voda, l'ad a organické rozpúšťadlo.No. 586,679 describes a process for preparing atrazine from cyanuric chloride, ethylamines, isopropylamine in anhydrous medium at a temperature of 120-170 ° C while distilling off the resulting hydrogen chloride. The advantage of the method is that the problem of waste waters containing mineral salts is eliminated. In Swiss patent no. No. 546,247 describes an adiobotic process for producing atrazine in a water-insoluble solvent by reacting ethylamines, isopropylamine, alkali hydroxide with cyanuric chloride. In French Patent 2,296,628, Romanian Patent 68,016, Japanese Patent no. 131 592 (1977), it is recommended that the first isopropylamine be metered in at amine dosing for atrazine production. Banks C. and spo-1 J. Am. Chem. Soc. BB, 1771 (1944) and Friedheim E., J. Am. Chem. Soc. 6B 1725 (1944) recommends a temperature of about 0 ° C in the first reaction stage of atrazine production and a second reaction stage at temperatures of 30 to 50 ° C. In the first reaction step, a mixture of water and ice is used as the reaction medium, optionally water, ice and an organic solvent.
Nevýhodou vyššie uvedených postupov- je, že kondenzácia prebieha v přítomnosti organického rozpúšťadla, ktoré sa musí po ukončení kondenzácie od produktu oddělit.A disadvantage of the above processes is that the condensation takes place in the presence of an organic solvent which must be separated from the product after the condensation has been completed.
Vyššie uvedené nedostatky sú zmiernené spůsobom výroby 2-izopropylamíno-4-etylamíno-6-chlór-s-triazínu, podstata ktorého spočívá v tom, že zreaguje kyanurchlorid s vodnými roztokmi etylaminů, izopropylamínu a hydroxidu sodného. Reakcia prebieha vo vodnom prostředí s prídavkom chloridu alkalického kovu, najčastejšie chloridu sodného.The above-mentioned drawbacks are alleviated by the process for the preparation of 2-isopropylamino-4-ethylamino-6-chloro-s-triazine, which consists in reacting cyanuric chloride with aqueous solutions of ethylamines, isopropylamine and sodium hydroxide. The reaction takes place in an aqueous medium with the addition of an alkali metal chloride, most often sodium chloride.
Výhodou podl'a vynálezu je, že ako- reakčné prostredie sa použije voda s prídavkom alkalického chloridu. Po ukončení reakcle sa atrazín z reakčnej zmesi odfiltruje a chloridy alkalického kovu sa vymyjú s vodou. Postup je omnoho jednoduchší ako pri použití organického rozpúšťadla, ktoré je potřebné regenerovat, čo si vyžaduje veta energie. Prídavkom chloridu alkalického kovu k vodnému prostrediu sa znižuje teplota tuhnutia vodných roztokov-, čo- je výhodné hlavně pri reakčných teplotách v okolí 0 °C, pričom pri chladení reakčnej zmesi so solankou nevytvára sa na chladiacich plochách námraza, ktorá zhoršuje přestup tepla, a tým aj chladenie reakčnej zmesi. Prídavkom chloridu sodného k vodnému prostrediu sa znížia straty kyanurchloridu spósobené hydrolýzou s vodou. Podlá postupu sa získá atrazín s vysokou čistotou, ktorá sa vyrovná produktu, získanému reakciou v přítomnosti organického rozpúšťadla. Bežne sa získá atrazín o obsahu 96 až 99 % hmot.It is an advantage of the invention that water with the addition of alkaline chloride is used as the reaction medium. After completion of the reaction, atrazine is filtered from the reaction mixture and the alkali metal chlorides are washed with water. The process is much simpler than using an organic solvent that needs to be regenerated, which requires a sentence of energy. The addition of the alkali metal chloride to the aqueous medium reduces the freezing point of the aqueous solutions, which is particularly advantageous at reaction temperatures in the region of 0 ° C, while the cooling of the reaction mixture with brine does not form ice on the cooling surfaces. cooling the reaction mixture. Addition of sodium chloride to the aqueous medium reduces the cyanuric chloride losses due to hydrolysis with water. According to the process, atrazine of high purity is obtained which is equal to the product obtained by the reaction in the presence of an organic solvent. Typically, atrazine is obtained having a content of 96 to 99% by weight.
Příklad 1Example 1
Do reakčnej banky sa dalo 225 ml vody, v ktorej sa rozpustilo 23 g chloridu sodného. Potom sa k roztoku přidalo 30 g kyanurchloridu. Obsah banky sa ochladil na 10 °C. Do banky sa potom začal dávkovat 48 ml 21 % hmot. vodného roztoku izopropylamínu. Potom sa zmes nechala 30 minút doreagovať pri teplote 15 °C. K reakčnej zmesi sa následné přidalo 5-0 ml 10,6 % hmot. vodného roztoku hydroxidu sodného a zmes sa nechala reagovat 1 hodinu pri teplote 15 °C. Hodnota pH suspenzie po doreagování bola 7,4. Potom sa k reakčnej zmesi přidalo 21,4 mililitra 39 % hmot. etylaminů a reakčná zmes sa nechala miešať pri teplote 20 °C. Potom sa -opStovne k nej přidalo 50 ml 10,6 % hmot. vodného roztoku hydroxidu sodného a zmes sa nechala doreagovať 1 hodinu pri teplote 20 °C. Zo suspenzie sa odfiltroval získaný atrazín, premyl vodou a vysušil. Získalo sa 31,6 g technického atrazínu s obsahom225 ml of water was added to the reaction flask in which 23 g of sodium chloride was dissolved. Then 30 g of cyanuric chloride was added to the solution. The contents of the flask were cooled to 10 ° C. 48 ml of 21 wt. aqueous isopropylamine solution. The mixture was then allowed to react for 30 minutes at 15 ° C. Subsequently, 5-0 ml of 10.6 wt. aqueous sodium hydroxide solution and the mixture was allowed to react at 15 ° C for 1 hour. The pH of the suspension after reaction was 7.4. Thereafter, 21.4 ml of 39 wt. ethylamine and the reaction mixture was allowed to stir at 20 ° C. 50 ml of 10.6% by weight were then added thereto. aqueous sodium hydroxide solution and the mixture was allowed to react for 1 hour at 20 ° C. The obtained atrazine was filtered from the suspension, washed with water and dried. 31.6 g of technical atrazine were obtained
97,6 % hmot. atrazínu, 1,6 % hmot. simazínu a 0,7 % hmot. propazínu.97.6 wt. atrazine, 1.6 wt. % simazine and 0.7 wt. propazine.
Příklad 2Example 2
Postupovalo sa podfa příkladu 1 s tým rozdielom, že sa miesto chloridu sodného použilo 25 g chloridu draselného. Teplota v prvom reakčnom stupni miesto 15 QC bola iba 5 °C a v druhom reakčnom stupni miesto 20 °C bola iba 10 °C. Získalo sa 31,5 g technického atrazínu, ktorý obsahoval 97,4 % hmot. atrazínu, 0,9 % hmot. simazínu a 1,6 percenta hmot. propazínu.The procedure of Example 1 was followed except that 25 g of potassium chloride was used instead of sodium chloride. The temperature in the first reaction step instead of 15 Q C was only 5 ° C and the second step instead of 20 ° C was only 10 ° C. 31.5 g of technical atrazine was obtained, which contained 97.4% by weight of the composition. atrazine, 0.9 wt. simazine and 1.6 wt. propazine.
Vynález je možno použit pri výrobě technického atrazínu, ktorý sa používá ako- herbicid v- pofnohospodárstve,The invention can be used in the production of technical atrazine, which is used as a herbicide in agriculture,
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CS861807A CS253429B1 (en) | 1986-03-15 | 1986-03-15 | Process for preparing 2-isopropylamino-4-ethylamino-6-chlor-s-triazine |
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CS861807A CS253429B1 (en) | 1986-03-15 | 1986-03-15 | Process for preparing 2-isopropylamino-4-ethylamino-6-chlor-s-triazine |
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