CS266142B1 - A method for preparing O.O-dimatyl-S-phthalimidomethyldithiophosphate - Google Patents

A method for preparing O.O-dimatyl-S-phthalimidomethyldithiophosphate Download PDF

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CS266142B1
CS266142B1 CS878032A CS803287A CS266142B1 CS 266142 B1 CS266142 B1 CS 266142B1 CS 878032 A CS878032 A CS 878032A CS 803287 A CS803287 A CS 803287A CS 266142 B1 CS266142 B1 CS 266142B1
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toluene
phthalimide
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Stefan Ing Csc Truchlik
Karol Ing Dulak
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Truchlik Stefan
Dulak Karol
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Abstract

Riešenie sa týká spósobu přípravy 0,0- -dimetyl-S-ftalimidometylditiofosfátu reakciou suspenzie N-hydroxymetylftalimidu v inertnom organickom rozpúštadle s chlorovodíkom a/alebo vodným roztokom kyseliny chlorovodíkovej s následnou reakciou vzniknutého roztoku N-chlórmetylftalimidu so sodnou solou 0,0-dimetylditiofosforečnej kyseliny, čím sa získá roztok 0,0-dimetyl- -S-ftalimidometylditiofosfátu v inertnom organickom rozpúštadle, z ktorého po premytí s roztokom hydroxidu sodného a vody sa izoluje známým spósobom technický 0,0-dimetyl- -S-ftalimidometylditiofosfát vo vysokom výtažku a čistotě.The solution relates to a method of preparing 0,0-dimethyl-S-phthalimidomethyldithiophosphate by reacting a suspension of N-hydroxymethylphthalimide in an inert organic solvent with hydrogen chloride and/or an aqueous solution of hydrochloric acid followed by the reaction of the resulting N-chloromethylphthalimide solution with the sodium salt of 0,0-dimethyldithiophosphoric acid, thereby obtaining a solution of 0,0-dimethyl- -S-phthalimidomethyldithiophosphate in an inert organic solvent, from which, after washing with a solution of sodium hydroxide and water, technical 0,0-dimethyl- -S-phthalimidomethyldithiophosphate is isolated in a known manner in high yield and purity.

Description

2 CS 266 142 B1

Vynález sa týká spůsobu přípravy 0,0-dimetyl-S-ftalimidometylditiofosfátu (fosmetu)z ftalimidu ako východiskovej suroviny. Fosmet je účinnou látkou viacerých insekticídnycha akaricídnych prípravkov. Všeobecne je známe, že fosmet je možné připravit reakciou N-halogénmetylftalimidus alkalickou resp. amonnou solou Ο,Ο-dimetylditiofosforečnej kyseliny v zmysle reakčnejschémy CO.

.CO

pričom X znamená chlór alebo bróm a Me znamená vodík, draslík alebo NH^.

Pri príprave fosmetu sa obyčajne ako východiskové suroviny uvádzajú N-bróm-metylftalimid(DE 930 446) a N-chlórmetylftalimid (US 2 767 194). Pretože výroba týchto východiskovýchsurovin navazuje na přípravu N-hydroxymetylftalimidu (DRP 104 624, Buc S. R.: J. Am. Chem. SOc. 69, 245 (1947) , hladala sa možnost zjednodušenia viacstupňovej syntézy fosmetu. Zistilosa (CS 120 423) , že reakciu N-hydroxymetylftalimidu s chlorovodíkom možno uskutočnit v přítom-nosti takého inertného rozpúštadla, ktoré v navSzujúcom reakčnom stupni bude slúžit akoreakčné prostredie. V dalšom zo spósobov výroby fosmetu (CS 162 692) sa východiskový bezvodý N-hydroxymetyl--ftalimid suspendovaný v toluéne, za katalytického účinku pyridinu, najprv pomocou chloridutionylu premení na N-chlórmetylftalimid, ktorý sa po vykrystalizovaní odfiltruje, premyjestudenou vodou a vo vlhkom stave, za miešania sa přidá do pripravenej emulzie toluénu vovodě, ktorá obsahuje sodnú sol Ο,Ο-dimetylditiofosforečnej kyseliny, čím sa dosiahne v prie-behu 1,5 h pri teplote 55 až 60 °C ukončenie reakcie. Po oddělení fáz sa z toluénovej vrstvyfiltráciou odstránia nečistoty (ftalimid, síra atd.) a po oddestilovaní toluénu za zničenéhotlaku sa získá tavenina technického fosmetu. V patentovéj literatúre (SU 652 897, GB 1 487 038) sa opisuje postup, pri ktorom vý-chodiskový N-hydroxymetylftalimid vo formě vlhkého filtračného koláča, sa suspenduje v benzé-ne, pomocou 35 až 40 %-nej kyseliny solnej a chlorovodíka zreaguje na N-chlórmetylftalimid, ktorýpotom vo formě benzénového roztoku s vodným roztokom sodnej soli Ο,Ο-dimetylditiofosforečnejkyseliny poskytne benzénový roztok fosmetu, ktorý po premytí s 10 %-ným roztokom hydroxidusodného a vody poskytne po odpaření rozpúštadla technický fosmet. Z uvádzaných spůsobov má postup podlá CS 162 692 tú nevýhodu, že východiskovou surovinouje bezvodý N-hydroxymetylftalimid, ktorý reakciou s chloridom tionylu poskytne N-chlórmetyl-ftalamid, ktorý sa musí odfiltrovat, dvakrát premyt studenou vodou a po dókladnom odsátísa použije k reakcii so sodnou solou Ο,Ο-dimetylditiofosforečnej kyseliny v přítomnosti toluénua 0,0,S-trimetylditiofosfátu. Po reakcii sa toluénová vrstva zbaví dalšou filtráciou nečistůt aaž potom sa izoluje očekávaný produkt. Nikde sa tiež nespomína ako sa technický produkt zbavuje0,0,S-trimetylditiofosfátu. Spůsob používá chloridu tionylu k výrobě N-chlórmetylftalimidu,čo je spojené s vývojom zmesi oxidu siřičitého a chlorovodíka, ktorú je třeba bud komplikova-né oddělovat, alebo po neutralizácii oxidovat podřel siričitanu na síran. Mimoriadne obtiažnaje aj manipulácia s N-chlórmetylftalimidom.

Postupu, pri ktorom je východiskovou surovinou vlhký filtračný koláč N-hydroxymetyl-ftalimidu (SU 652 897, GB 1 487 038), musela predchádzať jeho příprava a velmi nepříjemnáfiltrácia N-hydroxymetylftalimidu od matečných lúhov s obsahom formaldehydu.

Uvedené nedostatky odstraňuje spósob přípravy 0,0-dimetyl-S-ftalimidometylditiofosfátu reakciou ftalimidu s formaldehydom s odstránením prebytočného formaldehydu, metanolu a vody CS 266 142 B1 3 azeotropickou destiláciou s inertným organickým rozpúštadlom, reakciou N-hydroxymetylftalimidus chlorovodíkom a následnou reakciou vzniknutého N-chlórmetylftalimidu so sodnou solou 0,0--dimetylditiofosforečnej kyseliny podlá vynálezu. Podstata vynálezu spočívá v tom, že sus-penzia N-hydroxymetylftalimidu v inertnom organickom rozpúštadle sa nechá zreagovať s chloro-vodíkom a/alebo vodným roztokom kyseliny chlorovodíkovéj pri 20 °C až 80 °C, vzniknutý roztokN-chlórmetylftalimidu sa nechá reagovat so sodnou solou Ο,Ο-dimetylditiofosforečnej kyselinypri teplote 40 °C až 70 °C za vzniku roztoku 0,0-dimetyl-S-ftalimidometylditiofosfátu v inert-nom organickom rozpúštadle, z ktorého sa po premytí 0,5 až 8 í-ným roztokom hydroxidu sodné-ho s vodou a po odstráneni rozpúštadla známým spósobom izoluje technický O,O-dimetyl-S--ftalimidometylditiofosfát vo vysokom výtažku a s vysokou čistotou. Ako inertně organickérozpúštadlo sa móžu použit najma aromatické uhlovodíky ako benzén, toluén, xylén a ich zmesi,ale móžu sa použit aj 1,2-dichlóretán, tetrachlórmetán a pod. Spósobom podlá vynálezu sazíská vysokočistý technický fosmet obsahujúci viac ako 97 i 0,0-dimetyl-S-ftalimidometyl--ditiofosfátu vo viac ako 80 %-nom výtažku, počítané na východiskový ftalimid. V postupe, pri ktorom sa vychádzalo z bezvodého N-hydroxymetylftalimidu (CS 162 692) sa udává až 95,2 %-ný výťažok účinnej látky počítané na hydroxymetylftalamid. Uvedené teplotytopenia produktu (69 °C, 70 °C) neodpovedajú však uvádzaným čistotám (98,5 i), lebo čistýfosmet má t. t. 74 °C. V případe, ak sa vychádzalo z mokrého filtračného koláča N-hydroxymety1-ftalimidu (SU 652 897, GB 1 487 038) udávaný je 73 %-ný výťažok technického fosmetuo 95 %-nej čistotě. Výhody spósobu podlá vynálezu sú nasledujúce: N-hydroxymety1ftalimid nie je potřebné získávat vo formě mokrého filtračného koláča(CS 201 536), ani vo formě tuhého bezvodého produktu (CS 162 692). V stupni přípravy N-chlórmetylftalimidu nie je tento potřebné osobitne izolovat a pre-mývať (CS 162 692). V stupni přípravy techn. fosmetu možno reakciu roztoku N-chlórmetylftalimidu so sodnousolou Ο,Ο-dimetylditiofosforečnej kyseliny uskutočňovať aj za využitia principu dvojstupňové-ho přebytku reagujúcich zložiek (CS 253 920).

Napriek skutočnosti, že základnou východiskovou surovinou je ftalimid, že sa osobitneneizoluje ani N-chlórmetylftalimid (CS 162 652), ani N-hydroxymetylftalimid (SU 615 897GB 1 487 038), možno zlúčením všetkých troch postupov získat techn. fosmet v tak vysokejčistotě že jeho dalšia kryštalizácia je zbytočná.

Uvedené příklady ilustrujú, ale neobmedzujú predmet vynálezu. Příklad 1 K 147,2 dielom ftalimidu sa přidalo 101,2 dielu 35,6 %-ného vodného roztoku formaldehydua zmes sa vyhriala k refluxu, pri ktorom sa zotrvalo ešte 1 h po vyčírenf reakčnej zmesi.

Potom sa horúci roztok N-hydroxymetylftalimidu vlial do 900 objemových dielov toluénu avzniknutá suspenzia N-hydroxymetylftalimidu sa opat vyhriala k refluxu, za miešania a neustá-lého vydelovania vodnéj fázy sa reakčná zmes zahrievala potial, pokial teplota reakčnejzmesi nedosiahla 95 °C. Dovedná sa vydeliko 68 objemových dielov vodnej fázy s obsahom vody,metanolu a formaldehydu. Po ochladení reakčnej zmesi na 70 °C sa k nej přidalo 348 dielov32,4 %-nej kyseliny chlorovodíkovéj. Potom sa teplota reakčnej zmesi upravila na 34 °C av priebehu 50 min sa do zmesi voviedlo 104 dielov chlorovodíka. Reakčná zmes sa potom pomalyvyhriala na 55 °C až 60 °C, pri tejto teplote sa za miešania zmes udržiavala 1 h, čo postačo-valo na ostré vydelenie vrchnej organickej vrstvy s obsahom N-chlórmetylftalimidu od spodnejkyselinovej vrstvy. K odděleným 970 dielom toluénového roztoku N-chlórmetylftalimidu sa přidalo439 dielov 39,0 %-ného roztoku sodnej soli Ο,Ο-dimetylditiofosforečnej kyseliny, teplota 4 CS 266 142 B1 reakčnej zmesi sa upravila na 50 °C až 55 °C a pri tejto teplote sa reakčná zmes intenzívněmiešala 3,5 h. Potom sa zastavilo miešanie, oddělila sa spodná vodná vrstva s obsahom solía vrchná toluénová vrstva sa po ochladení na 25 °C až 30 °C premyla so 400 objemovými dilemi2 %-ného roztoku hydroxidu sodného a 300 dielmi vody. Potom sa toluénová vrstva zbavilarozpúŠ£adla na vákuovom rotačnom odparováku, nakoniec za tlaku 2,6 kPa a teploty kúpela80 °C. Získalo sa 294,3 dielov taveniny techn. produktu, ktorá po stuhnutí, rozdrvení avysušení v prúde dusíka, pri 50 °C, poskytla 264,9 dielov produktu s 99,2 %-ným obsahom0,0-dimetyl-S-ftalimidometylditiofosfátu, Čo odpovedá 82,81 %-nému výtažku, počítané navýchodiskový ftalimid. Příklad 2 K 73,6 dielom ftalimidu sa přidalo 50,0 dielov 36 %-ného vodného roztoku formaldehyduzmes sa vyhrievala k refluxu, pri ktorom sa zotrvalo 1 h. Potom sa vzniknutý roztok N-hydro-xymetylftalimidu za miešania vlial do 400 obj. dielov benzénu a azeotropickou destiláciousa zmes zbavila 32 obj. dielov vodnej fázy. Potom sa zmes ochladila na 25 °C, přidalo sak nej 240 dielov 41,5 %-nej kyseliny chlorovodíkovéj a v priebehu 1 h sa vyhrievala na 60 °Ca pri tejto teplote sa miešala ešte 1 h, oddělila sa spodná vrstva kyseliny a k zvyšným444,0 dielom benzénového roztoku N-chlórmetylftalimidu sa přidalo 227,0 dielov 38,5 %-néhoroztoku sodnej soli O,O-dimetylditiofosforečnej kyseliny a zmes sa potom miešala 3 h pri50 °C až 55 °C. Potom sa reakčná zmes ochladila na 25 °C, oddělila sa spodná vodná vrstvaa benzénový roztok techn. fosmetu sa premyl 200 obj. dielmi 3 %-ného roztoku hydroxidu sodné-ho a 300 obj. dielmi vody. Přepraný roztok sa zbavil rozpúšťadla oddestilovaním na vákuovejrotačnej odparke, v prúde dusíka, nakoniec za tlaku 1,3 kPa a teploty kúpela 80 °C, čímsa po vychladnutí a kryŠtalickom stuhnutí získalo 130,5 dielov produktu ktorý obsahoval99,3 % 0,0-dimetyl-S-ftalimidcmetylditiofosfátu, čo odpovedá 81,7 %-nému výtažku počítanéna ftalimid. Příklad 3 K 147,2 dielom ftalimidu sa přidalo 110,5 dielov 32,6 %-ného roztoku formaldehydu,zmes sa vyhriala k refluxu, pri ktorom sa zotrvalo 1,5 h, potom sa vydestilovalo 31 obj.dielov zmesi vody, formaldehydu a metanolu a zahuštěný roztok N-hydroxymetylftalimidu savlial za miešania do 900 objemových dielov toluénu a po vyhriati k refluxu sa ešte vyděliloz reakčnej zmesi dalších 40 dielov vodnej fázy. Potom sa reakčná zmes ochladila na 40 °C,přidalo sa k nej 350 dielov vydelenej kyselinovej vrstvy z přípravy roztoku N-chlórmetyl-ftalimidu z pokusu 1, ktorá obsahovala 32,6 % kyseliny chlorovodíkovéj a pri teplote 40 °Caž 55 °C sa k miešanej reakčnej zemsi priviedlo 105 dielov chlorovodíka, v priebehu 1 h.Reakčná zmes sa potom vyhriala na 60 °C až 65 °C a pri tejto teplote sa zotrvalo 1 h. Ná-sledovalo oddelenie spodněj kyselinovej vrstvy, od toluénovej vrstvy s obsahom N-chlórmetyl-ftalimidu, ku ktorej sa potom přidalo 462,0 dielov 39,0 %-ného vodného roztoku sodnej soliO,O-dimetylditiofosforečnej kyseliny, teplota reakčnej zmesi sa upravila na 50 °C až 55 °Ca pri tejto teplote sa reakčná zmes miešala 3 h. Po zastavení miešania sa oddělila spodnávodná vrstva s obsahom prebytočnej sodnej soli 0,O-dimetylditiofosforečnej kyseliny od toluénovej vrstvy s obsahom fosmetu. Toluénová vrstva sa potom přeprala 400 dielmi 2,5 %-ného rozto-ku hydroxidu sodného a potom so 400 dielmi vody. Toluénový roztok sa potom zbavil rozpúšfadlana vákuovej rotačnej odparke, nakoniec za tlaku 2,0 kPa a teploty kúpela 80 °C, čím sa získa-lo 288,5 g taveniny s obsahom 8 % toluénu a 91,4 % 0,0-dimetyl-S-ftalimidometylditiofosfátu,čo odpovedá 83,05 %-nému výfažku počítané na ftalimid. Produkt možno priamo použiť k výroběemulzných koncentrátov. Příklad 4

Zo 147,2 dielov ftalimidu, 110,5 dielov 32,6 %-ného roztoku formaldehydu, 900 obj. dielov toluénu, 351 dielov kyselinovej vrstvy z pokusu 3, ktorá obsahovala 31,9 % chlorovodíka a 106 cl plynného chlorovodíka připravil sa postupom podlá příkladu 3 toluénový roztok

2 CS 266 142 B1

The invention relates to a process for the preparation of 0,0-dimethyl-S-phthalimidomethyldithiophosphate (phosmet) from phthalimide as a starting material. Fosmet is the active ingredient of several insecticidal and acaricidal preparations. It is generally known that phosmet can be prepared by the reaction of N-halomethylphthalimide with alkali or alkali. ammonium salt of Ο, Ο-dimethyldithiophosphoric acid in the sense of the CO reaction.

.WHAT

wherein X is chlorine or bromine and Me is hydrogen, potassium or NH 4.

In the preparation of phosmet, N-bromomethylphthalimide (DE 930 446) and N-chloromethylphthalimide (US 2,767,194) are usually used as starting materials. Since the production of these starting materials follows the preparation of N-hydroxymethylphthalimide (DRP 104 624, Buc SR: J. Am. Chem. SOc. 69, 245 (1947), the possibility of simplifying the multistage synthesis of phosmet was sought. N-Hydroxymethylphthalimide with hydrogen chloride can be carried out in the presence of an inert solvent which will serve as the reaction medium in the next reaction step, and in another process for the production of phosmet (CS 162 692), anhydrous N-hydroxymethyl phthalimide suspended in toluene, The catalytic action of pyridine is first converted to N-chloromethylphthalimide by chloridyl chloride, which after crystallization is filtered off, washed with water and moist, added to the prepared toluene emulsion with water containing sodium Ο, Ο-dimethyldithiophosphoric acid, thereby achieving in the course of 1.5 h at 55-60 ° C, quench the reaction remove the impurities from the toluene layer (phthalimide, sulfur, etc.) by filtration, and after the toluene has been distilled off, the technical phthalate melt is obtained. The patent literature (SU 652 897, GB 1 487 038) describes a process wherein the starting N-hydroxymethylphthalimide in the form of a wet filter cake is suspended in benzene, reacted with 35-40% hydrochloric acid and hydrogen chloride to N-chloromethylphthalimide, which, in the form of a benzene solution with an aqueous solution of sodium Ο, ld-dimethyldithiophosphoric acid, gives a benzene solution of phosmet which, after washing with a 10% solution of sodium hydroxide and water, yields a technical phosmet after evaporation of the solvent. According to the aforementioned methods, the process according to CS 162 692 has the disadvantage that the starting material is anhydrous N-hydroxymethylphthalimide which, by reaction with thionyl chloride, yields N-chloromethyl-phthalamide which has to be filtered off, washed twice with cold water and used for reaction with sodium. Ο, Ο-dimethyldithiophosphoric acid salt in the presence of toluene and 0,0, S-trimethyldithiophosphate. After the reaction, the toluene layer is removed by further filtration to remove impurities and then the expected product is isolated. There is also no mention of how the technical product is de-0,0, S-trimethyldithiophosphate. The process uses thionyl chloride to produce N-chloromethylphthalimide, which is associated with the development of a mixture of sulfur dioxide and hydrogen chloride, which is either complicated to separate or oxidized to sulphate upon neutralization. Also, the handling of N-chloromethylphthalimide is extremely difficult.

The process whereby the starting feedstock is a wet N-hydroxymethyl-phthalimide filter cake (SU 652 897, GB 1 487 038), its preparation had to be avoided and the N-hydroxymethylphthalimide filtration from the formaldehyde-containing mother liquors was very unpleasant.

These drawbacks are overcome by the preparation of 0,0-dimethyl-S-phthalimidomethyldithiophosphate by reacting phthalimide with formaldehyde to remove excess formaldehyde, methanol and water by azeotropic distillation with an inert organic solvent, reaction of N-hydroxymethylphthalimide with hydrogen chloride followed by reaction of the resulting N-chloromethylphthalimide with the sodium salt of the 0,0-dimethyldithiophosphoric acid of the invention. SUMMARY OF THE INVENTION The present invention provides that the suspension of N-hydroxymethylphthalimide in an inert organic solvent is reacted with hydrogen chloride and / or aqueous hydrochloric acid at 20 ° C to 80 ° C and the resulting N-chloromethylphthalimide solution is reacted with sodium salt. Ο, Ο-dimethyldithiophosphoric acid at a temperature of 40 ° C to 70 ° C to form a solution of 0,0-dimethyl-S-phthalimidomethyldithiophosphate in an inert organic solvent from which, after washing with 0.5 to 8% sodium hydroxide solution high-purity high-purity, high purity technical O, O-dimethyl-S-phthalimidomethyldithiophosphate is isolated with water and, after removal of the solvent in a known manner. As the inert organic solvent, aromatic hydrocarbons such as benzene, toluene, xylene and mixtures thereof can be used, but 1,2-dichloroethane, carbon tetrachloride and the like can also be used. According to the present invention, high purity technical cosmetics containing more than 97% of O, O-dimethyl-S-phthalimidomethyl-dithiophosphate in more than 80% yield, calculated on the starting phthalimide, are extracted. Starting from anhydrous N-hydroxymethylphthalimide (CS 162 692), up to 95.2% yield of active compound calculated on hydroxymethylphthalamide is given. The product temperature of the product (69 ° C, 70 ° C) does not, however, correspond to the reported purity (98.5 i), since the pure cosmetic material is 74 ° C. When starting with a wet N-hydroxymethyl-phthalimide filter cake (SU 652 897, GB 1 487 038), a 73% yield of technical cosmetics is 95% pure. Advantages of the process according to the invention are as follows: N-hydroxymethylphthalimide is not required to be obtained in the form of a wet filter cake (CS 201 536) or in the form of a solid anhydrous product (CS 162 692). In the N-chloromethylphthalimide preparation step, it is not necessary to isolate and wash it separately (CS 162 692). Techn. phosmet, the reaction of a solution of N-chloromethylphthalimide with Ο, Ο-dimethyldithiophosphoric acid can also be carried out using the principle of a two-step excess of reactants (CS 253 920).

Despite the fact that the basic starting material is phthalimide, neither N-chloromethylphthalimide (CS 162 652) nor N-hydroxymethylphthalimide (SU 615 897GB 1 487 038) is isolated, but techn. phosmet in such a high purity that further crystallization is unnecessary.

These examples illustrate but do not limit the invention. EXAMPLE 1 101.2 parts of a 35.6% aqueous formaldehyde solution was added to 147.2 parts of phthalimide, and the mixture was heated to reflux for 1 hour after clarification of the reaction mixture.

Thereafter, a hot solution of N-hydroxymethylphthalimide was poured into 900 parts by volume of toluene and the resulting N-hydroxymethylphthalimide slurry was heated to reflux, while stirring and continuously separating the aqueous phase, the reaction mixture was heated until the reaction temperature reached 95 ° C. 68 parts by volume of an aqueous phase containing water, methanol and formaldehyde are obtained. After cooling the reaction mixture to 70 ° C, 348 parts of 32.4% hydrochloric acid were added. Then the temperature of the reaction mixture was adjusted to 34 ° C and 104 parts of hydrogen chloride was introduced into the mixture over 50 minutes. The reaction mixture was then slowly heated to 55 ° C to 60 ° C and maintained at this temperature for 1 hour while stirring, which was sufficient to sharpen the upper organic layer containing N-chloromethylphthalimide from the lower acid layer. To the separated 970 parts of a toluene solution of N-chloromethylphthalimide was added 439 parts of a 39.0% solution of sodium Ο, Ο-dimethyldithiophosphoric acid, the temperature of the reaction mixture was adjusted to 50 ° C to 55 ° C and at that temperature The reaction mixture was stirred vigorously for 3.5 h. Thereafter, the stirring was stopped, the lower aqueous salt-containing layer was separated, and the top toluene layer was washed with 400 parts by volume of 2% sodium hydroxide solution and 300 parts by cooling after cooling to 25 ° C to 30 ° C. water. The toluene layer was then removed from the solvent on a vacuum rotary evaporator, finally at a pressure of 2.6 kPa and a bath temperature of 80 ° C. 294.3 parts of the melt techn. a product which, upon solidification, crushing and drying under a stream of nitrogen, at 50 ° C, gave 264.9 parts of product with a 99.2% content of O, O-dimethyl-S-phthalimidomethyldithiophosphate, corresponding to an 82.81% yield; calcined phthalimide. Example 2 50.0 parts of a 36% aqueous formaldehyde solution were added to 73.6 parts of phthalimide and heated to reflux for 1 hour. The resulting solution of N-hydroxymethylphthalimide was then stirred into 400 parts by volume with stirring. the benzene and the azeotropic distillation mixture were freed of 32 parts by volume of the aqueous phase. Then, the mixture was cooled to 25 ° C, 240 parts of 41.5% hydrochloric acid was added to it and heated to 60 ° C for 1 hour and stirred for 1 hour at this temperature, the lower acid layer separated and the remaining 444, A portion of the benzene solution of N-chloromethylphthalimide was added with 227.0 parts of a 38.5% by weight solution of sodium O, O-dimethyldithiophosphoric acid and the mixture was then stirred at 50 ° C to 55 ° C for 3 hours. After the reaction mixture was cooled to 25 ° C, the lower aqueous layer was separated and the benzene solution was separated. Phosmet was washed with 200 parts by volume of 3% sodium hydroxide solution and 300 parts by volume of water. The washed solution was freed from the solvent by distillation on a vacuum rotary evaporator, under a stream of nitrogen, finally at a pressure of 1.3 kPa and a bath temperature of 80 ° C to obtain 130.5 parts of product containing 99.3% O-dimethyl after cooling and crystallization. -S-phthalimidomethyldithiophosphate corresponding to 81.7% yield calculated from phthalimide. Example 3 110.5 parts of a 32.6% formaldehyde solution were added to 147.2 parts of phthalimide, the mixture was heated to reflux for 1.5 hours, then 31 parts by volume of a mixture of water, formaldehyde and distilled water were distilled. methanol and a concentrated solution of N-hydroxymethylphthalimide savlial with stirring to 900 parts by volume of toluene and after heating to reflux, a further 40 parts of the aqueous phase are separated. Thereafter, the reaction mixture was cooled to 40 ° C, and 350 parts of a divided acidic layer was added therefrom to prepare a solution of N-chloromethyl-phthalimide from Experiment 1 which contained 32.6% hydrochloric acid at 40 ° C to 55 ° C. The reaction mixture was then heated to 60 ° C to 65 ° C and maintained at this temperature for 1 hour. The separation of the lower acid layer, from the N- toluene layer was followed by stirring at room temperature for 1 hour. chloromethyl-phthalimide, to which 462.0 parts of a 39.0% aqueous solution of sodium salt, O-dimethyldithiophosphoric acid, was added, the temperature of the reaction mixture was adjusted to 50 ° C to 55 ° C and the reaction mixture was stirred at this temperature. h. After the stirring was stopped, the bottom layer was separated with the excess of O, O-dimethyldithiophosphoric acid sodium salt from the toluene layer containing phosmet. The toluene layer was then washed with 400 parts of 2.5% sodium hydroxide solution and then with 400 parts of water. The toluene solution was then freed from the solvent by a vacuum rotary evaporator, finally at a pressure of 2.0 kPa and a bath temperature of 80 ° C to yield 288.5 g of melt containing 8% toluene and 91.4% 0.0-dimethyl- S-phthalimidomethyldithiophosphate, corresponding to a 83.05% yield calculated on phthalimide. The product can be used directly for the production of emulsion concentrates. Example 4

Of 147.2 parts of phthalimide, 110.5 parts of a 32.6% solution of formaldehyde, 900 parts by volume of toluene, 351 parts of the acid layer of Experiment 3, which contained 31.9% of hydrogen chloride and 106 liters of hydrogen chloride gas prepared by Example 3 toluene solution

Claims (1)

CS 266 142 B1 5 N-chlórmetylftalimidu, ku ktorému sa potom přidala oddělená vodná vrstva s obsahom sodnejsoli Ο,Ο-dimetylditiofosforečnej kyseliny z pokusu 3 a po 1 h miešaní pri teplote 50 °Caž 55 °C sa zastavilo miešanie, oddělila sa vodná vrstva solí, ktorá obsahovala už len 0,8 isodnej soli Ο,Ο-dimetylditiofosforečnej kyseliny. K toluénovému roztoku sodnej soli 0,0-di-metylditiofosforečnej kyseliny, teplota reakčnej zmesi sa upravila na 50 °C až 55 °C a pritejto teplote sa reakčná zmes miešala 3 h. Potom sa reakčná zmes nechala oddělit a po oddělenísa vrchná toluénová vrstva roztoku techn. fosmetu přeprala 500 dielmi vody. Přepraný toluénovýroztok sa potom zbavil rozpúšťadla na vákuovom rotačnom odparováku, nakoniec za tlaku 1,1 kPa,v prúde dusíka a teploty kúpela 80 °C, čím sa po vychladnutí a stuhnutí získalo 262,7 dielov99,3 %-ného produktu, čo odpovedá 82,2 %-nému výtažku z teoretických 317,3 dielov. Příklad 5 K 147,2 dielom ftalimidu sa přidalo 103 dielov 35 %-ného roztoku formaldehydu, zmessa vyhriala k refluxu, pri ktorom sa zotrvalo 1 h, potom sa zo zmesi vydestilovalo 32 dielovvodnej fázy, přidalo sa 900 obj. dielov toluénu a azeotropicky sa dodestilovala všetka vodnáfáza, ktorá destilovala do teploty reakčnej zmesi 95 °C až 98 °C. Suspenzia N-hydroxymetyl-ftalimidu sa potom ochladila na 40 °C, přidalo sa k nej 350 dielov 32 %-nej kyseliny chloro-vodíkovej a za miešania sa k nej voviedlo 109 dielov plynného chlorovodíka, pomaly sa vyhrialana 60 °C až 65 °C a po 1 h zahrievaní pri tejto teplote sa oddělila spodná kyselinová vrstvaod hornej toluénovej vrstvy s obsahom N-chlórmetylftalimidu. K toluénovej vrstvě sa přidalo430,0 dielov 39,8 %-ného vodného roztoku sodnej soli Ο,Ο-dimetylditiofosforečnej kyseliny,teplota zmesi sa upravila na 50 °C až 55 °C a pri tejto teplote sa reakčná zmes miešala3 h. Potom sa ochladila pod 30 °C, přidalo sa 23,8 dielu 42 %-ného roztoku hydroxidu sodnéhoa po krátkom zamiešaní oddělila sa spodná vodná vrstva od toluénovej, ktorá sa napokon přepralaešte s 300 dielmi vody. Přepraná toluénová vrstva sa potom zbavila rozpúšťadla na vákovomrotačnom odparováku nakoniec za tlaku 2,7 kPa a teploty kúpela 75 °C. Získalo sa 296,2 dielovtaveniny techn. produktu, ku ktorému sa přidalo 200 obj. dielov metanolu a po rozoustenía ochladení na 7 °C sa získalo 258,3 dielov kryštalického 99,7 %-ného produktu, čo odpovedá81,2 %-nému výťažku počítané na ftalimid. Priklad6 Vychádzajúc z rovnakých množstiev surovin a rovnakým spósobom ako je uvedené v příklade1 (iba miesto benzénu sa použil toluén) sa připravil toluénový roztok N-chlórmetylftalimidu,ku ktorému sa přidalo 216,2 dielov 38,6 %-ného roztoku amónnej soli Ο,Ο-dimetylditiofosforečnejkyseliny a zmes sa potom miešala 3 h pri 50 °C až 55 °C. Potom sa oddělila spodná vodnávrstva a toluénový roztok techn. fosmetu sa premyl 200 obj. dielmi 5 %-ného roztoku hydroxidusodného a potom 250 dielmi vody. Přepraný roztok sa zbavil rozpúšťadla oddestilovaním zatlaku nakoniec 1,5 kPa a teploty kúpela 80 °C, čím sa po vychladnutí a kryštalickom stuhnutízískalo 131,6 dielov produktu ktorý obsahoval 99,2 % 0,0-dimetyl-S-ftalimidometylditiofosfátu,čo odpovedá 82,3 %-nému výťažku počítané na východiskový ftalimid. PREDMET VYNALEZU Spósob přípravy 0,0-dimetyl-S-ftalimidometylditiofosfátu reakciou ftalimidu s formaldehy-dom s odstránením prebytočného formaldehydu, metanolu a vody azeotropickou destilácious inertným organickým rozpúšťadlom, reakciou vzniknutej zmesi obsahujúcej N-hydroxymetyl-ftalimid s chlorovodfkom a následnou reakciou vzniknutého N-chlórmetylftalimidu so sodnousolou Ο,Ο-dimetylditiofosforečnej kyseliny vyznačujúci sa tým, že suspenzia N-hydroxymetyl-ftalimidu v inertnom organickom rozpúšťadle sa nechá zreagovať s chlorovodíkom a/alebo vodnýmroztokom kyseliny chlorovodíkovéj pri 20 °C až 80 °C, vzniknutý roztok N-chlórmetylftalimidusa nechá reagovat so sodnou solou Ο,Ο-dimetylditiofosforečnej kyseliny pri teplote 40 °Caž 70 °C za vzniku roztoku Ο,Ο-dimetyl-S-ftalimidometylditiofosfátu v inertnom organickomrozpúšťadle, z ktorého sa po premytí 0,5 až 8 %-ným roztokom hydroxidu sodného a vodou apo odstránení rozpúšťadla izoluje technický 0,0-dimetyl-S-ftalimidometylditiofosfát.5 N-chloromethylphthalimide to which a separate aqueous layer containing sodium Ο, Ο-dimethyldithiophosphoric acid from experiment 3 was added and stirring was stopped after 1 h of stirring at 50 ° C to 55 ° C, the aqueous layer was separated salt, which contained only 0.8 isodium salt of Ο, Ο-dimethyldithiophosphoric acid. To the toluene solution of 0,0-di-dimethyldithiophosphoric acid sodium salt, the temperature of the reaction mixture was adjusted to 50 ° C to 55 ° C and the reaction mixture was stirred for 3 hours at that temperature. techn. Phosmet with 500 parts of water. The washed toluene solution was then freed from the solvent on a vacuum rotary evaporator, finally at a pressure of 1.1 kPa, under a stream of nitrogen and a bath temperature of 80 ° C, yielding 262.7 parts of 99.3% product after cooling and solidification, corresponding to 82%. A 2% yield of the theoretical 317.3 parts. Example 5 103 parts of 35% formaldehyde solution were added to 147.2 parts of phthalimide, heated to reflux for 1 hour, then 32 parts of the aqueous phase were distilled off, 900 parts by volume of toluene was added and azeotropically all the water phase that distilled to the reaction mixture temperature of 95 ° C to 98 ° C was distilled off. The N-hydroxymethyl-phthalimide suspension was then cooled to 40 ° C, 350 parts of 32% hydrochloric acid were added thereto, and 109 parts of hydrogen chloride gas were introduced with stirring, and 60 ° C to 65 ° C was slowly heated. and after 1 h at this temperature, the lower acid layer was separated from the upper toluene layer containing N-chloromethylphthalimide. To the toluene layer was added 430.0 parts of a 39.8% aqueous solution of sodium os, dim-dimethyldithiophosphoric acid, the temperature of the mixture was adjusted to 50 ° C to 55 ° C and the reaction mixture was stirred for 3 hours. below 30 ° C, 23.8 parts of a 42% sodium hydroxide solution was added, and after brief mixing, the lower aqueous layer was separated from toluene, which was finally rinsed with 300 parts of water. The washed toluene layer was then freed from the solvent in a vacuum evaporator, finally at 2.7 kPa and a bath temperature of 75 ° C. 296.2 parts of melt techn. of the product to which 200 parts by volume of methanol was added and after dissolving and cooling to 7 ° C, 258.3 parts of crystalline 99.7% product was obtained, corresponding to a 81.2% yield calculated on phthalimide. EXAMPLE 6 A toluene solution of N-chloromethylphthalimide was prepared starting from the same amounts of raw materials and in the same manner as in Example 1 (instead of benzene only, using 216.2 parts of a 38.6% ammonium salt solution). the dimethyldithiophosphoric acid and the mixture was then stirred at 50 ° C to 55 ° C for 3 h. Subsequently, the bottom aqueous solution and the toluene solution were separated. The phosmet was washed with 200 parts by volume of a 5% solution of sodium hydroxide and then with 250 parts of water. The washed solution was freed from the solvent by distillation of a pressure of finally 1.5 kPa and a bath temperature of 80 ° C, yielding 131.6 parts of a product containing 99.2% of O, O-dimethyl-S-phthalimidomethyldithiophosphate after cooling and crystallization. A 3% yield calculated on the starting phthalimide. OBJECT OF THE INVENTION A process for preparing 0,0-dimethyl-S-phthalimidomethyldithiophosphate by reacting phthalimide with formaldehyde to remove excess formaldehyde, methanol and water by an azeotropic distillation with an inert organic solvent, reacting the resulting mixture containing N-hydroxymethyl-phthalimide with a hydrogen chloride followed by N- N- Ο, Ο-dimethyldithiophosphoric acid chloromethylphthalimide, characterized in that the suspension of N-hydroxymethyl-phthalimide in an inert organic solvent is reacted with hydrogen chloride and / or aqueous hydrochloric acid solution at 20 ° C to 80 ° C, leaving the resulting N-chloromethylphthalimide solution with Ο, Ο-dimethyldithiophosphoric acid sodium salt at 40 ° C to 70 ° C to form a Ο, Ο-dimethyl-S-phthalimidomethyldithiophosphate solution in an inert organic solvent from which, after washing with 0.5 to 8% sodium hydroxide solution and water and after removal of solvent i technical O, O-dimethyl-S-phthalimidomethyldithiophosphate is isolated.
CS878032A 1987-11-09 1987-11-09 A method for preparing O.O-dimatyl-S-phthalimidomethyldithiophosphate CS266142B1 (en)

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