CS223661B1 - Production method of 1,4-dinitro-tetrahydroimidazo [4,5-d] imidazole-2,5 (1H, 3H) -dione - Google Patents

Production method of 1,4-dinitro-tetrahydroimidazo [4,5-d] imidazole-2,5 (1H, 3H) -dione Download PDF

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CS223661B1
CS223661B1 CS791380A CS791380A CS223661B1 CS 223661 B1 CS223661 B1 CS 223661B1 CS 791380 A CS791380 A CS 791380A CS 791380 A CS791380 A CS 791380A CS 223661 B1 CS223661 B1 CS 223661B1
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dione
tetrahydroimidazo
nitration
imidazole
dinitro
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CS791380A
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Czech (cs)
Slovak (sk)
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Svatopluk ZEMAN
Milan Dimun
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Svatopluk ZEMAN
Milan Dimun
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Abstract

Vynález sa týká výroby l,4-dinitro-retra- hydroimidazo [ 4,5-d ] -imidazol-2,5 ( 1H, 3H J - -diónu nitráciou tetrahydroimidazo [ 4,5-d j- -imidazol-2,5 (1H, 3H)-diónu v prostředí ky ­ seliny dusičnej, pričom podmienky nitrácie sú volené v přítomnosti močoviny, čo má za následok zvýšenie výťažnosti a bezpeč ­ nosti procesu. Vynález je možné bez problé- mov využívat pri výrobě titulnej substancie.The invention relates to the production of 1,4-dinitro-retra-hydroimidazo[4,5-d]-imidazol-2,5 (1H, 3H)-dione by nitration of tetrahydroimidazo[4,5-d]-imidazol-2,5 (1H, 3H)-dione in nitric acid, whereby the nitration conditions are selected in the presence of urea, which results in an increase in the yield and safety of the process. The invention can be used without problems in the production of the title substance.

Description

222 3222 3

Vynález sa týká výroby 1,4-dinitroderivá-tu tetrahydroimidazo [ 4,5-d] -imidazol-2,5-(1H, 3H)-diónu nitráciou tetrahydroimida-zo [4,5-d]-imidazol-2,5(1H, 3H)-diónu v pro-středí kyseliny dusičnej, pričom podmlenkysú volené tak, že priaznivo ovplyvňujú vý-ťažok a bezpečnost procesu.The invention relates to the preparation of 1,4-dinitroderating tetrahydroimidazo [4,5-d] imidazole-2,5- (1H, 3H) -dione by nitration of tetrahydroimidazo [4,5-d] imidazole-2,5 (1H, 3H) -dione in the nitric acid medium, being chosen so as to favorably influence the yield and process safety.

Dinitroderiváty tetrahydroimidazo [4,5-d ] --imidazol-2,5(lH, 3H)-diónu známe tiež podnázvom dinitroglykolurily označované kó-dom DINGU, je možné získat nitráciou vprostředí kyseliny dusičnej a/alebo kyseli-nou dusičnou v prostředí acetanhydridu. Zprvého uvedeného variantu sa uvádza vznikzmesi 1,4-; 1,6-; a 1,3-dinitroderivátov (En-cyclopedia of Explosives and Related Items.Vol. 6, PATR 2700, Picatinny Arsenal, Dover,1974, str. G 117 až 118). 1,3-dinitroglykolu-ril je nestabilný a 1'ahko sa rozkládá vo vria-cej vodě, čo umožňuje vhodná volbu spůso-bu izolácie produktu z nitrácie glykoluriluv prostředí kyseliny dusičnej s možnosťouzískania zmesi izomérov s vysoko prevláda-júcim obsahom 1,4-dinitroglykolurilu a prak-ktitiky neobsahujúcu 1,3-dinitroglykoluril. Výťažok dinitroglykolurilov je vedla vše-obecnej závislosti na reakčných podmien-kach daný stabilitou glykolurilu, teda 2,4,6,8--tetraazalbicyklo-[ 3.3.0] oktánového skele-tu v reakčnom prostředí. V prostředí dymi-vej kyseliny dusičnej je dominujúcou ved-1'ajšou reakciou acidolýza glykolurilu, kto-rú je možné do určitej miery potlačit prí-davkom substancie schopnej v acidolytic-kých rovnovážných reakciách vystupovat nastraně produktov reakcie.The dinitroderivatives of tetrahydroimidazo [4,5-d] imidazole-2,5 (1H, 3H) -dione also known by the subtitle dinitroglycolurils denoted DINGU can be obtained by nitrating in the nitric acid and / or nitric acid medium in the acetic anhydride medium . The first mentioned variant is referred to as 1,4-; 1,6-; and 1,3-dinitroderivatives (En cyclopedia of Explosives and Related Items. Vol. 6, PATR 2700, Picatinny Arsenal, Dover, 1974, pp. G 117-118). 1,3-dinitroglycol-1 is unstable and readily decomposes in boiling water, allowing for a suitable choice of the method of isolating the nitration product of the glycoluril in the nitric acid medium, with the possibility of obtaining a high-1,4-isomer mixture of isomers predominantly. dinitroglycoluril, and non-1,3-dinitroglycoluril-containing functionalities. The yield of dinitroglycolurils resulted in general dependence on the reaction conditions due to the stability of glycoluril, i.e. 2,4,6,8-tetraazalbicyclo [3.3.0] octane glass in the reaction medium. In the nitric acid environment, acidolysis of glycoluril, which to some extent can be suppressed by the addition of a substance capable of exiting the reaction products in acidolytic equilibrium reactions, is the dominant side reaction.

Podl'a tohto vynálezu spósob výroby 1,4--dinitro-tetrahydroimidazo [ 4,5-d ] -imidazol--2,5 (1H, 3H)-diónu nitráciou tetrahydroimi-dazo [4,5-d]-imidazol-2,5(lH, 3H)-diónu vprostředí kyseliny dusičnej sa uskutočňujetak, že proces nitrácie prebieha v přítom-nosti močoviny pridávanej do nitračnéhosystému naraz alebo postupné v množstve0,05 až 15 % hmot., s výhodou v množstve0,4 až 11,0 % hmot. vztiahnuté na hmot-nost do reakcie braného tetrahydroimida-zo [4,5-d ] -imidazol-2,5- (1H, 3H j -diónu. Výhodou spůsobu podl’a vynálezu je táskutočnost, že přítomnost močoviny v re-akčnej zmesi priaznivo ovplyvňuje selekti-vitu a výťažnosť procesu v celom výhodnomrozsahu. Optimálny obsah močoviny prida- 61 4 ný ku kyselině dusičnej před nitráciou je 1,1 až 1,7 °/o hmot. na navážku glykolurilu.Pozitivny, avšak menej výrazný vplyv navýtažky dinitroglykolurilu má aj močovinavnášaná do reakčného systému ako adití-vum aplikovaného glykolurilu.According to the present invention, the process for the preparation of 1,4-dinitro-tetrahydroimidazo [4,5-d] imidazole-2,5 (1H, 3H) -dione by nitration of tetrahydroimidazo [4,5-d] imidazole- The 2.5 (1H, 3H) -dione in the nitric acid medium is carried out in that the nitration process takes place in the presence of urea added to the nitration system at one time or successively in an amount of 0.05 to 15% by weight, preferably 0.4 to 11% by weight. % Wt. % of the tetrahydroimidazo [4,5-d] -imidazole-2,5- (1H, 3H-dione) reaction. The advantage of the process according to the invention is that the presence of urea in the reaction mixture The optimum content of urea added to nitric acid prior to nitration is 1.1 to 1.7% by weight for the weight of glycoluril.Positive but less pronounced effect of the dinitroglycoluril feedstock it also has urea introduced into the reaction system as an additive of applied glycoluril.

Vedla uvedeného ekonomického efektu jevýhodou tohto vynálezu aj zvýšenie stabili-ty reakčnej zmesi a teda bezpečnosti proce-su v důsledku přítomnosti močoviny. Stabi-lizujúci vplyv močoviny pri nitrolýzach vprostředí kyseliny dusičnej (čs. pat. číslo97100, čs. autorské osvedčenie č. 227 903).alebo esterifikáciách alifatických alkoholovkyselinou dusičnou alebo zmesou kyselinydusičnej s kyselinou sírovou (čs. autorskéosvedčenie č. 168 189) je dobré známy, a takisto dobře interpretovaný v prácach V. Ka-deřábek a J. Denkstein: Coll. Czech. Chem.Comun. 1960, 25, 1070; alebo tiež čs. autors-ké osvedčenie č. 227 903.As a result of this economic effect, it is an advantage of the present invention to increase the stability of the reaction mixture and hence the safety of the process due to the presence of urea. The stabilizing effect of urea in nitroses in the nitric acid medium (U.S. Pat. No. 97100, MS Author No. 227 903) or by esterification of aliphatic nitric acid or nitric acid with sulfuric acid (U.S. Pat. No. 168,189) is well known , as well as well interpreted in the works of V. Ka-deřábek and J. Denkstein: Coll. Czech. Chem.Comun. 1960, 25, 1070; or also MS. Authorized Certificate No. 227 903.

Nový a vyšší účinok dosahovaný v zmysletohto vynálezu nebol v literatuře doposial'popísaný a je dokumentovaný nasledujúcimipríkladmi. Příklad 1 50 hmot. dielov glykolurilu (90 min suše-ného pri teplote 80 až 85 °C) sa za stáléhomiešania po dobu 4 až 5 minut vnáša do500 obj. dielov kyseliny dusičnej 99,15%-nej.Pri vnášení glykolurilu je teplota reakčnejzmesi vonkajším chladením udržovaná ná24 až 27 °C. Potom následuje zvýšenie tep-loty reakčnej zmesi vonkajším ohrevom vpriebehu 6 až 7 minút na 50 až 53 °C a vtomto teplotnom rozmedzí sa udržuje po do-bu 45 minút. Po tejto době je nitračná zmestenkým prúdom opatrné vedená do 1000 obj.dielov variacej vody. Vzniknutá suspenziaje 10 minút refluxovaná a po vychladnutína 15 až 20 °C je produkt izolovaný filtrá-ciou, na filtri premytý vodou do neutaálnejreakcie odchádzajúceho filtrátu, a potomsušený v tenkej vrstvě 4 hodiny pri teplote80 až 85 °C.The novel and superior effects achieved in the present invention have not been described in the literature so far and are exemplified by the following examples. Example 1 50 wt. glycoluril (90 min dried at 80-85 ° C) was added to 500 parts by volume of nitric acid (99.15%) with stirring for 4-5 minutes. The temperature of the reaction mixture was maintained at room temperature for 24 hours by adding glycoluril. Deň: 27 ° C. This is followed by an increase in the temperature of the reaction mixture by external heating over 6 to 7 minutes to 50 to 53 ° C and is maintained for 45 minutes in this temperature range. After this time, the nitration is carefully passed into a 1000 vol. The resulting suspension is refluxed for 10 minutes and after cooling to 15-20 ° C, the product is isolated by filtration, washed with water on the filter until neutral reaction of the outgoing filtrate, and then dried in a thin layer at 80-85 ° C for 4 hours.

Tento základný postup bol ešte páťkrátreprodukovaný s tým, že před vlastným vná-šaním glykolurilu je v predloženej kyseli-ně dusičnej rozpuštěné vždy určité množstvomočoviny. Výsledky prezentuje nasledujúcatabulka:This basic procedure has been repeatedly reproduced, with certain amounts of urea dissolved in the present nitric acid prior to the introduction of glycoluril. The results are presented in the following table:

Množstvo močoviny v predlože- Výtažky 1,4-dinitro-glykolurilu nej kyselině dusičnej hmot. dlely hmot. % na návažok hmot. dlely % oproti teórii glykolurilu 0,0 0,0 67,0 82,04 0,2 0,4 68,7 84,12 0,7 1,4 69,2 84,73 1,4 2,8 68,7 84,12 3,5 7,0 68,1 83,38 5,5 11,0 67,5 82,65The amount of urea in the 1,4-dinitro-glycoluril nitric acid extract. dlely hmot. % to weight gain. % vs. glycoluril 0.0 0.0 67.0 82.04 0.2 0.4 68.7 84.12 0.7 1.4 69.2 84.73 1.4 2.8 68.7 84.12 3.5 7.0 68.1 83.38 5.5 11.0 67.5 82.65

Claims (1)

5 222661 Příklad 2 Nitrácia glykolurilu sa robí ako v příkla-de 1, len s tým rozdielom, že použitý gly-koluril v množstve 50 hmot. dielov je před vnášaním do kyseliny dusičnej zmiešaný s1 hmot. dielom močoviny rovnakej kvalityako v příklade 1. Vzniká 67,9 hmot. dielovdinitroglykolurilu, čo představuje 83,14 %oproti teorii. PREDMET Spósob výroby 1,4-dinitro-tetrahydroimi-dazo[4,5-d]imidazol-2,5(lH, 3H)-diónu nitrá-ciou tetrahydroimidazo [ 4,5-d ] -imidazol-2,5-(1H, 3H)-diónu v prostředí kyseliny dusič-nej, vyznačujúci sa tým, že proces nitráciesa uskutočňuje v prostředí močoviny, pridá- ynAlezu vanej do nitračného systému naraz alebopostupné v množstve 0,05 až 15,0 % hmot.,s výhodou v množstve 0,4 až 11,0 % hmot.,vztiahnuté na hmotnost do reakcie branéhotetrahydroimidazo [4,5-d ] -imidazol-2,5 [ 1H,3H)-diónu. I VExample 2 Nitration of glycoluril is performed as in Example 1, except that the glycoluril used in an amount of 50 wt. of the parts is mixed with 1 wt. of urea of the same quality as in Example 1. 67.9 wt. dielovdinitroglycoluril, which represents 83.14% over theory. SUBJECT A process for preparing 1,4-dinitro-tetrahydroimidazo [4,5-d] imidazole-2,5 (1H, 3H) -dione by nitration tetrahydroimidazo [4,5-d] imidazole-2,5- ( Characterized in that the nitration process is carried out in a urea medium added to the nitration system at one time or at a rate of 0.05 to 15.0% by weight, preferably at a concentration of 0.05 to 15.0% by weight. 0.4 to 11.0% by weight, based on the weight of the branethotetrahydroimidazo [4,5-d] imidazol-2,5 [1H, 3H] -dione reaction. I V
CS791380A 1980-11-20 1980-11-20 Production method of 1,4-dinitro-tetrahydroimidazo [4,5-d] imidazole-2,5 (1H, 3H) -dione CS223661B1 (en)

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