CS270521B1 - Process for producing 3-methyl-4-nitrosophenol - Google Patents

Process for producing 3-methyl-4-nitrosophenol Download PDF

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CS270521B1
CS270521B1 CS881210A CS121088A CS270521B1 CS 270521 B1 CS270521 B1 CS 270521B1 CS 881210 A CS881210 A CS 881210A CS 121088 A CS121088 A CS 121088A CS 270521 B1 CS270521 B1 CS 270521B1
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methyl
nitrosophenol
methylphenol
producing
nitrosation
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CS881210A
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Czech (cs)
Slovak (sk)
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CS121088A1 (en
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Peter Ing Hauskrecht
Ivan Ing Zervan
Henrich Kovacic
Juraj Lacko
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Hauskrecht Peter
Ivan Ing Zervan
Henrich Kovacic
Juraj Lacko
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Priority to CS881210A priority Critical patent/CS270521B1/en
Publication of CS121088A1 publication Critical patent/CS121088A1/en
Publication of CS270521B1 publication Critical patent/CS270521B1/en

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Abstract

3-metyl-4r-nitrózofenol sa vyrába nitrozáciou 3-metylCenolu s dusitanom sodným. v prostředí minerálně;) kyseliny v přítomnosti tenzidu.3-Methyl-4-nitrosophenol is produced by nitrosation of 3-methylphenol with sodium nitrite in a mineral acid environment in the presence of a surfactant.

Description

CS 270521 B1CS 270521 B1

Vynález sa týká sposobu výroby 3-metyl-4-nitrózofenolu nitrozáoiou 3-metylfeno-lu s roztokom dusitanu sodného v prostředí, minerálnej kyseliny v přítomnosti tenzidu 3-metyl-4-nitrózofenol sa najčastejšie používá ako medziprodukt pri výrobě nitroderi-vátov 3-metylfenolu. Výrobu 3-metyl-4-nitrózofanolu popisuje Bridge Morgan, J. Am.Chem. Soc. 20 766 (1898) nitrozáoiou 3-metylfenolu s kyselinou dusitou. Nitrozácia3-metylfenolu s alkalickým dusitanem v prostředí kyseliny sírovej popisuje USA pat.δ. 1 502 849. Rozpustnosti 3-metylfenolu vo vodných roztokoch minerálnej kyselinys minerálnymi solami je malá a z toho dovodu reakcia prebieha prakticky na rozhraníkvapalnej páry organickej vrstvy a vodných roztokov. 3-metyl-4-nitrázofenol je vel-mi málo rozpustilý v reakčnej zmesi. V priemyselnom měřítku sa často stává, že do-chádzu k tvorbo inkrustov na stěnách reaktora, mieSadlách a pod., pričom časti3-metylfenolu zostáva nezreagovaná a samotná inkrusty znižujú přestup tepla cez ste-nu reaktora, pričom mŽže dochádzati k lokálnemu prehriatiu reakčnej zmesi.The invention relates to a process for the preparation of 3-methyl-4-nitrosophenol by nitroso-3-methylphenol with a solution of sodium nitrite in an environment of mineral acid in the presence of surfactant 3-methyl-4-nitrosophenol is most frequently used as an intermediate in the production of 3-methylphenol nitroderates . The preparation of 3-methyl-4-nitroso-ethanol is described by Bridge Morgan, J. Am. Soc. 20,766 (1898) nitroso-3-methylphenol with nitrous acid. The nitrosation of 3-methylphenol with alkali nitrite in sulfuric acid is described in U.S. Pat. The solubility of 3-methylphenol in aqueous mineral acid solutions is low and the reaction proceeds to virtually interfacial vapors of the organic layer and aqueous solutions. 3-Methyl-4-nitrazophenol is very poorly soluble in the reaction mixture. On an industrial scale, it is often the case that incrustations are formed on the reactor walls, stirrers, etc., while the 3-methylphenol moieties remain unreacted and the encrustations themselves reduce heat transfer through the reactor core, and local overheating of the reaction mixture may occur.

VySšie uvedené nedostatky sú zmiernené spSsobom výroby 3-metyl-4-nitrózofenolu,podstata ktorého spočívá v tom, že 3*-metylfenol sa nitrozuje s vodným roztokom dusi-tanu sodného v přítomnosti minerálnej kyseliny, najčastejšie kyseliny sírovéj alebochlorovodíkovéj.The aforementioned drawbacks are alleviated by the process for the preparation of 3-methyl-4-nitrosophenol, wherein 3-methylphenol is nitrosated with an aqueous solution of sodium nitrite in the presence of a mineral acid, most commonly sulfuric acid or hydrochloric acid.

Nitrozácia prebieha v přítomnosti tenzidu. Výhodou postupu podlá vynálezu je, že pri výrobě 3-metyl-4-nitrózofenolu sa ne-tvoria inkrusty na stěnách reakčnej aparatuře, ktorá zhoršovali přestup tepla, čímmohlo nastati miestne prehriatie. Po ukončení výroby 3-metyl-4-nitrúzofenolu sa muse-li inkrusty odstrániti, čo. bolo podstatná a sp8Bobovalo časová a materiálně stráty.Tenzid zabezpečuje lepší styk organickej i anorganickej časti kvapalnej fázy a reak-cia m3že prebiehati čiastočne v emulzii, ktorá umožňuje váččiu reakčnú rýchlosti ako ilepší odvod tepla. ’ Příklad 1Nitrosation occurs in the presence of a surfactant. An advantage of the process according to the invention is that in the production of 3-methyl-4-nitrosophenol there are no incrustations on the walls of the reaction apparatus which impair the heat transfer, thereby causing local overheating. After the production of 3-methyl-4-nitrosophenol has been completed, the incrustation must be removed. The surfactant provides better contact between the organic and inorganic portions of the liquid phase and the reaction can take place in part in the emulsion, which allows the poultry reaction rate to be better than heat dissipation. Example 1

Do reakčnej banky sa dalo 340 g 60,3 % hmot. kyseliny sírovéj a 35 g 3-metyl-fenolu a 2 mg etylenoxidovaný adukt kyseliny nanoolejovej s počtom etylenoxidovýchjedno tisk 19 až 24 (SlovaeolBL). Zmes sa za miešanla ochladila na 0 °C. Potom sak zmesi přidávalo počas 90 minut 70 g 38 % hmot. vodného roztoku NaNOg. Po ukončenípremývania sa suspenzia odfiltrovala a premyla s 100 ml vody. Piltračný koláč o hmot-nosti 44,3 g obsahoval 99 % hmot. 3-metyl-4-nitrozofenolu. Příklad 2340 g of 60.3% by weight were added to the reaction flask. sulfuric acid and 35 g of 3-methylphenol and 2 mg of ethylene oxide oxidation adduct of nanoic acid with ethylene oxide print 19 to 24 (SlovaeolBL). The mixture was cooled to 0 ° C with stirring. Then, 70 g of 38 wt. NaNO 3 aqueous solution. After washing, the suspension was filtered and washed with 100 mL of water. The 44.3 g filter cake contained 99 wt. 3-methyl-4-nitrosophenol. Example 2

Do reakčného kotlá sa dalo 1 220 1 60-,3 % hmot. kyseliny sírovéj, ktorá sa vy-chladila na 5 °C. Potom sa k roztoku HgSO^ přidalo 183 1 3-metylfenolu a 0,02 1 20 %hmot. vodného roztoku dodecylbenzánsulfonanu sodného (Abeson NAM). Potom se po ochla-dení na 0 °C začalo dávkovat za miešania pod hladinu 300 1 38 % hmot. vodného rozto-ku dusitanu sodného, pričom teplota nepresiahla 5 °C. Doba dávkovania bola 160 min.Reakčná zmes sa miešala ešte 30 minút. Získaná suspenzia obsahovala v přepočítaní235 kg 100 % hmot 3-metyl-4-nitrózofenolu.1,220 l of 60-, 3 wt. sulfuric acid, which was cooled to 5 ° C. Then 183 l of 3-methylphenol and 0.02 l of 20 wt. aqueous sodium dodecylbenzanesulfonate solution (Abeson NAM). Then, after cooling to 0 ° C, a weight of 300 wt. aqueous sodium nitrite solution while the temperature does not exceed 5 ° C. The dosing time was 160 min. The reaction mixture was stirred for 30 minutes. The obtained suspension contained, on the basis of 235 kg, 100% by weight of 3-methyl-4-nitrosophenol.

Vynález sa uplatní pri výrobě 3-metyl-4-nitrózofenolu, ktorý je medziproduktpri výrobě viacerých organických látok, například 0,0-dimetyl-0-/3-metyl-4-nitrofe-nyl/tiofosfátu.The invention is applicable to the production of 3-methyl-4-nitrosophenol which is an intermediate in the production of several organic substances, for example O, O-dimethyl-O- (3-methyl-4-nitrophenyl) thiophosphate.

Claims (1)

PREDMET VYNÁLEZUOBJECT OF THE INVENTION Sp6sob výroby 3-metyl-4-nitrózofenolu nitrozáciou 3-metyIfenolu s vodným roztokom dusitanu sodného v prostředí minerálnej kyseliny vyznačujúci sa tým, že nitrozácia sa robí v přítomnosti tenzidu.Process for the preparation of 3-methyl-4-nitrosophenol by nitrosation of 3-methylphenol with an aqueous solution of sodium nitrite in a mineral acid medium, characterized in that the nitrosation is carried out in the presence of a surfactant.
CS881210A 1988-02-25 1988-02-25 Process for producing 3-methyl-4-nitrosophenol CS270521B1 (en)

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CS270521B1 true CS270521B1 (en) 1990-07-12

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