Liq. phase oxidn. of cyclohexane

Cyclohexane is oxidised in the liq. phase under press. with O2-contg. gases in the presence of catalysts such as salts of metals with variable valency, esp. Co naphthenate, to a degree of conversion of up to 5 % in more than one reaction stage in a multistage gas injecion tube system, while maintain...

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Hauptverfasser: KASZNIA ANDRZEJ, POHORECKI RYSZARD, MACIEJCZYK STANISLAW, USZYNSKI ALEKSANDER, CIBOROWSKI STANISLAW, GUCWA ANTONI JANUSZ, LUBIEWA-WIELEZYNSKI WOJCIECH, SCHIMMELPFENNIG ZBIGNIEW, JANITZ ALINA, WAIS JAN, VIEWEGER TADEUSZ, MARCHWIANY HENRYK, RYGIEL STANISLAW, ZYLBERSTEJN MICHAL, SZPARSKI JOZEF, WOJCIK ZBIGNIEW, BALCERZAK KAZIMIERZ, KRZYSZTOFORSKI ANDRZEJ, POCHWALSKI MAREK
Format: Patent
Sprache:eng ; spa
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Zusammenfassung:Cyclohexane is oxidised in the liq. phase under press. with O2-contg. gases in the presence of catalysts such as salts of metals with variable valency, esp. Co naphthenate, to a degree of conversion of up to 5 % in more than one reaction stage in a multistage gas injecion tube system, while maintaining a limited oxygen concn. within the liq. phase. - Pref. the oxidn. is carried out in the presence of Co naphthenate in a concn. of 0.2 - 5 ppm, esp. 0.5 - 2 ppm in the reactor and with a max. concn. of oxygen in the liq. phase (in mol/dm3 x 10 power -4). Cyclohexane is oxidised in the liq. phase under press. with O2-contg. gases in the presence of catalysts such as salts of metals with variable valency, esp. Co naphthenate, to a degree of conversion of up to 5 % in more than one reaction stage in a multistage gas injecion tube system, while maintaining a limited oxygen concn. within the liq. phase. - Pref. the oxidn. is carried out in the presence of Co naphthenate in a concn. of 0.2 - 5 ppm, esp. 0.5 - 2 ppm in the reactor and with a max. concn. of oxygen in the liq. phase (in mol/dm3 x 10 power -4). (Machine-translation by Google Translate, not legally binding) PROCEDIMIENTO DE OXIDACION DE CICLOHEXANO EN FASE LIQUIDA, MEDIANTE GASES CONTENIENDO OXIGENO, EN PRESENCIA DE CATALIZADORES QUE CONTIENEN SALES DE METALES DE VALENCIA VARIABLE, PARTICULARMENTE NAFTENATO DE COBALTO, A TEMPERATURAS COMPRENDIDAS ENTRE 150 Y 200GC, MANTENIENDOSE EL GRADO DE CONVERSION HASTA 5% Y 200GC, MANTENIENDOSE EL GRADO DE CONVERSION HASTA 5%, Y CUYO PROCEDIMIENTO SE REALIZA EN UN SISTEMA DE BORBOTEO DE MAS DE UNA ETAPA DE REACCION, CARACTERIZADO PORQUE SE MANTIENE UNA CONCENTRACION DE OXIGENO LIMITADA EN LA FASE LIQUIDA.LA INVENCION RESUELVE EL PROBLEMA DE PODER INCREMENTAR LA SELECTIVIDAD DEL PROCESO DE OXIDACION DE CICLOHEXANO EN FASE LIQUIDA.