INFLUENCE DE LA DISTANCE ENTRE LES DEUX AGITATEURS A TURBINE SUR LES DIVERSES CARACTERISTIQUES D'UN RECIPIENT AGITE HORIZONTALANDO K; FUKUDA T; SATO K et al.1974; KAGAKU KOGAKU; JAP.; DA. 1974; VOL. 38; NO 7; PP. 540-542; ABS. ANGL.; BIBL. 8 REF.Article

ECHANGE D'IONS EN REACTEUR AGITE OUVERTRODRIGUES AE.1973; REV. PORTUG. QUIM.; PORTUG.; DA. 1973; VOL. 15; NO 2; PP. 86-95; ABS. PORT.; BIBL. 7 REF.Article

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