DISTILLATIVE PURIFICATION OF 2,5-DIOXO-1-OXA-2-PHOSPHOLANES

    公开(公告)号:CA1055877A

    公开(公告)日:1979-06-05

    申请号:CA256929

    申请日:1976-07-14

    Applicant: HOECHST AG

    Abstract: 2,5 dioxo-1-oxa-2-phospholanes of the general formula: in which R1 stands for a n alkyl radical having form 1 to 4 carbon atoms, or a phenyl radical, and R2 and R3 each stand for hydrogen or CH3, are distillativelypurified. To this end the respective crude compound is preheated to 120 to 160.degree.C and fed to the head of a distilling column provided with a plurality of individually heatable trays maintained at temperatures increasing from the upper-most tray to the lowermost, the uppermost tray in the column being maintained at 160 to 200.degree.C, the pressure at the head of the column being 20 to 200 mm Hg, preferably 50 to 120 mm Hg; an inert gas preheated at 160 to 200.degree.C is introduced countercurrently at the base of the column; those impurities having a boiling point lower than that of the respective 2,5-dioxo-1-oxa-2-phospholane are withdrawn overhead together with the inert gas; the 2,5-dioxo-1-oxa-2-phospholane thus freed from low-boiling impurities is withdrawn from the base of the distilling column and passed to a film evaporator; and the 2,5-dioxo-1-oxa-2-phospholane is distilled off from higher-boiling impurities in the film evaporator under a pressure of 0.1 to 5 mm Hg.

    6.
    发明专利
    未知

    公开(公告)号:DE2531920B1

    公开(公告)日:1976-10-21

    申请号:DE2531920

    申请日:1975-07-17

    Applicant: HOECHST AG

    Abstract: 2,5 DIOXO-1-OXA-2-PHOSPHOLANES OF THE GENERAL FORMULA: in which R1 stands for an alkyl radical having from 1 to 4 carbon atoms, or a phenyl radical, and R2 and R3 each stand for hydrogen or CH3, are distillatively purified. To this end the respective crude compound is preheated to 120 DEG to 160 DEG C and fed to the head of a distilling column provided with a plurality of individually heatable trays maintained at temperatures increasing from the upper-most tray to the lowermost, the uppermost tray in the column being maintained at 120 DEG to 160 DEG C and the lowermost tray being maintained at 160 DEG to 200 DEG C, the pressure at the head of the column being 20 to 200 mm Hg, preferably 50 to 120 mm Hg; an inert gas preheated to 160 DEG to 200 DEG C is introduced countercurrently at the base of the column; those impurities having a boiling point lower than that of the respective 2,5-dioxo-1-oxa-2-phospholane are withdrawn overhead together with the inert gas; the 2,5-dioxo-1-oxa-2-phospholane thus freed from low-boiling impurities is withdrawn from the base of the distilling column and passed to a film evaporator; and the 2,5-dioxo-1-oxa-2-phospholane is distilled off from higher-boiling impurities in the film evaporator under a pressure of 0.1 to 5 mm Hg.

    8.
    发明专利
    未知

    公开(公告)号:DD131026A5

    公开(公告)日:1978-05-24

    申请号:DD20000477

    申请日:1977-07-12

    Applicant: HOECHST AG

    Abstract: Production of methyldichlorophosphane. The compound is made by reacting methane and phosphorus trichloride in a reaction zone in which a temperature higher than 500 DEG C is maintained. More specifically, hot reaction gas coming from the reaction zone is mechanically freed from solid matter, and the reaction gas freed from solid matter is passed to a quenching zone in which it is quenched with liquefied reaction mixture having 0.3 to 5 weight % of an organic barium compound or a non-ionic surfactant dissolved therein.

    9.
    发明专利
    未知

    公开(公告)号:CH598272A5

    公开(公告)日:1978-04-28

    申请号:CH689176

    申请日:1976-06-01

    Applicant: HOECHST AG

    Abstract: 2,5 DIOXO-1-OXA-2-PHOSPHOLANES OF THE GENERAL FORMULA: in which R1 stands for an alkyl radical having from 1 to 4 carbon atoms, or a phenyl radical, and R2 and R3 each stand for hydrogen or CH3, are distillatively purified. To this end the respective crude compound is preheated to 120 DEG to 160 DEG C and fed to the head of a distilling column provided with a plurality of individually heatable trays maintained at temperatures increasing from the upper-most tray to the lowermost, the uppermost tray in the column being maintained at 120 DEG to 160 DEG C and the lowermost tray being maintained at 160 DEG to 200 DEG C, the pressure at the head of the column being 20 to 200 mm Hg, preferably 50 to 120 mm Hg; an inert gas preheated to 160 DEG to 200 DEG C is introduced countercurrently at the base of the column; those impurities having a boiling point lower than that of the respective 2,5-dioxo-1-oxa-2-phospholane are withdrawn overhead together with the inert gas; the 2,5-dioxo-1-oxa-2-phospholane thus freed from low-boiling impurities is withdrawn from the base of the distilling column and passed to a film evaporator; and the 2,5-dioxo-1-oxa-2-phospholane is distilled off from higher-boiling impurities in the film evaporator under a pressure of 0.1 to 5 mm Hg.

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