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    • 64. 发明授权
    • Process for the continuous production of saturated aliphatic dicarboxylic acids
    • 连续生产饱和脂肪族二羧酸的方法
    • US3880921A
    • 1975-04-29
    • US34812473
    • 1973-04-05
    • HUELS CHEMISCHE WERKE AG
    • HELLEMANNS GERHARDROHL HERMANNHEGENBERG PETEREVERSMANN WERNER
    • C07C55/02B01J10/00B01J19/24C07C51/00C07C51/31C07C67/00C07C51/18C07C55/04
    • C07C51/316B01J19/2435
    • Process and apparatus for the continuous production of saturated aliphatic dicarboxylic acids by the catalyzed nitric acid oxidation of the corresponding cycloalkanols and cycloalkanones with recirculation of the reaction sludge and the reaction gases, which comprises cooling the reaction sludge by passing it through the tubes of a multiple tube heat exchanger, separating the reaction gases downstream of the heat exchanger, and dispersing the recycled portion of the reaction gases in the reaction sludge upstream of the heat exchanger, in a volume amount 0.1 to 2.0 times the volume of the reaction sludge circulating per unit time and in a pressure ratio of initial gas pressure to pressure in the circulation reactor at the gas feed point of (x + 0.25) : x to (x + 1.5) : x, wherein x is the pressure at the gas feed point, to form a homogeneously dispersed three-phase mixture of the recycled reaction gases in the reaction sludge in the tubes of the heat exchanger.
    • 通过反应淤渣和反应气体的再循环,通过反应淤渣和反应气体的再循环,通过催化硝酸氧化相应的环烷醇和环烷酮来连续生产饱和脂族二羧酸的方法和装置,其包括通过将反应淤渣通过多个管 分离热交换器下游的反应气体,并将反应气体的再循环部分分散在热交换器上游的反应污泥中,体积为每单位循环的反应污泥的体积的0.1至2.0倍 (x + 0.25):x至(x + 1.5):x处的循环反应器中的初始气体压力与压力的压力比,其中x是气体进料点处的压力, 在热交换器的管中的反应污泥中形成均匀分散的三相循环反应气体的三相混合物。