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    • 3. 发明授权
    • Recovery of caprolactam from caprolactam distillation low boilers or
high boilers or mixtures thereof
    • 从己内酰胺蒸馏低沸点锅炉或高锅炉或其混合物中回收己内酰胺
    • US4882430A
    • 1989-11-21
    • US257274
    • 1988-10-13
    • Gerald NeubauerEmile De DeckerHugo FuchsBernhard HolzknechtJosef Ritz
    • Gerald NeubauerEmile De DeckerHugo FuchsBernhard HolzknechtJosef Ritz
    • C07D201/16
    • C07D201/16
    • Caprolactam is recovered from caprolactam distillation low boilers or high boilers or mixtures thereof by the following steps:(a) crystallizing a low or high boiler or a mixture thereof to form purified capro-lactam crystals and a mother liquor,(b) separating off the purified caprolactam crystals to leave a mother liquor,(c) recycling from 5 to 90% by weight of the mother liquor of stage (b) into stage (a) and transferring the remainder of the mother liquor into the subsequent stage (d),(d) crystallizing the remaining mother liquor portion from stage (c) to form caprolactam crystals and a mother liquor, separating off the caprolactam crystals of stage(e) (d) and recycling the same into stage (a) to leave a mother liquor,(f) recycling from 20 to 99% by weight of mother liquor of stage (e) into stage (d) and channeling out the remainder of the impurity-containing mother liquor of stage (e).
    • 通过以下步骤从己内酰胺蒸馏低锅炉或高锅炉或其混合物回收己内酰胺:(a)使低或高锅炉或其混合物结晶以形成纯化的己内酰胺结晶和母液,(b)将 纯化的己内酰胺晶体离开母液,(c)将阶段(b)的母液的5至90重量%循环到阶段(a)中,并将剩余的母液转移到后续阶段(d)中, (d)从阶段(c)中将剩余的母液部分结晶以形成己内酰胺晶体和母液,分离阶段(e)(d)的己内酰胺晶体并将其再循环到阶段(a)中以留下母液 ,(f)将阶段(e)的母液的20至99重量%循环到阶段(d)中,并且引出阶段(e)的含杂质母液的剩余部分。