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    • 1. 发明授权
    • Recovery of caprolactam from oligomers and/or polymers of caprolactam
    • 从己内酰胺的低聚物和/或聚合物中回收己内酰胺
    • US5700358A
    • 1997-12-23
    • US396623
    • 1995-03-01
    • Hugo FuchsJosef RitzGerald Neubauer
    • Hugo FuchsJosef RitzGerald Neubauer
    • C07D201/12C07D201/16C08G69/14C08G69/46B01D3/34
    • C07D201/12C07D201/16
    • Caprolactam is recovered from oligomers and/or polymers of caprolactam by cleavage of oligomers and/or polymers of caprolactam and subsequent working up by distillation of the caprolactam obtained in the cleavage, by a process including (a) cleaving oligomers and/or polymers of caprolactam to obtain an aqueous reaction mixture which contains caprolactam, (b) removing water from the reaction mixture obtained under (a) to obtain a residue, (c) distilling the residue obtained under (b) in an acidic medium and (d) then distilling the distillate in an alkaline medium to obtain caprolactam, or (c') distilling the residue obtained under (b) in an alkaline medium and (d') then distilling the distillate in an acidic medium to obtain caprolactam.
    • 通过裂解己内酰胺的低聚物和/或聚己内酯并随后通过蒸馏在切割中获得的己内酰胺来处理己内酰胺从己内酰胺的低聚物和/或聚合物中回收己内酰胺,方法包括(a)裂解己内酰胺的低聚物和/或聚合物 得到含有己内酰胺的水性反应混合物,(b)从(a)得到的反应混合物中除去水,得到残渣,(c)将酸性介质中的(b)得到的残渣蒸馏,然后蒸馏 在碱性介质中的馏出物得到己内酰胺,或(c')将在(b)获得的残余物在碱性介质中蒸馏,然后(d'),然后在酸性介质中蒸馏出馏出物,得到己内酰胺。
    • 7. 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。