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    • 91. 发明授权
    • Process for recovering and purifying caprolactam from an organic solvent
    • 从有机溶剂中回收和纯化己内酰胺的方法
    • US06849731B2
    • 2005-02-01
    • US10468263
    • 2002-02-27
    • Maria Louisa Christina Dsinter-De HondtJoannes Albertus Wilhelmus Lemmens
    • Maria Louisa Christina Dsinter-De HondtJoannes Albertus Wilhelmus Lemmens
    • C07D201/16
    • C07D201/16
    • Process for recovering caprolactam from a solution comprising caprolactam dissolved in an organic solvent, said process comprising: a) washing the solution with water or an aqueous alkaline solution, resulting in a washed solution comprising caprolactam and organic solvent and in a washing residue, b) evaporating organic solvent from the washed solution, resulting in caprolactam product, c) optionally, hydrogenating the caprolactam product, d) optionally, evaporating water from the caprolactam product, e) distilling the caprolactam product to recover caprolactam and a distillation residue, f) extracting the distillation residue with an organic solvent in the presence of water to obtain (i) an extract comprising caprolactam dissolved in organic solvent and (ii) an aqueous effluent, and g) recycling the extract to step a) or b).
    • 从包含溶解在有机溶剂中的己内酰胺的溶液中回收己内酰胺的方法,所述方法包括:a)用水或碱性水溶液洗涤溶液,得到包含己内酰胺和有机溶剂的洗涤溶液,并在洗涤残渣中,b) 从洗涤的溶液中蒸发有机溶剂,得到己内酰胺产物,c)任选地使己内酰胺产物氢化,d)任选地从己内酰胺产物蒸发水,e)蒸馏己内酰胺产物以回收己内酰胺和蒸馏残渣,f) 在水的存在下用有机溶剂蒸馏残余物,得到(i)包含溶解在有机溶剂中的己内酰胺的提取物和(ii)含水流出物,和g)将提取物再循环到步骤a)或b)。
    • 97. 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。
    • 99. 发明授权
    • Method for recovering caprolactam
    • 己内酰胺回收方法
    • US4764607A
    • 1988-08-16
    • US945117
    • 1986-12-22
    • Laszlo J. BalintJulius Greenburg
    • Laszlo J. BalintJulius Greenburg
    • C07D201/16
    • C07D201/16
    • Method and improved apparatus for recovering a volatile organic material, such as caprolactam, from a liquid mixture of organic and inorganic materials are disclosed. The method features the step of mixing the liquid mixture with superheated steam for 0.005 to 1.0 second to vaporize a large portion of the volatile organic material without degrading the organic materials. The steam and vaporized organic materials are then separated from the liquid mixture remaining, followed by separation of the vaporized organic material from the steam. The vaporized organic material subsequently is condensed. The improved apparatus features means for introducing superheated steam into a vaporizer feed pipe, as well as means for mixing the superheated steam with the liquid mixture in the pipe for 0.005 to 1.0 second so that a large portion of the volatile organic material is vaporized and feeds with the steam and remaining liquid mixture into the vaporizer for separation.
    • 公开了用于从有机和无机材料的液体混合物中回收挥发性有机材料如己内酰胺的方法和改进的装置。 该方法的特征在于将液体混合物与过热蒸汽混合0.005至1.0秒以蒸发大部分挥发性有机材料而不降解有机材料。 然后将蒸汽和蒸发的有机材料与剩余的液体混合物分离,然后将蒸发的有机材料与蒸汽分离。 蒸发的有机材料随后被冷凝。 改进的装置具有用于将过热蒸汽引入蒸发器进料管的装置,以及用于将过热蒸汽与管中的液体混合物混合0.005至1.0秒的装置,使得大部分挥发性有机材料蒸发并进料 蒸汽和剩余的液体混合物进入蒸发器进行分离。