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Method and device for the continuous return of extract water in the polyamide production process

机译:在聚酰胺生产过程中连续回收提取水的方法和装置

摘要

Continuously recycling extract waters in polyamide production process comprises polymerizing, granulating and subsequently extracting the granules with water. The method comprises concentrating the extract water of at least one production line, subjecting the extract water as an extract water flow to re-polymerizator for degradation of cyclic oligomers, diluting the extract water as re-polymerization with at least an inflow and subsequently supplying as a mixed stream of the polymerization. Continuously recycling extract waters in polyamide production process comprises polymerizing, granulating and subsequently extracting the granules with water. The method comprises concentrating the extract water of at least one production line, subjecting the extract water as an extract water flow to re-polymerization for degradation of cyclic oligomers, diluting the extract water as re-polymerizate with at least an inflow, and subsequently supplying as a mixed stream of the polymerization. The temperature is adjusted to 220-280[deg] C, the water content is adjusted to 20-40 wt.% and the residence time is adjusted to 0.5-20 hours to maximize the oligomer degradation during the re-polymerization. The pressure formation is reduced by metering at least one inflow containing caprolactam for direct supply of the mixed stream in the production process of polyamide. An independent claim is also included for a device for continuously recycling the extract water in polyamide production process comprising (a) re-polymerizator for degradation of cyclic oligomers, (b) a premixer for mixing fresh lactum, optionally additives and mixed stream, (c) a bypass for recycling the circular flow, which is branched into the premixer and dosed at a feed point prior to the premixer, and (d) a pump, which is arranged in the bypass, for conveying the circular flow.
机译:在聚酰胺生产过程中连续回收提取水包括聚合,制粒,然后用水提取颗粒。该方法包括浓缩至少一条生产线的提取水,将提取水作为提取水流进行再聚合器以降解环状低聚物,以至少流入的方式稀释提取水以进行再聚合,随后供应聚合的混合流。在聚酰胺生产过程中连续回收提取水包括聚合,制粒,然后用水提取颗粒。该方法包括浓缩至少一条生产线的提取水,使作为提取水流的提取水进行再聚合以降解环状低聚物,通过至少流入物稀释作为再聚合的提取水,然后供应作为聚合的混合物流。将温度调节至220-280℃,将水含量调节至20-40wt。%,并将停留时间调节至0.5-20小时,以使再聚合期间的低聚物降解最大化。通过计量至少一种含有己内酰胺的流入物来减少压力形成,以在聚酰胺的生产过程中直接供应混合料流。还包括用于在聚酰胺生产过程中连续回收萃取水的装置的独立权利要求,该装置包括(a)用于降解环状低聚物的再聚合器,(b)用于混合新鲜乳,任选的添加剂和混合料流的预混合器,(c )用于循环循环流的旁路,该旁路分支到预混合器中,并在预混合器之前的进料点处计量;以及(d)泵,该泵布置在旁路中,用于输送循环流。

著录项

  • 公开/公告号EP2784102B1

    专利类型

  • 公开/公告日2015-12-09

    原文格式PDF

  • 申请/专利权人 UHDE INVENTA-FISCHER GMBH;

    申请/专利号EP20130161146

  • 发明设计人 KATZER JOHANNES;SIEBECKE EKKEHARD;

    申请日2013-03-26

  • 分类号C08G69/46;C08G69/16;C08J11/02;B01F5/06;B01F5/10;

  • 国家 EP

  • 入库时间 2022-08-21 14:49:51

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