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    • 3. 发明授权
    • Process and device for the standardized continuous production of
polyamides
    • 标准化连续生产聚酰胺的工艺和装置
    • US6136947A
    • 2000-10-24
    • US77737
    • 1998-11-13
    • Karlheinz WiltzerPeter LausmannBaldur Ebert
    • Karlheinz WiltzerPeter LausmannBaldur Ebert
    • C08G69/04C08G69/16C08G69/28C08G69/36
    • C08G69/16C08G69/04C08G69/28C08G69/36Y02P20/582
    • A process and device for the standardised continuous production of polyamide 6, polyamide 6.6 and/or copolyamides from e-caprolactam and/or adipic acidic hexamethylenediamine or adipic acid and hexamethylenediamine uses a combination of known specific processes to design a polymerisation reactor in which product with sufficiently high quality can be produced with the most efficient possible use of the energy applied and in such a way that the initial substances can be used alternately in the individual processing stages: pre-heating of the initial products using a common heat exchanger to 190-300.degree. C.; polymerisation of the initial products in a pressure stage with or without elimination of water and product recycling at 150-280.degree. C. and a pressure of
    • PCT No.PCT / EP96 / 05514 Sec。 371日期:1998年11月13日 102(e)1998年11月13日PCT PCT 1996年12月10日PCT公布。 WO90 / 21758 PCT公开号 日期1996年6月19日由ε-己内酰胺和/或己二酸的六亚甲基二胺或己二酸和六亚甲基二胺的聚酰胺6,聚酰胺6.6和/或共聚酰胺的标准连续生产的方法和装置使用已知的具体方法的组合来设计聚合 反应器,其中可以以最有效的可能使用所施加的能量并且以这样的方式产生具有足够高质量的产品,使得初始物质可以在各个处理阶段中交替使用:使用共同的预热初始产品 热交换器至190-300℃。 在150-280℃,压力<20bar的压力阶段使初始产品聚合,在低压还原的情况下将聚合物熔体在一至五圈的线圈中脱水; 以及在210-285℃的温度下在至少一个常见的立式反应器中熔体的最终冷凝。
    • 5. 发明申请
    • Method and Device for Continuously Producing Copolyamides with Melting Points Gr Eater Than 265 C
    • 用于连续生产熔点高于265℃的共聚酰胺的方法和装置
    • US20080051527A1
    • 2008-02-28
    • US11630217
    • 2005-05-21
    • Karlheinz WiltzerGunda MorgensternPeter Lausmann
    • Karlheinz WiltzerGunda MorgensternPeter Lausmann
    • C08F2/01
    • C08G69/265C08G69/28
    • The invention relates to a method for continuously producing copolyamides with melting points greater than approximately 265° C. According to the invention, in a continuous process, partially aromatic and partially crystalline polyamides of the following chemical systems with defined molar percentages of the individual components are produced during the synthesis of polymers: 30 to 50 mol % of aromatic dicarboxylic acids, which are derived from terephthalic acid; 30 to 50 mol % of aliphatic diamines, which are derived from hexamethylenediamine or of cycloaliphatic diamines having at least 6 C atoms, and; 0.5-25 mol % of aromatic diamines or cyclic diamines with at least 6 C atoms. The sum of all polymer-forming components add up to a composition of 100 mol %, and a stoichiometric ratio between amines and carboxylic acids exists.
    • 本发明涉及一种用于连续生产熔点大于约265℃的共聚酰胺的方法。根据本发明,在连续方法中,具有确定的各组分摩尔百分数的以下化学体系的部分芳族和部分结晶聚酰胺是 在合成聚合物期间产生的:30-50摩尔%的衍生自对苯二甲酸的芳族二羧酸; 衍生自六亚甲基二胺或具有至少6个C原子的脂环族二胺的30至50摩尔%的脂族二胺,和 0.5-25摩尔%的具有至少6个C原子的芳族二胺或环状二胺。 所有聚合物形成组分的总和加起来为100摩尔%的组成,存在胺和羧酸之间的化学计量比。
    • 6. 发明授权
    • Method of continuously producing polyamide 6 using recycled lactam
    • 使用回收的内酰胺连续生产聚酰胺6的方法
    • US5962538A
    • 1999-10-05
    • US29526
    • 1998-02-27
    • Karlheinz WiltzerPeter LausmannBaldur Ebert
    • Karlheinz WiltzerPeter LausmannBaldur Ebert
    • C08G69/16C08G69/46C08J11/04C08G69/14
    • C08G69/46C08G69/16
    • The invention concerns a method of continuously producing polyamide 6 using recycled lactam from extraction and melt-demonomerizing stages. According to the invention, the cyclic oligomers present in the recycled lactam owing to the addition of .epsilon.-caprolactam (fresh lactam) are dissolved in the lactam as a function of the concentration of the oligomers in the product in use, at a dissolution temperature of between 120.degree. C. and 180.degree. C. The solution is then passed to a treatment, the solution preferably being introduced into a closed system and hydrolyzed in the fusible phase under pressure, at water contents of between 3 and 15% and temperatures ranging from 220 to 280.degree. C. With a constant low water content being set, the melt is then fed to the polymerization process in a further pressure stage incorporating a gas chamber (polymerizator).
    • PCT No.PCT / EP96 / 03827 Sec。 371日期1998年2月27日 102(e)1998年2月27日PCT 1996年8月30日PCT公布。 公开号WO97 / 08224 PCT 日期1997年3月16日本发明涉及使用来自萃取和熔融 - 脱单体化阶段的再循环内酰胺连续生产聚酰胺6的方法。 根据本发明,由于加入ε-己内酰胺(新鲜内酰胺)而存在于回收的内酰胺中的环状低聚物作为所使用产物中低聚物浓度的函数溶解在内酰胺中,溶解温度为 在120℃和180℃之间。然后将溶液通过处理,该溶液优选引入封闭体系中,并在可压相中在压力下水解,水含量为3至15%,温度范围为 在恒定的低含水量的情况下,将熔体在进一步加入气室(聚合反应器)的压力阶段中进料到聚合过程中。
    • 7. 发明授权
    • Method and device for continuously producing copolyamides with melting points greater than 265° C.
    • 用于连续生产熔点大于265℃的共聚酰胺的方法和装置
    • US07615606B2
    • 2009-11-10
    • US11630217
    • 2005-05-21
    • Karlheinz WiltzerGunda MorgensternPeter Lausmann
    • Karlheinz WiltzerGunda MorgensternPeter Lausmann
    • C08G69/08
    • C08G69/265C08G69/28
    • The invention relates to a method for continuously producing copolyamides with melting points greater than approximately 265° C. According to the invention, in a continuous process, partially aromatic and partially crystalline polyamides of the following chemical systems with defined molar percentages of the individual components are produced during the synthesis of polymers: 30 to 50 mol % of aromatic dicarboxylic acids, which are derived from terephthalic acid; 30 to 50 mol % of aliphatic diamines, which are derived from hexamethylenediamine or of cycloaliphatic diamines having at least 6 C atoms, and; 0.5-25 mol % of aromatic diamines or cyclic diamines with at least 6 C atoms. The sum of all polymer-forming components add up to a composition of 100 mol %, and a stoichiometric ratio between amines and carboxylic acids exists.
    • 本发明涉及一种用于连续生产熔点大于约265℃的共聚酰胺的方法。根据本发明,在连续方法中,具有确定的各组分摩尔百分数的以下化学体系的部分芳族和部分结晶聚酰胺是 在合成聚合物期间产生的:30-50摩尔%的衍生自对苯二甲酸的芳族二羧酸; 衍生自六亚甲基二胺或具有至少6个C原子的脂环族二胺的30至50摩尔%的脂族二胺,和 0.5-25摩尔%的具有至少6个C原子的芳族二胺或环状二胺。 所有聚合物形成组分的总和加起来为100摩尔%的组成,存在胺和羧酸之间的化学计量比。