Method for making polyamides
    2.
    发明授权
    Method for making polyamides 有权
    制造聚酰胺的方法

    公开(公告)号:US06696544B1

    公开(公告)日:2004-02-24

    申请号:US10009523

    申请日:2002-08-08

    CPC classification number: C08G69/28 C08G69/04

    Abstract: The invention concerns a method for making polyamide. More particularly, the invention concerns a method for making polyamides derived from the reaction between a diacid and a diamine. It concerns a method for making a polyamide derived from the reaction of at least a diacid with at least a polyamide comprising the following steps: preparing a first mixture of diacid and diamine with a diacid/diamine molar ratio ranging between 0.8 and 0.995, preferably ranging between 0.95 and 0.99 in a first reactor (5); preparing a second mixture of diacid and diamine with a diacid/diamine molar ratio ranging between 1.005 and 1.2, preferably between 1.01 and 1.05, in a second reactor (4); introducing in melted form a first flow of the first mixture and a second flow of the second mixture in a stirred polymer reactor (7); drawing, preferably, continuously, from said reactor a flow of polyamide prepolymer; feeding said polyamide flow into a finishing step to obtain the desired degree of polymerisation. The invention is characterised in that the stoichiometry of the polyamide in the reactor (7) or the acid function/amine function ratios in the different reactors are measured by near infrared spectrometric analysis, and by controlling the feed flows in the different reactors using the results of said analyses.

    Abstract translation: 本发明涉及一种制备聚酰胺的方法。 更具体地说,本发明涉及一种制备衍生自二酸和二胺之间的反应的聚酰胺的方法。 它涉及制备衍生自至少二酸与至少一种聚酰胺的聚酰胺的聚酰胺的方法,包括以下步骤:制备二酸和二胺的二元酸/二胺摩尔比范围在0.8-0.995之间的第一混合物, 在第一反应器(5)中在0.95和0.99之间; 在第二反应器(4)中制备二酸和二胺的二酸/二胺摩尔比在1.005和1.2之间,优选在1.01和1.05之间的第二混合物; 以熔融形式将第一混合物的第一流和第二混合物的第二流引入搅拌聚合反应器(7)中; 优选连续地从所述反应器中抽出聚酰胺预聚物流; 将所述聚酰胺流进料到精整步骤中以获得所需的聚合度。 本发明的特征在于通过近红外光谱分析测量反应器(7)中聚酰胺的化学计量或不同反应器中酸功能/胺官能团的比例,并通过使用结果控制不同反应器中的进料流量 的分析。

    Continuous production of polyamides
    3.
    发明授权
    Continuous production of polyamides 有权
    连续生产聚酰胺

    公开(公告)号:US08759475B2

    公开(公告)日:2014-06-24

    申请号:US12593080

    申请日:2008-03-25

    CPC classification number: C08G69/04 C08G69/08 C08G69/16 C08G69/28

    Abstract: Polyamides, e.g., polyhexamethylene adipamide, are continuously produced via the following stages: Stage 1: into and through a reactor, polycondensing a liquid stream which contain the polyamide monomer(s) at a pressure P1 greater than atmospheric pressure, the stream of material at the outlet of the reactor including a vapor phase which contains steam and a liquid phase which at least contains the product of polycondensation; Stage 2: feeding the outlet stream of material into a chamber, evacuating at least a portion of the vapor phase therefrom and recovering at least the liquid phase which at least contains the product of polycondensation, the pressure P2 in the chamber being regulated at a set value such that it is greater than atmospheric pressure and the residence time of said liquid phase in the chamber being less than 5 minutes; and Stage 3: pressure reducing at least the liquid phase which at least contains the stream of polycondensation product recovered during Stage 2.

    Abstract translation: 聚酰胺,例如聚己二酰己二胺,通过以下阶段连续生产:阶段1:进入和通过反应器,将含有聚酰胺单体的液体流以大于大气压的压力P1缩聚, 反应器的出口包括含有蒸汽的气相和至少含有缩聚产物的液相; 阶段2:将物料的出口物料供给到室中,从其中排出至少一部分气相,并至少回收至少含有缩聚产物的液相,将室内的压力P2调节到一组 使得其大于大气压,并且所述液相在室中的停留时间小于5分钟; 和阶段3:减压至少含有在阶段2期间回收的缩聚产物流的液相。

    CONTINUOUS PRODUCTION OF POLYAMIDES
    4.
    发明申请
    CONTINUOUS PRODUCTION OF POLYAMIDES 有权
    连续生产聚氨酯

    公开(公告)号:US20100144986A1

    公开(公告)日:2010-06-10

    申请号:US12593080

    申请日:2008-03-25

    CPC classification number: C08G69/04 C08G69/08 C08G69/16 C08G69/28

    Abstract: Polyamides, e.g., polyhexamethylene adipamide, are continuously produced via the following stages:Stage 1: into and through a reactor, polycondensing a liquid stream which contain the polyamide monomer(s) at a pressure P1 greater than atmospheric pressure, the stream of material at the outlet of the reactor including a vapor phase which contains steam and a liquid phase which at least contains the product of polycondensation;Stage 2: feeding the outlet stream of material into a chamber, evacuating at least a portion of the vapor phase therefrom and recovering at least the liquid phase which at least contains the product of polycondensation, the pressure P2 in the chamber being regulated at a set value such that it is greater than atmospheric pressure and the residence time of said liquid phase in the chamber being less than 5 minutes; andStage 3: pressure reducing at least the liquid phase which at least contains the stream of polycondensation product recovered during Stage 2.

    Abstract translation: 聚酰胺,例如聚己二酰己二胺,通过以下阶段连续生产:阶段1:进入和通过反应器,将含有聚酰胺单体的液体流以大于大气压的压力P1缩聚, 反应器的出口包括含有蒸汽的气相和至少含有缩聚产物的液相; 阶段2:将物料的出口物料供给到室中,从其中排出至少一部分气相,并至少回收至少含有缩聚产物的液相,将室内的压力P2调节到一组 使得其大于大气压,并且所述液相在室中的停留时间小于5分钟; 和阶段3:减压至少含有在阶段2期间回收的缩聚产物流的液相。

    Production of Spherical Polyamide Particles
    5.
    发明申请
    Production of Spherical Polyamide Particles 有权
    球形聚酰胺颗粒的生产

    公开(公告)号:US20070269656A1

    公开(公告)日:2007-11-22

    申请号:US10562051

    申请日:2004-06-22

    CPC classification number: C08J3/14 C08G69/04 C08G69/28 Y10T428/2982

    Abstract: Spherical polyamide particles having a mean particle size of less than 1 mm, notably less than 100 μm, are produced by dispersing the polyamide monomers in an inert liquid and then polymerizing same.

    Abstract translation: 平均粒径小于1mm,特别是小于100μm的球形聚酰胺颗粒是通过将聚酰胺单体分散在惰性液体中,然后进行聚合制备的。

    Production of spherical polyamide particles
    7.
    发明授权
    Production of spherical polyamide particles 有权
    球形聚酰胺颗粒的生产

    公开(公告)号:US07740938B2

    公开(公告)日:2010-06-22

    申请号:US10562051

    申请日:2004-06-22

    CPC classification number: C08J3/14 C08G69/04 C08G69/28 Y10T428/2982

    Abstract: Spherical polyamide particles having a mean particle size of less than 1 mm, notably less than 100 μm, are produced by dispersing the polyamide monomers in an inert liquid and then polymerizing same.

    Abstract translation: 平均粒度小于1mm,特别是小于100μm的球形聚酰胺颗粒是通过将聚酰胺单体分散在惰性液体中,然后进行聚合制备的。

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