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    • 1. 发明授权
    • Solid-phase drying and solid-phase polymerization of polyamide
    • 聚酰胺的固相干燥和固相聚合
    • US06693163B2
    • 2004-02-17
    • US10098056
    • 2002-03-15
    • Kazumi TanakaHideyuki Kurose
    • Kazumi TanakaHideyuki Kurose
    • C08G6904
    • C08G69/26C08G69/30
    • In the method for solid-phase drying or solid-phase polymerizing a polyamide of the present invention, the polyamide that is stored for 20 days or longer after the production thereof until subjected to the solid-phase drying or the solid-phase polymerization under the specific conditions is used as the starting material. By storing the polyamide under the specific conditions of the present invention, the resultant solid-phase dried or solid-phase polymerized polyamide with a low yellowness is obtained even if 20 days or more time has lapsed after the starting polyamide is produced until it is subjected to the solid-phase drying or solid-phase polymerization.
    • 在固相干燥或固相聚合本发明的聚酰胺的方法中,将聚酰胺在其生产后储存20天或更长时间直到进行固相干燥或固相聚合 使用特定条件作为原料。 通过在本发明的特定条件下储存聚酰胺,即使在起始聚酰胺生产直至其经受之后已经经过了20天或更多的时间,也可获得所得的黄色低的固相干燥或固相聚合的聚酰胺 进行固相干燥或固相聚合。
    • 3. 发明授权
    • Method for producing polyamide 6 of a low extract content, high viscosity stability and low remonomerization rate
    • 低提取物含量的聚酰胺6的制备方法,高粘度稳定性和低再聚合速率
    • US06525167B1
    • 2003-02-25
    • US09913122
    • 2001-08-09
    • Ralf MohrschladtVolker HildebrandtMotonori Yamamoto
    • Ralf MohrschladtVolker HildebrandtMotonori Yamamoto
    • C08G6904
    • C08G69/04C08G69/16
    • The continuous process for producing polyamides by reacting at least one aminonitrile with water comprises the following steps: (10) reacting at least one aminonitrile with water at a temperature of from 200 to 290° C. at a pressure of from 40 to 70 bar in a flow tube containing a Brönsted acid catalyst selected from a beta-zeolite, sheet-silicate or metal oxide catalyst in the form of a fixed bed, (11) diabatically or adiabatically expanding the reaction mixture from step (1) into a first separation zone to a pressure of from 20 to 40 bar, the pressure being at least 10 bar lower than the pressure in step (1), and to a temperature within the range from 220 to 290° C. by flash evaporation and removal of ammonia, water and any aminonitrile monomer and oligomer, (12) further reacting the reaction mixture from step (2) in the presence of water at a temperature of from 200 to 290° C. and a pressure of from 25 to 55 bar and in the presence or absence of a Brönsted acid catalyst selected from a beta-zeolite, sheet-silicate or metal oxide catalyst in the form of a fixed bed, (13) diabatically or adiabatically expanding the reaction mixture from step (3) into a second separation zone to a pressure of from 0.01 to 20 bar, the pressure being at least 20 bar lower than the pressure in step (3), and to a temperature within the range from 220 to 290° C. by flash evaporation and removal of ammonia, water and any aminonitrile monomer and oligomer.
    • 通过使至少一种氨基腈与水反应生产聚酰胺的连续方法包括以下步骤:(10)在200至290℃的温度下,在40至70巴的压力下使至少一种氨基腈与水反应, 含有布朗斯台德酸催化剂的流动管,其选自固体床形式的β-沸石,硅酸盐或金属氧化物催化剂,(11)将反应混合物从步骤(1)进行绝热或绝热膨胀到第一分离区 压力为20至40巴,压力比步骤(1)中的压力低至少10巴,并且通过闪蒸和除去氨,水的温度在220至290℃的范围内 和任何氨基腈单体和低聚物,(12)在水存在下,在200-290℃的温度和25至55巴的压力下,使步骤(2)的反应混合物进一步反应,并在 没有布朗斯台德酸催化剂选择f 以固定床形式的β-沸石,片状硅酸盐或金属氧化物催化剂(13)将步骤(3)的反应混合物从第二分离区中分离或绝热膨胀至压力为0.01至20巴 ,压力比步骤(3)中的压力低至少20巴,并通过闪蒸和氨,水和任何氨基腈单体和低聚物的除去而达到220-290℃的温度。
    • 5. 发明授权
    • Continuous method for producing polyamides from aminonitriles
    • 从氨腈生产聚酰胺的连续方法
    • US06815527B2
    • 2004-11-09
    • US10332579
    • 2003-01-10
    • Peter BasslerHelmut WinterlingRolf-Hartmuth FischerWolfgang Loth
    • Peter BasslerHelmut WinterlingRolf-Hartmuth FischerWolfgang Loth
    • C08G6904
    • C08G69/04C08G69/08C08G69/16
    • The continuous process for preparing a polyamide by reacting at least one aminonitrile with water comprises: (1) reacting at least one aminonitrile with water in the presence of an organic liquid diluent at from 90 to 400° C. and from 0.1 to 35×106 Pa in a flow tube containing a Brönsted acid catalyst selected from a beta-zeolite catalyst, a sheet-silicate catalyst or a titanium dioxide catalyst comprising from 70 to 100% by weight of anatase and from 0 to 30% by weight of rutile and in which up to 40% by weight of the titanium dioxide may be replaced by tungsten oxide, to obtain a reaction mixture, (2) further reacting the reaction mixture at from 150 to 400° C. and a pressure which is lower than the pressure in stage 1 in the presence of a Brönsted acid catalyst selected from a beta-zeolite catalyst, a sheet-silicate catalyst or a titanium dioxide catalyst comprising from 70 to 100% by weight of anatase and from 0 to 30% by weight of rutile and in which up to 40% by weight of the titanium dioxide may be replaced by tungsten oxide, the temperature and pressure being selected so as to obtain a first gas phase and a first liquid phase or a first solid phase or a mixture of first solid and first liquid phases and so that the first gas phase is separated from the first liquid phase or first solid phase or from the mixture of first liquid and first solid phases, and (3) admixing the first liquid or the first solid phase or the mixture of first liquid and first solid phases with a gaseous or liquid phase comprising water at from 150 to 370° C. and from 0.1 to 30×106 Pa, to obtain a product mixture.
    • 通过使至少一种氨基腈与水反应制备聚酰胺的连续方法包括:(1)在有机液体稀释剂存在下,在90至400℃和0.1至35×10 6时使至少一种氨基腈与水反应 在含有选自β-沸石催化剂,片状硅酸盐催化剂或二氧化钛催化剂的布朗斯台德酸催化剂的流动管中包含70至100重量%的锐钛矿和0至30重量%的金红石和 其中高达40重量%的二氧化钛可以被氧化钨代替,以获得反应混合物,(2)使反应混合物在150-400℃下进一步反应,并且压力低于压力 在选自β-沸石催化剂,片状硅酸盐催化剂或二氧化钛催化剂的布朗斯台德酸催化剂存在下,其包含70至100重量%的锐钛矿和0至30重量%的金红石,以及 其中高达40%的重量 二氧化钛可以被氧化钨代替,选择温度和压力以获得第一气相和第一液相或第一固相或第一固相和第一液相的混合物,使得第一气相 与第一液相或第一固相或第一液相和第一固相的混合物分离,和(3)将第一液体或第一固相或第一液相和第一固相的混合物与气体或 液相,其包含150至370℃和0.1至30×10 6 Pa的水,以获得产物混合物。
    • 6. 发明授权
    • Method for the continuous production of copolyamides based on a lactam (I), a diamine (II) and a dicarboxylic acid (III)
    • 基于内酰胺(I),二胺(II)和二羧酸(III)的共聚酰胺的连续生产方法,
    • US06703475B1
    • 2004-03-09
    • US10130044
    • 2002-05-13
    • Jürgen DeiningerWalter GötzAlfons LudwigGunter Pipper
    • Jürgen DeiningerWalter GötzAlfons LudwigGunter Pipper
    • C08G6904
    • C08G69/04C08G69/28C08G69/36C08G69/48D01F6/80
    • A process for continuous production of copolyamides based on a lactam (I), a diamine (II) and a dicarboxylic acid (III) comprises reacting a mixture (IV) comprising a diamine (II), a dicarboxylic acid (III) and water in a first reaction zone at a pressure in the range from 1.3*105 to 2.5*105 Pa in the entry zone of the reaction zone and at a temperature above the melting point of polymer (V) to a conversion, based on the molar amounts of diamine (II) and dicarboxylic acid (III), of at least 80% to form a polymer (V), reacting a mixture (VI) comprising lactam (I) and water in a second reaction zone at a pressure in the range from 5*105 to 40*105 Pa and at a temperature above the melting point of polymer (VII) to a conversion, based on the molar amount of lactam (I), of at least 80% to form a polymer (VII), then reacting polymer (V) and polymer (VII) with each other in a third reaction zone at a pressure in the range from 1*105 to 1.5*105 Pa in the entry zone of the reaction zone at temperatures above the melting point of polymer (VIII) to form a polymer (VIII), said polymer (VIII) having a 95° C. water extractables content, based on lactam (I), diamine (II) and dicarboxylic acid (III), of not more than 10% by weight, and then extracting the polymer (VIII) with water to obtain the copolyamide.
    • 基于内酰胺(I),二胺(II)和二羧酸(III)连续生产共聚酰胺的方法包括将包含二胺(II),二羧酸(III)和水的混合物(IV) 第一反应区,在反应区的进入区中在1.3×10 5至2.5×10 5 Pa范围内的压力下,在高于聚合物(V)熔点的温度下,以基于 使二胺(II)和二羧酸(III)的摩尔量为至少80%,以形成聚合物(V),使第二反应区中含有内酰胺(I)和水的混合物(VI)在压力 在5×10 5至40×10 5 Pa的范围内,并且在高于聚合物(VII)的熔点的温度下,基于内酰胺(I)的摩尔量,至少80 %以形成聚合物(VII),然后在第三反应区中将聚合物(V)和聚合物(VII)彼此反应,在1×10 5至1.5×10 5 Pa的压力范围内 反应区的进入区 e在高于聚合物(VIII)熔点的温度下形成聚合物(VIII),基于内酰胺(I),二胺(II)和二羧酸(II),所述聚合物(VIII)具有95℃的可水提取物含量 III),不大于10重量%,然后用水萃取聚合物(VIII),得到共聚酰胺。