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    • 9. 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。
    • 10. 发明授权
    • Poly(meth)acrylamides
    • 聚(甲基)丙烯酰胺
    • US5374688A
    • 1994-12-20
    • US994634
    • 1992-12-21
    • Siegmund BeseckeAndreas DeckersWolfgang LothHarald Lauke
    • Siegmund BeseckeAndreas DeckersWolfgang LothHarald Lauke
    • C08F8/32C08F8/48
    • C08F8/32C08F8/48
    • A polymer comprising essentially units of formula I ##STR1## where R.sup.1 and R.sup.2 are each hydrogen or methyl, andR.sup.3 is C.sub.4 -C.sub.18 -alkyl, C.sub.5 -C.sub.8 -cycloalkyl, C.sub.6 -C.sub.10 -aryl or C.sub.6 -C.sub.10 -aryl-C.sub.1 -C.sub.4 -alkyl, each of which except for the C.sub.4 -C.sub.18 -alkyl may be monosubstituted, disubstituted or trisubstituted by radicals selected from the group consisting of C.sub.1 -C.sub.4 -alkyl, C.sub.1 -C.sub.4 -alkoxy and halogen, and having a carboxyl and anhydride group content of equal to or less than 0.40 equivalent per kilogram of polymer and an inherent color (measured as yellowness index) of equal to or less than 2.0, is obtainable by reacting a polymer based on C.sub.1 -C.sub.20 -alkyl esters of (meth)acrylic acid with a primary amine of the general formula IIR.sup.3 NH.sub.2 IIby removing the alcohol that forms during the reaction from the reaction mixture.
    • 包含基本上单元的式I的聚合物,其中R 1和R 2各自为氢或甲基,R 3为C 4 -C 18烷基,C 5 -C 8 - 环烷基,C 6 -C 10 - 芳基或C 6 -C 10 - 芳基-C 1 C 1-4 - 烷基,其中除C 4 -C 18 - 烷基之外的每一个可以被选自C 1 -C 4 - 烷基,C 1 -C 4 - 烷氧基和卤素的基团单取代,二取代或三取代,并具有羧基和 酸酐基含量等于或小于0.40当量/千克聚合物和固有颜色(黄色指数测定)等于或小于2.0可通过使基于(甲基)丙烯酸的C 1 -C 20烷基酯的聚合物 )丙烯酸与通式II R3NH2II的伯胺通过除去在反应期间形成的醇从反应混合物中。