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    • 2. 发明申请
    • Child seat
    • 儿童座椅
    • US20060163923A1
    • 2006-07-27
    • US10532759
    • 2003-10-02
    • Karl-Heinz BaumannMichael FehringPeter HornRainer Justen
    • Karl-Heinz BaumannMichael FehringPeter HornRainer Justen
    • A47D1/10
    • B60N2/2812B60N2/2806B60N2/286B60N2/2884B60N2/2887B60R22/1951
    • The invention relates to a child seat (1) which can be fastened to a vehicle seat of a motor vehicle by means of a three-point seat belt (14). It is also possible for the child seat also to be connected to the supporting structure of the vehicle via an ISOFIX fastening system (17). The three-point seat belt (14) is equipped with a tightening device. The child seat (1) has its own belt system for securing a child sitting on the child seat. According to the invention, it is proposed that the three-point seat belt (14) be coupled to the belt system of the child seat (1). This coupling makes it possible, during a preventative or crash-active tightening of the three-point seat belt (14), for the belt system of the child seat (1) also to be tightened without a separate tightening device being necessary.
    • 本发明涉及一种可通过三点式安全带(14)固定在机动车辆的车辆座椅上的儿童座椅(1)。 儿童座椅还可以经由ISOFIX紧固系统(17)连接到车辆的支撑结构。 三点式安全带(14)配有紧固装置。 儿童座椅(1)具有自己的皮带系统,用于固定坐在儿童座椅上的儿童。 根据本发明,提出三点式安全带(14)与儿童座椅(1)的皮带系统联接。 这种联接使得在三点式安全带(14)的预防或紧急主动紧固期间,也可以在不需要单独的紧固装置的情况下使儿童座椅(1)的皮带系统被紧固。
    • 7. 发明授权
    • Process for the preparation of optionally cellular polyurethane polyurea
molded parts
    • 制备任选细胞聚氨酯聚脲模制件的方法
    • US4595705A
    • 1986-06-17
    • US700758
    • 1985-02-13
    • Frank WernerMatthias MarxPeter HornHans U. Schmidt
    • Frank WernerMatthias MarxPeter HornHans U. Schmidt
    • C08G18/32C08G18/40C08G18/65C08G18/14C08G18/30
    • C08G18/6529C08G18/3221C08G18/4009C08G18/4018C08G2101/0033C08G2120/00Y10T428/249989
    • The invention relates to a one-shot process for the preparation of cellular or noncellular polyurethane polyurea parts having a modulus of flexural elasticity greater than 600 N/mm.sup.2 and densities of from 0.8 to 1.2 g/cm.sup.3 using the reaction injection molding technique, by reacting organic polyisocyanates, a polyol component, aromatic diamines, additional chain extenders and/or cross-linking agents in the presence of catalysts and optionally blowing agents, auxiliaries and/or additives, wherein the polyol component is a mixture containing(i) from 95 to 60 percent by weight of at least one compound selected from the group consisting of polyols, polyether polyamines, polyesteramides, and their mixtures having functionalities of from 2 to 6 and a molecular weight of from 1000 to 8000 and(ii) from 5 to 40 percent by weight of a least one aromatic and/or aromatic-aliphatic polyester polyol having a functionality of from 2 to 3 and a molecular weight of from 254 to 700, wherein the percents by weight are based on the total weight of the polyol component.
    • 本发明涉及使用反应注射成型技术制备具有大于600N / mm2的弯曲弹性模量和0.8至1.2g / cm 3的密度的细胞或非细胞聚氨酯聚脲部件的一步法,通过使 有机多异氰酸酯,多元醇组分,芳族二胺,另外的增链剂和/或交联剂,在催化剂和任选的发泡剂,助剂和/或添加剂的存在下,其中多元醇组分是含有(i)95至 60重量%的至少一种选自多元醇,聚醚多胺,聚酯酰胺及其混合物的至少一种化合物,其官能度为2至6,分子量为1000至8000,(ii)5至40% 的至少一种官能度为2至3且分子量为254至700的至少一种芳族和/或芳族 - 脂族聚酯多元醇,其中百分比 基于多元醇组分的总重量。
    • 10. 发明授权
    • Continuous production of polycarbonates
    • 连续生产聚碳酸酯
    • US3945969A
    • 1976-03-23
    • US438753
    • 1974-02-01
    • Peter HornHeribert Kuerten
    • Peter HornHeribert Kuerten
    • C08G63/00C08G64/20C08G64/22C08G63/62
    • C08G64/205
    • High molecular weight linear polycarbonates are prepared by continuous condensation of organic dihydroxy compounds and phosgene in two reaction zones, a mixture of an aqueous-alkaline solution of the organic dihydroxy compound and an aqueous catalyst solution being introduced at the rate of from 1 to 50 meters per second and the phosgene at the rate of from 30 to 300 meters per second into the first reaction zone and condensed, an organic solvent being incorporated into the resultant reaction mixture containing oligomer and polycarbonate and the condensation of the aqueous-organic reaction mixture carried to completion in the second reaction zone by the two-phase interfacial method.
    • 通过有机二羟基化合物和光气在两个反应区中连续缩合制备高分子量线性聚碳酸酯,将有机二羟基化合物的碱性水溶液与以1至50米的速率引入的水性催化剂溶液的混合物 每秒30至300米的光气进入第一反应区并冷凝,将有机溶剂加入到所得到的含有低聚物和聚碳酸酯的反应混合物中,并将所携带的水 - 有机反应混合物冷凝至 通过两相界面方法在第二反应区完成。