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    • 9. 发明授权
    • Diaminobenzoate catalytic chain extenders
    • 二氨基苯甲酸酯催化增链剂
    • US4908394A
    • 1990-03-13
    • US267217
    • 1988-11-04
    • Jeremiah P. CaseySusan M. Clift
    • Jeremiah P. CaseySusan M. Clift
    • C08G18/18C08G18/32
    • C08G18/325C08G18/1825
    • The present invention relates to a process for the production of polyurethanes wherein a tertiary amine functionality is incorporated into the side chain of a diaminobenzoate to form catalytic polyurethane chain extender. These chain extenders are polyurethane catalysts which provide adequate cure without residual odor and safety hazards associated with the more traditional tertiary amine catalysts. When reacted with the isocyanate reactive group the non-tertiary amine portion of the chain extender is bound to the polymeric network thereby preventing diffusion of the catalyst species from the polyurethane and negating odor and toxicity as problems. The diaminobenzoate provides enhanced polyurethane physical properties.
    • 本发明涉及生产聚氨酯的方法,其中叔胺官能团被引入到二氨基苯甲酸酯的侧链中以形成催化聚氨酯增链剂。 这些增链剂是提供足够固化而不具有与更传统的叔胺催化剂相关的残留气味和安全危害的聚氨酯催化剂。 当与异氰酸酯反应性基团反应时,扩链剂的非叔胺部分结合到聚合物网络,从而防止催化剂物质从聚氨酯扩散,并且作为问题消除气味和毒性。 二氨基苯甲酸酯提供增强的聚氨酯物理性能。
    • 10. 发明授权
    • Removal of BOD and nitrogenous pollutants from wastewaters
    • 从废水中去除BOD和含氮污染物
    • US3994802A
    • 1976-11-30
    • US568712
    • 1975-04-16
    • Jeremiah P. CaseyMarshall L. Spector
    • Jeremiah P. CaseyMarshall L. Spector
    • C02F3/12C02F3/26C02F3/28C02F3/30C02F3/34C12N1/20C02C1/06
    • C02F3/302C02F3/12C02F3/26C02F3/28C02F3/301Y02W10/15Y10S210/903
    • A multistage treatment is disclosed for the removal of carbonaceous BOD and nitrogenous pollutants from wastewaters, wherein the influent wastewater undergoes successive nitrification-denitrification in the presence of recycled activated sludge containing a mixed culture biomass comprising heterotrophic and autotrophic organisms. The initial mixing of the wastewater with recycled sludge is effected in the presence of sufficient oxygen to maintain oxic conditions. The mixed liquor from the initial oxic treatment, without intermediate separation of solids, is passed to an anoxic stage wherein nitrites and nitrates (NO.sub.x .sup.-, x = 2,3) formed by oxidation of ammonium compounds are reduced to nitrogen gas. Any number of oxic treating stages each followed by an anoxic stage may be employed. The final treating stage prior to solids separation from the mixed liquor may be either oxic or anoxic. The separated solids constitute the activated sludge recycled to at least the initial mixing stage. A short residence time, resulting in a high food to biomass ratio, is maintained in the initial oxic stage or the first subsection thereof, in order to avoid sludge bulking and to promote an active dense biomass.
    • 公开了用于从废水中去除碳质BOD和含氮污染物的多级处理,其中在含有包含异养和自养生物体的混合培养生物质的再循环活性污泥的存在下,进水废水经历连续的硝化 - 脱氮。 废水与循环污泥的初始混合是在有足够氧气的情况下进行的,以保持氧气条件。 来自初始氧化处理的混合液体,没有固体的中间分离,被传递到缺氧阶段,其中通过铵化合物的氧化形成的亚硝酸盐和硝酸盐(NO x - ,x = 2,3)被还原成氮气。 可以使用任何数量的氧治疗阶段,每个后续是缺氧阶段。 固体分离混合液之前的最后处理阶段可以是含氧还是缺氧。 分离的固体构成再循环至至少初始混合阶段的活性污泥。 为了避免污泥膨胀和促进活性致密的生物质,在最初的氧化阶段或其第一阶段中保持了较高的食物与生物质比例的停留时间。