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    • 24. 发明授权
    • Method for producing polyether polyols
    • 聚醚多元醇的制备方法
    • US09120894B2
    • 2015-09-01
    • US14131977
    • 2012-07-17
    • Thomas Ernst MüllerChristoph GürtlerMatthias WohakJörg HofmannMuhammad Afzal SubhaniMaurice CosemansWalter Leitner
    • Thomas Ernst MüllerChristoph GürtlerMatthias WohakJörg HofmannMuhammad Afzal SubhaniMaurice CosemansWalter Leitner
    • C08G85/00C08G65/00C08G65/26C08G64/34
    • C08G65/2663C08G64/34C08G65/2603
    • The present invention relates to a process for the preparation of polyether carbonate polyols from one or more H-functional starter compounds, one or more alkylene oxides and carbon dioxide in the presence of a double metal cyanide catalyst, wherein (α) the H-functional starter substance or a mixture of at least two H-functional starter substances is initially introduced into the reaction vessel, (β) for the activation, a part amount (based on the total amount of the amount of alkylene oxides employed in steps (β) and (γ)) of one or more alkylene oxides is added to the mixture resulting from step (α), it also being possible for step (β) to be carried out several times for the activation, (γ) one or more alkylene oxides and carbon dioxide are metered continuously into the mixture resulting from step (β) (“copolymerization”), the alkylene oxides employed for the copolymerization being identical to or different from the alkylene oxides employed in step (β), characterized in that in step (γ) the carbon dioxide is passed into the mixture by (i) gassing the reaction mixture in the reactor from the bottom, (ii) using a hollow shaft stirrer, (iii) a combination of the metering operations according to (i) and (ii), and/or (iv) gassing over the surface of the liquid by using stirrer units configured in several stages.
    • 本发明涉及在双金属氰化物催化剂存在下由一种或多种H官能起始化合物,一种或多种环氧烷和二氧化碳制备聚醚碳酸酯多元醇的方法,其中(α)H官能团 起始物质或至少两种H功能性起始物质的混合物最初被引入反应容器((bgr))中用于活化,部分量(基于步骤(bgr)中使用的环氧烷烃的总量 (γ))和(γ))加入到由步骤(α)得到的混合物中,对于活化,(γ)一个或多个步骤(&bgr)可以进行几次, 更多的环氧烷和二氧化碳被连续地计量到由步骤((bgr))(“共聚”)得到的混合物中,用于共聚的烯化氧与步骤(bgr)中使用的环氧烷烃相同或不同, 其特征在于在步骤(γ)中,二氧化碳通过以下步骤进入混合物:(i)从底部将反应混合物放入反应器中,(ii)使用中空轴搅拌器,(iii)根据 至(i)和(ii),和/或(iv)通过使用在几个阶段中配置的搅拌器单元在液体的表面上放气。
    • 26. 发明授权
    • Polymer derivative of cytidine metabolic antagonist
    • 胞苷代谢拮抗剂的聚合物衍生物
    • US09018323B2
    • 2015-04-28
    • US13884413
    • 2011-11-16
    • Keiichirou YamamotoManami OkazakiDai Kawamura
    • Keiichirou YamamotoManami OkazakiDai Kawamura
    • C08G81/00A61K31/513C07D407/04C08G69/40C08G69/48A61K31/77A61K31/785A61K47/48C08G85/00
    • C08G81/00A61K31/513A61K31/77A61K31/785A61K47/60A61K47/645C07D407/04C08G69/40C08G69/48
    • [Problem]To provide a novel polymer derivative of a cytidine metabolic antagonist which allows release of a medicament irrespective of enzymes of the living body and is expected to have high therapeutic effects. [Solution]The polymer derivative of a cytidine metabolic antagonist in which a substituent represented by the general formula (I) or the general formula (II) [wherein R7 and R8 each independently represent a hydrogen atom or an optionally substituted (C1-C6)alkyl group, R6 represents a hydrogen atom, an optionally substituted (C1-C40)alkyl group, an optionally substituted (C1-C40)aralkyl group, an optionally substituted aromatic group, an amino acid residue in which the carboxy group is protected, or an optionally substituted sugar residue, CX—CY represents CH—CH or C═C (double bond), and A represents the residue of the cytidine metabolic antagonist except the amino group at the position 4] is bonded to the side-chain carboxy group of a block copolymer of a polyethylene-glycol structural moiety and a polymer having 10 or more carboxy groups.
    • [问题]提供一种胞苷代谢拮抗剂的新型聚合物衍生物,其允许不管生物体的酶释放药物并且预期具有高治疗效果。 [溶液]通式(I)或通式(II)表示的取代基的胞苷代谢拮抗剂的聚合物衍生物[其中,R7和R8各自独立地表示氢原子或可以具有取代基的(C1-C6) 烷基,R 6表示氢原子,任选取代的(C 1 -C 40)烷基,任选取代的(C 1 -C 40)芳烷基,任选取代的芳族基团,其中羧基被保护的氨基酸残基,或 任选取代的糖残基,CX-CY表示CH-CH或C = C(双键),A表示胞苷代谢拮抗剂的残基,除了位置4]上的氨基键合到侧链羧基 的聚乙二醇结构部分和具有10个或更多个羧基的聚合物的嵌段共聚物。
    • 29. 发明申请
    • CURABLE RESIN COMPOSITION AND SHORT-CURE METHOD
    • 可固化树脂组合物和短效方法
    • US20130225788A1
    • 2013-08-29
    • US13776754
    • 2013-02-26
    • CYTEC TECHNOLOGY CORP.
    • Jonathan E. MEEGAN
    • C08G65/22C08G85/00D06M17/04
    • C08K7/06B29C70/48B29K2063/00B29K2105/0809C08G59/00C08G59/38C08G59/50C08G59/5026C08G59/504C08G59/56C08G65/22C08G85/00C08J3/243C08J3/244C08J2363/00C08L63/00D06M17/04Y10T428/24994Y10T428/31511
    • Disclosed herein is a method for utilizing the exothermic energy generated by a low temperature cure reaction to access a high-temperature cure reaction, which is otherwise energetically inaccessible at a chosen tool temperature, thereby producing a cured resin matrix with properties closely matching to those produced via high-temperature cure reactions but achieved via a short cure time and low cure temperature. Also disclosed is a short-cure resin composition containing: (a) at least one multifunctional epoxy resin having an epoxy functionality of greater than 1; (b) a hardener composition containing (i) at least one aliphatic or cycloaliphatic amine curing agent having one or more amino groups per molecule; (ii) at least one aromatic amine curing agent having one or more amino groups per molecule; and optionally, (iii) an imidazole as curing accelerator. The improved properties of this resin composition include being curable at a temperature of ≦120° C. for a time period of less than 10 minutes to achieve a degree of cure higher than that derived from the same composition with just (i) aliphatic/cycloaliphatic amine or (ii) aromatic amine in isolation.
    • 本文公开了一种利用由低温固化反应产生的放热能进行高温固化反应的方法,否则在所选择的工具温度下能够达到高能量固化反应,从而产生固化的树脂基质,其特性与所生产的 通过高温固化反应,但通过短的固化时间和低固化温度实现。 还公开了一种短固化树脂组合物,其包含:(a)至少一种环氧官能度大于1的多官能环氧树脂; (b)一种硬化剂组合物,其包含(i)至少一种每分子具有一个或多个氨基的脂族或脂环族胺固化剂; (ii)每分子具有一个或多个氨基的至少一种芳族胺固化剂; 和(iii)咪唑作为固化促进剂。 该树脂组合物的改进的性质包括在120℃的温度下可固化的时间小于10分钟,以达到比来自相同组成的固化程度高于(i)脂肪族/脂环族 胺或(ii)芳族胺。
    • 30. 发明授权
    • Gas-phase polymerization of alpha-olefin
    • α-烯烃的气相聚合
    • US08058368B1
    • 2011-11-15
    • US13090973
    • 2011-04-20
    • Sung Woo KangNam Kyu KimYoung Jae JunMan Jung KimKil Su Kim
    • Sung Woo KangNam Kyu KimYoung Jae JunMan Jung KimKil Su Kim
    • C08F2/00C08F210/00C08G85/00B01J8/18
    • B01J8/44B01J8/1827B01J8/1854B01J8/1863B01J2208/00274B01J2208/0092B01J2208/00929C08F210/16C08F2/34C08F210/14C08F2500/07C08F2500/18C08F2500/08
    • A method for preparing polyolefin from alpha-olefin with high productivity using an internal circulating fluidized bed polymerization reactor is disclosed. The method for gas-phase polymerization of alpha-olefin comprising the steps of: supplying circulation gas including one or more alpha-olefins and inert gas into a polymerization reactor; polymerizing the alpha-olefin to polyolefin in two separated polymerization areas in the polymerization reactor; and discharging produced polyolefin from the polymerization reactor. The polymerization reactor is divided into the two polymerization areas by a draft tube, and an inside of the draft tube forms a riser where growing polyolefin polymers move up in fast fluidization, and an outside of the draft tube forms an annulus where the polyolefin polymers passing the riser move down by gravity, and the polyolefin polymers passing the annulus are introduced to a lower part of the riser again, so that the polyolefin polymers are polymerized during circulating between the riser and the annulus.
    • 公开了一种使用内部循环流化床聚合反应器以高生产率从α-烯烃制备聚烯烃的方法。 包括以下步骤的α-烯烃气相聚合方法:将包括一种或多种α-烯烃和惰性气体的循环气体供应到聚合反应器中; 在聚合反应器中的两个分离的聚合区域中将α-烯烃聚合成聚烯烃; 并从聚合反应器中排出生产的聚烯烃。 聚合反应器通过引流管分成两个聚合区域,引流管的内部形成提升管,其中生长的聚烯烃聚合物在快速流化中向上移动,并且引流管的外部形成环状物,其中聚烯烃聚合物通过 立管通过重力向下移动,并且通过环的聚烯烃聚合物再次被引入提升管的下部,使得聚烯烃聚合物在提升管和环之间循环期间聚合。