会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 3. 发明申请
    • Method for the Production of Double Metal Cyanide Complex Catalysts
    • 双金属氰化物复合催化剂生产方法
    • US20080292526A1
    • 2008-11-27
    • US11913484
    • 2006-05-02
    • Edward BohresMichael StosserLudwig VolkelRaimund RuppelEva BaumNorbert WagnerJorg SundermeyerUdo GarreltsMichael Zirnstein
    • Edward BohresMichael StosserLudwig VolkelRaimund RuppelEva BaumNorbert WagnerJorg SundermeyerUdo GarreltsMichael Zirnstein
    • C01C3/14C01C3/20C01B21/20C01G1/04
    • B01J27/26B01J31/1805B01J31/20B01J2231/48C08G65/2663
    • Process for preparing double metal cyanide catalysts of the general formula (I) M2a[M1(CN)rXt]b   (I) where M2 is preferably Co(III) or Fe(III), and M1 is preferably Zn(II), X is a group other than cyanide which forms a coordinate bond to M1 and is selected from the group consisting of carbonyl, cyanate, isocyanate, nitrile, thiocyanate and nitrosyl, a, b, r, t are integers which are selected so that the compound is electrically neutral, by reacting a) a cyanometallic acid of the general formula (II) Hw[M1(CN)r(X)t] where M1 and X are as defined above, r and t are as defined above and w is selected so that the compound is electrically neutral, with b) a readily protolyzable metal compound (IIIa) M2Rw and/or (IIIb) M2RuYv, where M2 is as defined above, the groups R are identical or different and are each the anion of a very weak protic acid having a pKa of ≧20, and Y is the anion of an inorganic mineral acid or a moderately strong to strong organic acid having a pKa of from −10 to +10, w corresponds to the valence of M2, u+v corresponds to the valence of M2, with u and v each being at least 1, with the reaction being carried out in a nonaqueous, aprotic solvent.
    • 制备通式(I)的双金属氰化物催化剂的方法<?in-line-formula description =“In-line formula”end =“lead”→> M2a [M1(CN)rXt] b(I) 其中M2优选为Co(III)或Fe(III),M1优选为Zn(II),X为氰化物以外的基团 其形成与M1的配位键,并且选自羰基,氰酸酯,异氰酸酯,腈,硫氰酸酯和亚硝酰基,a,b,r,t是选择为使化合物电中性的整数,通过使 )通式(II)的卤代金属盐Hw [M1(CN)r(X)t]其中M1和X如上定义,r和t如上所定义,并且w被选择为使得化合物是电中性的 ,其中b)易于分解的金属化合物(IIIa)M2Rw和/或(IIIb)M2RuYv,其中M2如上所定义,基团R相同或不同,各自为非常弱的质子酸的阴离子,其具有pKa为 > = 20,和 Y是无机无机酸的阴离子或pKa为-10至+10的中等强至强有机酸的阴离子,w对应于M2的化合价,u + v对应于M2的化合价,u和v 每个至少为1,反应在非水性非质子溶剂中进行。
    • 7. 发明申请
    • Dmc catalysts, polyether alcohols, and method for the production thereof
    • Dmc催化剂,聚醚醇及其制备方法
    • US20050203274A1
    • 2005-09-15
    • US10514714
    • 2003-06-18
    • Edward BohresDirk FrankeMichael StosserRaimund RuppelEva BaumKathrin Harre
    • Edward BohresDirk FrankeMichael StosserRaimund RuppelEva BaumKathrin Harre
    • C08G65/12B01J27/26B01J37/03C08G18/48C08G65/26C08G65/04
    • B01J27/26B01J37/03C08G18/4866C08G65/2663
    • The invention relates to a process for preparing polyether alcohols by addition of alkylene oxides onto H-functional starter substances using multimetal cyanide compounds as catalysts, wherein the multimetal cyanide compound is prepared by a process comprising the steps: a) adding a metal salt solution to a cyanometalate solution at a specific stirring power ε in the range from 0.05 to 10 W/l, preferably from 0.4 to 4 W/l, a temperature in the range from 0° C. to 100° C., preferably from 20° C. to 60° C., and an addition time of from 5 to 120 minutes, b) reducing the specific stirring power ε to a value in the range from 0.03 to 0.8 W/l and at the same time adding a surface-active agent, c) heating the solution while stirring at a specific stirring power ε of from 0.03 to 0.8 W/l, to a temperature of not more than 100° C., preferably in the range from 55° C. to 75° C., d) adding further metal salt solution while stirring at a specific stirring power ε of from 0.03 to 0.8 W/l, e) when the conductivity begins to drop, dispersing the solid, for example by stirring while increasing the specific stirring power ε to >0.7 W/l or by installation of a pumped circuit with an appropriate pump or by means of a high-speed stirrer, f) stirring at the specific stirring power ε of step e) until the conductivity or the pH remains constant, g) separating off the multimetal cyanide compound and washing it with water and, if desired, h) drying the catalyst.
    • 本发明涉及通过使用多金属氰化物作为催化剂将烯化氧加成到H官能起始物质上制备聚醚醇的方法,其中所述多金属氰化合物通过包括以下步骤的方法制备:a)将金属盐溶液加入到 在特定搅拌功率ε为0.05至10W / l,优选0.4至4W / l的范围内的氰酸金属盐溶液,温度范围为0℃至100℃,优选为20℃ 至60℃,加入时间为5至120分钟,b)将比重搅拌功率ε3降低至0.03-0.8W / l的范围内,同时加入表面活性剂 ,c)在0.03-0.8W / l的特定搅拌功率ε的搅拌下将溶液加热至不超过100℃,优选在55℃至75℃的温度, d)在搅拌下以特定搅拌功率ε加入另外的金属盐溶液 从0.03至0.8W / l,e)当电导率开始下降时,例如通过搅拌分散固体,同时将特定搅拌功率ε提高至> 0.7W / l或通过用合适的泵安装泵浦回路或 通过高速搅拌器,f)在步骤e)的特定搅拌功率ε下搅拌,直到导电率或pH保持恒定,g)分离多金属氰化合物并用水洗涤,如果需要,h )干燥催化剂。
    • 10. 发明申请
    • Preparation of polyether alcohols
    • 聚醚醇的制备
    • US20050107643A1
    • 2005-05-19
    • US10712707
    • 2003-11-13
    • Thomas OstrowskiRaimund RuppelEva BaumKathrin Harre
    • Thomas OstrowskiRaimund RuppelEva BaumKathrin Harre
    • C07C43/11C08G65/00C08G65/10C08G65/12C08G65/26
    • C08G65/2663C08G18/4866C08G65/2696
    • The invention relates to a process for the continuous preparation of polyether alcohols by reaction of alkylene oxides with H-functional starter substances in the presence of DMC catalysts, which comprises, at the beginning of the process a) firstly placing initial charge material and DMC catalyst in a reactor, b) metering in alkylene oxide so that the metering rate which is maintained for continuous operation of the reactor is reached in a time of from 100 to 3 000 seconds, c) metering in starter substance during or after step b) so that the metering rate which is maintained for continuous operation of the reactor is reached in a time of from 5 to 500 seconds, d) after the fill level in the reactor which is desired for continuous operation of the reactor has been reached, taking product off continuously from the reactor while at the same time metering in starter substance and alkylene oxides in such an amount that the fill level in the reactor remains constant and metering in DMC catalyst so that the catalyst concentration necessary for continuous operation of the reactor is maintained in the reactor.
    • 本发明涉及一种通过在DMC催化剂存在下使烯化氧与H官能起始物质反应来连续制备聚醚醇的方法,该方法在方法开始时包括:a)首先将初始的电荷材料和DMC催化剂 在反应器中,b)在环氧烷中计量,使得在100至3000秒的时间内达到维持反应器连续操作的计量速率,c)在步骤b)或之后计量起始物质 在5至500秒的时间内达到维持反应器连续运行的计量速率,d)在达到反应器连续运行所需反应器的填充量后,将产品关闭 连续地从反应器中同时在起始物质和环氧烷中计量,使得反应器中的填充水平保持恒定并且在DMC cata中计量 使得在反应器中保持连续操作反应器所需的催化剂浓度。