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    • 71. 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。
    • 76. 发明授权
    • Double-flow regenerator
    • 双流再生器
    • US3963072A
    • 1976-06-15
    • US526007
    • 1974-11-21
    • Norbert Wagner
    • Norbert Wagner
    • F28D7/00F28D17/00F28F9/02F28D7/10
    • F28F9/02F28D17/00Y10S165/429Y10S62/909
    • A double-flow regenerator has several separate groups of tubes each of which is used for a respective fluid heat-exchange medium. These tubes are all received in a packed housing through which fluids to be treated are passed in heat-exchange relationship with the packing in the housing through the tubes in contact with this packing. Each group of tubes terminates within the housing at each end of a plurality of separate manifold connectors. Thus the middle of the housing is provided with a plurality of manifolds for the inner end of each tubing group and the outer end is provided with a plurality of such manifolds for each group, with several such manifold connectors provided for each group for minimum variation in tube lengths within the group.
    • 双流再生器具有几组单独的管,各自用于相应的流体热交换介质。 这些管都被接收在一个包装的外壳中,待处理流体通过与包装接触的管与壳体中的包装物进行热交换关系。 每组管在多个分开的歧管连接器的每个端部处在壳体内终止。 因此,壳体的中间设置有用于每个管组的内端的多个歧管,并且外端为每组设置有多个这样的歧管,其中为每个组提供了几个这样的歧管连接器,用于最小的变化 管长度在组内。