Complex catalyst contg. two or more than two kinds of bimetal cyanide, prepn. method and application thereof
A double metal cyanide and catalyst technology, applied in the production of polyether polyols, the field of complex catalysts containing two or more double metal cyanides, can solve the problem of poor storage stability, uneconomical, expensive, etc. problem, to achieve the effect of wide applicable temperature range and high product activity
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[0015] Take USP5158922 (Arco Company) as the dividing line, represented by it and L in the previous DMC cat 1 It is basically Glyme (dimethoxyethane) or Diglyme (diethylene glycol dimethyl ether), which are characterized by high cat crystalline content, >35%, and low activity, known as traditional DMC cat. USP5470813 (Arco company) finds that two kinds of salt solutions are strongly mixed by homogenizer etc., destroys the crystallization condition of catalyst, makes organic complexing agent with TBA, makes amorphous state cat, (crystalline state DMC compound 35wt%) obtained by simple stirring, the activity is 65% greater at the same 100ppm (relative to the final product, hereinafter the same), and the activity is 200% greater at 130-250ppm. Example: Polyoxypropylene Triol (M n =700) 685g as initiator, cat250ppm, reaction temperature 105°C, induction time 85min, maximum reaction rate (reaction pressure maintained 2 The amount makes xn =700) 70g as initiator, cat100ppm, reaction...
Embodiment 1
[0044] The specific embodiment embodiment 1 system {Zn 3 [Co(CN) 6 ] 2 +0.06Ni 3 [Co(CN) 6 ] 2 +0.06Fe[Co(CN) 6 ]}·ZnCl 2 0.5H 2 O 0.15TBA 0.015P 0.092A In a batching kettle, put 22kg ZnCl 3 Dissolve in 50L TBA / 90L deionized water, in another batching kettle, 5.5kg K 3 [Co(CN) 6 ] was dissolved in 50L TBA / 90L deionized water, and the two solutions were added to the reactor within 30 minutes, and mixed at a high speed circulation (660L / min), and 0.33Kg Ni was added after the circulation was continued for 1.5 hours 3 [Co(CN) 6 ] 2 and 0.15Kg Fe[Co(CN) 6 ] into the built-in separation membrane pipeline, wash with 300L of 50% TBA solution (0.5% concentration A), and then replace part of the water in the slurry with 200L pure TBA for 3 hours after 5 hours, continue membrane separation, and concentrate to the slurry 300L. Add 0.6kg polyoxypropylene trihydric alcohol (Mn=3000) and 1.8kg A, circulate for 2 hours, press or suck the slurry into a filter press, press filter...
Embodiment 4
[0049] Operation is the same as embodiment 1, but in a batching still, with 21kg ZnCl 2 , 1.8kg FeCl 3 , 1.2kgNiSO 4 Dissolve in 50LTBA / 90L deionized water, in another batching kettle, 5.9kg K 3 [Co(CN)] 6 Dissolve in 50L TBA / 90L deionized water. Get cat〔V〕8.4kg
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