A system and method for continuous production of low molecular weight polyetheramine
A low molecular weight polyether, part of the technology, applied in chemical instruments and methods, chemical/physical processes, chemical/physical/physical chemical processes, etc., can solve the problems of many side reactions, large equipment investment, unsuitable catalysts, etc. achieve the effect of increasing the conversion rate
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Embodiment 1
[0060] The reaction is carried out by adopting 3 loop circulation reactors 6 which are continuously fed and connected in series with each other. The volume of the loop circulation reactor 6 is 3000L, and each loop circulation reactor 6 is filled with lightning which accounts for 1 / 3 of the volume of the loop circulation reactor 6. Nickel-nickel catalyst and Raney-nickel catalyst are fixed in the loop recycle reactor 6 .
[0061] When working, first open the first control valve 16 on the corresponding branch pipe 11 of the first-stage loop circulation reactor 6, and the second control valve between the discharge port of the polyether polyol tank 2 and the first-stage loop circulation reactor 6 17.
[0062] The polypropylene glycol ether (molecular weight of 230) in the polyether polyol tank 2 is preheated to 100-110 °C by the preheater 12 and mixed with the liquid ammonia and hydrogen mixture transported by the liquid ammonia and hydrogen transport pipeline 1, and then goes dow...
Embodiment 2
[0073] Three loop circulation reactors 6 with continuous feeding and connected in series are used for the reaction. The volume of the loop circulation reactor 6 is 3000L. Nickel-nickel catalyst and Raney-nickel catalyst are fixed in the loop recycle reactor 6 .
[0074] First open the first control valve 16 on the corresponding branch pipe 11 of the first-stage loop circulation reactor 6 and the second control valve 17 between the discharge port of the polyether polyol tank 2 and the first-stage loop circulation reactor 6 .
[0075]The trimethylolpropane polypropylene glycol ether (molecular weight 430) in the polyether polyol tank 2 is preheated to 100-110°C by the preheater 12 and mixed with the liquid ammonia and hydrogen mixture transported by the liquid ammonia and hydrogen transport pipeline 1, and then passed through the preheater 12. The injector 9 is continuously fed downward into the first-stage loop reactor 6 .
[0076] Among them, the feeding speed of trimethylolp...
Embodiment 3
[0086] The reaction is carried out by adopting 2 loop circulation reactors 6 which are continuously fed and connected in series with each other, the volume of the loop circulation reactor is 3000L, and each loop circulation reactor 6 is filled with Raney nickel catalyst accounting for 1 / 4 of the volume of the reactor, The Raney nickel catalyst was immobilized in the loop reactor 6 .
[0087] First open the first control valve 16 on the corresponding branch pipe 11 of the first-stage loop circulation reactor 6 and the second control valve 17 between the discharge port of the polyether polyol tank 2 and the first-stage loop circulation reactor 6 .
[0088] The polyethylene glycol and polypropylene glycol ether (molecular weight of 600) in the polyether polyol tank 2 is preheated to 100-110°C by the preheater 12 and mixed with the liquid ammonia and hydrogen mixture transported by the liquid ammonia and hydrogen transport pipeline 1, and then sprayed through the preheater 12. The...
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