A fluidized bed reaction process for preparing amino-terminated polyether
A technology of amino-terminated polyether and fluidized bed reaction, which is applied in the chemical industry and can solve problems such as low conversion rate
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Embodiment 1
[0024] Use 10~20 mesh r-Al 2 o 3 Microspheres are used as a carrier to prepare a supported catalyst, in which the nickel content is 30%, the copper content is 10%, the catalyst loading volume is 50ml, and the liquid ammonia space velocity is 0.5h -1 , The reaction temperature is 230°C, and the results of synthesizing amino-terminated polyethers with different molecular weights are shown in Table 1.
[0025] Table 1 Example 1 reaction result
[0026]
Embodiment 2
[0028] Use 20~40 mesh r-Al 2 o 3 Microspheres are used as a carrier to prepare a supported catalyst, in which the nickel content is 40%, the copper content is 5%, the iron content is 3%, the catalyst loading volume is 50ml, and the liquid ammonia space velocity is 1.0h -1 , The reaction temperature is 250°C, and the results of synthesizing amino-terminated polyethers with different molecular weights are shown in Table 2.
[0029] Table 2 Example 2 reaction results
[0030]
Embodiment 3
[0032] Use 80~100 mesh r-Al 2 o 3 Microspheres are used as a carrier to prepare a supported catalyst, in which the nickel content is 35%, the copper content is 8%, the iron content is 5%, the catalyst loading volume is 50ml, and the liquid ammonia space velocity is 0.8h -1 , The reaction temperature is 245°C, and the results of synthesizing amino-terminated polyethers with different molecular weights are shown in Table 3.
[0033] Table 3 Example 3 reaction results
[0034]
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