Method for producing isopropanolamine and 1, 2-propane diamine by cracking 2, 5-dimethyl piperazine
A technology of dimethylpiperazine and isopropanolamine, which is applied in chemical instruments and methods, preparation of amino compounds, preparation of organic compounds, etc., can solve problems such as unusable, easy to control parameters, simple cracking process, and easy The effect of industrialization promotion
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Embodiment 1
[0044] The method for producing isopropanolamine and 1,2-propylenediamine by cracking 2,5-dimethylpiperazine described in Example 1 consists of the following steps:
[0045] (1) Pass 2,5-dimethylpiperazine into the vaporizer of the reaction system, and after heating and vaporizing the mixed gas of ammonia and water, mix with Co-Ni-Pd / Al in the reactor 2 o 3 Catalyst carries out contact cracking reaction;
[0046] (2) After condensing the reaction product obtained in step (1), enter the distillation separation system to obtain pure isopropanolamine and 1,2-propanediamine.
[0047] in:
[0048] The Co-Ni-Pd / Al 2 o 3 As for the catalyst, based on the weight of the metal oxide, CoO is 2% by weight of the catalyst, NiO is 2% by weight of the catalyst, and PdO is 4% by weight of the catalyst.
[0049] The Co-Ni-Pd / Al 2 o 3 The pore volume is 0.5ml / g, and the specific surface area is 290m 2 / g.
[0050] The temperature of the mixed gas of ammonia and water described in step (1...
Embodiment 2
[0073] The method for producing isopropanolamine and 1,2-propylenediamine by cracking 2,5-dimethylpiperazine described in Example 2 consists of the following steps:
[0074] (1) Pass 2,5-dimethylpiperazine into the vaporizer of the reaction system, and after heating and vaporizing the mixed gas of ammonia and water, mix with Co-Ni-Pd / Al in the reactor 2 o 3 Catalyst carries out contact cracking reaction;
[0075] (2) After condensing the reaction product obtained in step (1), enter the distillation separation system to obtain pure isopropanolamine and 1,2-propanediamine.
[0076] in:
[0077] The Co-Ni-Pd / Al 2 o 3 As for the catalyst, according to the weight of the metal oxide, CoO is 1% of the weight of the catalyst, NiO is 1% of the weight of the catalyst, and PdO is 3% of the weight of the catalyst.
[0078] The Co-Ni-Pd / Al 2 o 3 The pore volume is 0.6ml / g, and the specific surface area is 320m 2 / g.
[0079] The temperature of the mixed gas of ammonia and water de...
Embodiment 3
[0102] The method for producing isopropanolamine and 1,2-propylenediamine by cracking 2,5-dimethylpiperazine described in Example 3 consists of the following steps:
[0103] (1) Pass 2,5-dimethylpiperazine into the vaporizer of the reaction system, and after heating and vaporizing the mixed gas of ammonia and water, mix with Co-Ni-Pd / Al in the reactor 2 o 3 Catalyst carries out contact cracking reaction;
[0104] (2) After condensing the reaction product obtained in step (1), enter the distillation separation system to obtain pure isopropanolamine and 1,2-propanediamine.
[0105] in:
[0106] The Co-Ni-Pd / Al 2 o 3 As for the catalyst, based on the weight of the metal oxide, CoO is 3% by weight of the catalyst, NiO is 3% by weight of the catalyst, and PdO is 4% by weight of the catalyst.
[0107] The Co-Ni-Pd / Al 2 o 3 The pore volume is 0.4ml / g, and the specific surface area is 250m 2 / g.
[0108] The temperature of the mixed gas of ammonia and water described in step ...
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