A method for continuously preparing diacetyl using a reactive distillation tower
The technology of a reactive distillation column and a distillation column is applied in the field of flavor and fragrance production, and can solve the problems of difficulty in large-scale production, large environmental pollution of waste acid, expensive catalyst, etc., and achieve the effects of prolonging the service life and reducing the amount of production.
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Embodiment 1
[0081] Example 1: Continuous preparation of 2,3-butanedione using a reactive distillation column
[0082] This embodiment uses the attached figure 1 The described reactive distillation scheme was implemented.
[0083] The steps of this diacetyl preparation method are as follows:
[0084] A. The reaction of acetoin with ferric chloride
[0085] Under normal pressure, acetoin is added dropwise in the reaction section (1) of rectifying tower still by the first feeding tank (5), simultaneously adds ferric chloride by ferric chloride feed port (8), and acetoin The molar ratio to ferric chloride is 1:0.14;
[0086] Under the agitation of stirring speed 80pm, this reaction mixture is heated to temperature 124 ℃ and carries out reactive rectification, and the temperature of tower top condenser (3) is controlled at 40 ℃ simultaneously, when forming total reflux in the whole rectifying column, reflux The ratio R1 is controlled at 10:1;
[0087] B. Add hydrogen peroxide drop by drop...
Embodiment 2
[0095] Example 2: Continuous preparation of 2,3-butanedione using a reactive distillation column
[0096] This embodiment uses the attached figure 1 The described reactive distillation scheme was implemented.
[0097] The steps of this diacetyl preparation method are as follows:
[0098] A. The reaction of acetoin with ferric chloride
[0099] Under normal pressure, acetoin is added dropwise in the reaction section (1) of rectifying tower still by the first feeding tank (5), simultaneously adds ferric chloride by ferric chloride feed port (8), and acetoin The molar ratio to ferric chloride is 1:0.18;
[0100] Under the agitation of stirring speed 80pm, this reaction mixture is heated to temperature 130 ℃ and carries out reactive rectification, and the temperature of tower top condenser (3) is controlled at 50 ℃ simultaneously, when forming total reflux in the whole rectifying column, reflux The ratio R1 is controlled at 6:1;
[0101] B. Add hydrogen peroxide drop by drop ...
Embodiment 3
[0109] Example 3: Continuous preparation of 2,3-butanedione using a reactive distillation column
[0110] This embodiment uses the attached figure 1 The described reactive distillation scheme was implemented.
[0111] The steps of this diacetyl preparation method are as follows:
[0112] A. The reaction of acetoin with ferric chloride
[0113] Under normal pressure, acetoin is added dropwise in the reaction section (1) of rectifying tower still by the first feeding tank (5), simultaneously adds ferric chloride by ferric chloride feed port (8), and acetoin The molar ratio to ferric chloride is 1:0.10;
[0114] Under the agitation of stirring speed 150pm, this reaction mixture is heated to temperature 100 ℃ and carries out reactive rectification, and the temperature of tower top condenser (3) is controlled at 60 ℃ simultaneously, when forming total reflux in the whole rectifying column, reflux The ratio R1 is controlled at 2:1;
[0115] B. Add hydrogen peroxide drop by drop...
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Abstract
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