Preparation method for polyoxymethylene dimethyl ether
A polyoxymethylene dimethyl ether and trioxymethylene technology, which is applied in the preparation of organic compounds, chemical instruments and methods, sustainable manufacturing/processing, etc., can solve the problems of low conversion rate and selectivity of polyoxymethylene dimethyl ether, etc., Achieve the effect of overcoming difficult control, promoting reaction, improving conversion rate and selectivity
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Embodiment 1
[0014] press figure 1 As shown, the operating pressure of the catalytic distillation column is 0.5 MPa, in which the number of theoretical plates in the rectification section is 15, and the number of theoretical plates in the stripping section is 15. The separation efficiency of the upper reaction section is equivalent to the theoretical plate number of 15, and the separation efficiency of the upper reaction section is equivalent to The number of theoretical plates is 15, the catalyst is SAPO-34 molecular sieve, the raw material (the mass ratio of methylal to trioxane is 1:2) enters from between the two reaction sections at a flow rate of 3 g / min, and the reflux ratio is 4, which is effective The temperature range of the catalytic reaction section of the reaction conditions is 100-130°C, and the bottom of the tower is extracted at a flow rate of 3 g / min. The catalytic distillation results are shown in Table 1.
Embodiment 2~5
[0016] Other conditions are the same as in Example 1, except that the type of catalyst is changed. The catalysts are Suqing brand 001×4 strong acid resin, ZSM-5, SO 4 -2 / Fe 2 O 3 , Cl -1 / TiO 2 And SO 4 -2 / Fe 2 O 3 , The catalytic distillation results are shown in Table 1.
Embodiment 6
[0018] press figure 1 As shown, the operating pressure of the catalytic distillation column is 4.0 MPa, in which the number of theoretical plates in the rectification section is 5, the number of theoretical plates in the stripping section is 5, the separation efficiency of the upper reaction section is equivalent to the theoretical plate number of 5, and the separation efficiency of the upper reaction section is equivalent to The number of theoretical plates is 5, the catalyst is MCM-22 molecular sieve, and the raw materials (the mass ratio of methylal to trioxane is 10:1) enter from between the two reaction sections at a flow rate of 11 g / min. The reflux ratio is 10, which is effective The temperature range of the catalytic reaction section of the reaction conditions is 160-200°C, and the bottom of the tower is extracted at a flow rate of 11 g / min. The catalytic distillation results are shown in Table 1.
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