Method for preparing polyoxymethylene dimethyl ether
A technology of polyoxymethylene dimethyl ether and paraformaldehyde, which is applied in chemical instruments and methods, preparation of organic compounds, sustainable manufacturing/processing, etc., can solve the problem of low selectivity and achieve improved conversion rate and selectivity, Overcome uncontrollable, responsive effects
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Embodiment 1
[0014] according to figure 1 As shown, the operating pressure of the catalytic distillation tower is 0.5 MPa, the number of theoretical plates in the stripping section is 20, the separation efficiency of the catalytic reaction section is equivalent to 25 theoretical plates, the catalyst is SAPO-34 molecular sieve, and the flow rate of paraformaldehyde is 2 g / min Enter the first theoretical plate (counting from top to bottom, the same below), methylal enters from the bottom of the catalytic reaction section with a flow rate of 1 g / min, the top of the tower is fully refluxed, and the ratio of the first part of the tower kettle to the second part of the material is 3:1, the temperature range of the catalytic reaction section under effective reaction conditions is 100-120 ° C, and the flow rate of 3 g / min is extracted at the bottom of the tower. 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, and the catalyst is Su Qing 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 , Catalytic distillation results are shown in Table 1.
Embodiment 6
[0018] according to figure 1 As shown, the operating pressure of the catalytic distillation tower is 4.0 MPa, the number of theoretical plates in the stripping section is 5, the separation efficiency of the catalytic reaction section is equivalent to 5 theoretical plates, the catalyst is MCM-22 molecular sieve, and the flow rate of paraformaldehyde is 1 g / min and methylal enter the first theoretical plate at a flow rate of 10 g / min, total reflux at the top of the tower, the ratio of the first part of the tower to the second part of the material is 10:1, and the temperature range of the catalytic reaction section under effective reaction conditions is 180 ~ At 200°C, the bottom of the tower was withdrawn at a flow rate of 11 g / min. The catalytic distillation results are shown in Table 1.
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