Reaction system for continuously preparing polyoxymethylene dialkyl ether, and process thereof
A polymethoxydialkyl ether and reaction system technology, which is applied to chemical methods, chemical instruments and methods, ether preparation and other directions for reacting liquids with liquids, can solve problems such as low catalyst recovery rate, and achieve simple post-processing. , to achieve the effect of regeneration and recycling
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Embodiment 1
[0081] in the attached figure 1 In the shown reaction process, the volume of the reactor R1 is 1000mL, and the reactor R1 is connected to the heat exchanger in circulation, and the reaction liquid circulates between the reactor and the heat exchanger.
[0082] Purge with high-purity nitrogen to replace the system air. Add ionic liquid catalyst I in the flow reaction system, feed rate is 1.0g / h, until the catalyst starts to circulate, stop feeding, ensure that the catalyst concentration is not less than 4%; add the paraformaldehyde of purity 98.5wt%, purity 99% Methanol raw material reaction, the feeding rate is 15.0mL / h, 10.0mL / h respectively. The operating conditions of the reactor R1 are controlled at 115-120° C. and 2.5-3.5 MPa.
[0083] The reaction liquid is sent into the extraction tower V8, and the feed rate of the extractant benzene is 25mL / h. The heavy phase (catalyst aqueous solution) enters the film evaporator V12 continuously from the bottom of the tower, dehydr...
Embodiment 2
[0088] The basic process steps and equipment configuration are the same as in Example 1, except that the addition of ionic liquid II is a catalyst, and the feed rate is 0.6g / h. When the catalyst starts to circulate, the feed is stopped; the reaction raw material is 80wt% formaldehyde solution, purity 99% of the methanol raw material is reacted, the feed rates are 10.8mL / h and 5.8mL / h respectively, and the operating conditions of the reactor R1 are controlled at 125-130°C and 3.5-4.0MPa. The continuous acetalization reaction was carried out for 100 hours, and the results are listed in Table 2.
[0089] Table 2
[0090]
[0091] Note: Catalyst 13.3% is contained in the aqueous catalyst solution (14) after extraction.
Embodiment 3
[0093] The basic process steps, equipment configuration and parameters thereof are the same as those in Example 1, except that toluene is used as the extraction agent and the process is run continuously for 100 hours. 9.1mL / h DMM was obtained 3-8 Product (from line 21).
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