Production method for ultra-clean high-purity ethyl acetate
A technology of ethyl acetate and a production method, which is applied in the production field of ultra-clean and high-purity ethyl acetate, can solve the problems of high energy consumption in extraction and rectification, high production cost, difficulty in controlling the metal content of finished products, etc., and achieve simple process and low consumption. can low effect
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[0043] Example 1
[0044] This embodiment provides a continuous production method of ultra-clean and high-purity ethyl acetate. Industrial-grade ethyl acetate is sequentially carried out continuously according to the process of adsorbent pretreatment→membrane filtration→molecular sieve dehydration→ion exchange resin adsorption→circulation filtration. as follows:
[0045] (1) Adsorbent pretreatment: pump industrial-grade ethyl acetate into the adsorbent pretreatment tower at a constant flow rate of 300L / h. The ethyl acetate flows in from the bottom of the tower and flows out from the top of the tower. The adsorbent is diatomite and fine pores The mixture of silica gel, the volume ratio of diatomaceous earth and fine-pore silica gel is 1:2, and the filling amount of the adsorbent accounts for 70% of the volume of the adsorbent pretreatment tower;
[0046] (2) Membrane filtration: The pretreated ethyl acetate flows through the separation membrane at a constant flow rate, the mem...
Example Embodiment
[0051] Example 2
[0052] A kind of continuous production method of ultra-clean high-purity ethyl acetate, implementation method is basically the same as embodiment 1, difference is in:
[0053] The flow rate of the adsorbent pretreatment step is controlled at 200L / h, and the pressure of the membrane filtration step is maintained at 2-3.5bar.
Example Embodiment
[0054] Example 3
[0055] A kind of continuous production method of ultra-clean high-purity ethyl acetate, implementation method is basically the same as embodiment 1, difference is in:
[0056] The volume ratio of anion exchange resin to cation exchange resin is 1:3.
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