Method for producing isobutyl acetate
A technology of isobutyl acetate and production method, which is applied in the preparation of carboxylate, chemical instruments and methods, preparation of organic compounds, etc., can solve the problems of high labor intensity, difficult process control, large amount of waste water, etc. Short, easy to operate, less side effects
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Embodiment 1
[0022] Embodiment 1, a kind of production method of isobutyl acetate, the production device of the used isobutyl acetate mainly comprises esterification reactor, rectifying tower and phase separator.
[0023] The esterification reaction kettle is a stainless steel reaction tube, the ratio of its inner diameter to the total height: 1:1.3~2 (for example, inner diameter Φ=200mm, height 300mm). The steam source communicates with the esterification reactor through a pipeline with a valve (ie, a steam valve).
[0024] The acetic acid raw material tank for storing acetic acid and the isobutanol raw material tank for storing isobutanol are respectively communicated with the esterification reaction kettle after passing through respective flow meter regulating valves.
[0025] The above two flow meter regulating valves and steam valves can be connected with the signal of the DCS control system to realize automatic control.
[0026] Add composite catalyst 4.5g from the top position of e...
Embodiment 2
[0032] Embodiment 2, a kind of production method of isobutyl acetate, the production device of the used isobutyl acetate is with the production device of embodiment 1;
[0033] In advance, add 500ml of isobutanol and acetic acid to the esterification reaction kettle according to the acid-alcohol mass ratio of 2:1, and then add acid sulfate and p-toluenesulfonic acid to mix according to the molar ratio of 1:1.5. 5.9g of the composite catalyst, that is, the composite catalyst accounts for 1.25% of the total weight of the bottom material of the raw material. Acid sulfate is selected BaHSO 4 .
[0034] Through DCS control, perform the following operations on the console: control the opening of the steam valve to control the temperature rise and reaction pressure of the esterification reactor. When the temperature in the esterification reactor rises to 60-80°C, the acetic acid and Butanol flow meter regulating valve, adjust the feed opening (control feed flow,) control the flow o...
Embodiment 3
[0040] Embodiment 3, a kind of production method of isobutyl acetate, the production device of the used isobutyl acetate is with the production device of embodiment 1;
[0041] Add 500ml of isobutanol mixed with acetic acid in the esterification reactor in advance at an acid-alcohol mass ratio of 2:1, add acid sulfate and p-toluenesulfonic acid (molar ratio 1:1) and mix to form The obtained composite catalyst was 4.75g, that is, the composite catalyst accounted for 1.0% of the total weight of the raw material base. Acid sulfate choose CaHSO 4 .
[0042] All the other are with embodiment 1.
[0043] The yield was 98.9%.
[0044] The purity of the finally obtained isobutyl acetate is 99.0%, moisture %: 0.1%, acidity %: 0.01%; above-mentioned % is mass percentage.
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