Purifying method for 1,2-epoxybutane
A technology of butylene oxide and butyraldehyde, which is applied in the field of purifying 1,2-butylene oxide, and can solve problems such as product loss
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Embodiment 1
[0028] The crude 1,2-epoxybutane solution 1 containing 1,2-epoxybutane and water, butyraldehyde, propionaldehyde, methanol, and acetone impurities enters the middle and lower part of the weight removal tower 100, and the extractant dimethyl sulfoxide is extracted from The upper part of the light removal tower enters, and after separation by extraction and rectification, a stream 4 containing water, butyraldehyde and methanol is obtained in the tower reactor, and a stream 3 at the top of the tower goes to the light removal tower 200 .
[0029] The still liquid 4 of the weight-removing tower enters the extractant recovery tower 400 to recover the extractant dimethyl sulfoxide, and circulates to the weight-removing tower 100 as the extractant.
[0030] The overhead stream 3 of the de-lightening tower enters the middle and lower part of the light-removing tower 200, and isooctane enters from a position close to the top of the de-lightening tower. - stream 5 of butylene oxide.
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Embodiment 2
[0041]The composition of crude 1,2-butylene oxide solution 1: 94% of 1,2-butylene oxide, 3% of water, and the rest are impurities of butyraldehyde, propionaldehyde, methanol, acetone and methyl formate.
[0042] The embodiment is the same as [Example 1], except that the extractant B is a mixture of n-octane and isooctane.
[0043] The theoretical plate number of the weight removal tower is 50, the operating temperature is 85°C, the operating pressure is 180kPa, and the reflux ratio is 1.5.
[0044] The solvent ratio (mass ratio of extractant dimethyl sulfoxide to crude 1,2-epoxybutane feed flow) of the weight-removing tower is 5:1.
[0045] The theoretical plate number of the extraction agent recovery tower is 50, the operating pressure is 200kPa, the operating temperature is 90°C, and the reflux ratio is 12.
[0046] The theoretical plate number of the light removal tower is 50, the operating temperature is 75°C, the operating pressure is 180kPa, and the reflux ratio is 10. ...
Embodiment 3
[0051] The composition of crude 1,2-butylene oxide solution 1: 96% of 1,2-butylene oxide, 2% of water, and the rest are impurities of butyraldehyde, propionaldehyde, methanol, acetone and methyl formate.
[0052] The embodiment is the same as [Example 1], except that the extractant B is 2-methylheptane.
[0053] The theoretical plate number of the weight removal tower is 35, the operating temperature is 73°C, the operating pressure is 140kPa, and the reflux ratio is 3.
[0054] The solvent ratio (mass ratio of extractant A to crude 1,2-butylene oxide feed flow) of the weight-removing tower is 4:1.
[0055] The theoretical plate number of the extraction agent recovery tower is 35, the operating pressure is 150kPa, the operating temperature is 64°C, and the reflux ratio is 15.
[0056] The theoretical plate number of the light removal tower is 35, the operating temperature is 74°C, the operating pressure is 140kPa, and the reflux ratio is 25.
[0057] The solvent ratio of the ...
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