N-butanol separation and purification device and separation and purification method using the device
A technology of n-butanol and static separation, applied in the field of chemical rectification, can solve the problems of low separation purity of n-butanol, difficult separation of n-butanol mixed solution, etc. low effect
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Embodiment 1
[0021] like figure 1 As shown, the n-butanol separation and purification device includes a primary chromatography 1, a dehydration tower 2, a secondary chromatography 3, a rectification tower 4 and a n-butanol storage tank 5 connected in sequence.
[0022] like figure 1 As shown, the primary chromatography 1 and the secondary chromatography 3 are provided with an overflow plate, and the overflow plate separates the primary chromatography 1 and the secondary chromatography 3 into a light phase area and a heavy phase area; and in light phase area, heavy phase area and rectifying column 4, are all provided with the liquid level controller that is used to measure separation liquid discharge in light phase area and heavy phase area; and static separation in the secondary chromatography device 3.
[0023] like figure 1 As shown, the first-level chromatography 1 heavy phase area and the second-level chromatography 3 heavy-phase area are all connected with the dehydration tower 2; ...
Embodiment 2
[0031] Adopt the method for above-mentioned device separation and purification n-butanol, comprise the following steps:
[0032] (1) Add the mixed solution of n-butanol 7%, water 80% and formaldehyde 13% in the primary chromatograph, stand and separate at 80°C for 0.5h, and the components in the light phase region of the primary chromatograph are used as The raw material returns to the synthesis system; the components in the heavy phase area enter the dehydration tower and continue to be separated;
[0033] (2) Separation under the conditions that the temperature at the top of the dehydration tower is 100°C, the temperature at the bottom of the dehydration tower is 100°C, the reflux ratio is 2, and the pressure is 0.2mPa. The formaldehyde component is obtained at the bottom of the dehydration tower, of which n-butanol The content is controlled at about 100ppm, and the formaldehyde component is stored in the formaldehyde storage tank; the mixed component of n-butanol, water and...
Embodiment 3
[0036] Adopt the method for above-mentioned device separation and purification n-butanol, comprise the following steps:
[0037] (1) Add the mixed solution of 10% n-butanol, 82% water and 8% formaldehyde into the primary chromatograph, stand and separate at 80°C for 0.5h, and the components in the light phase region of the primary chromatograph are used as The raw material returns to the synthesis system; the components in the heavy phase area enter the dehydration tower and continue to be separated;
[0038] (2) Separation under the conditions that the temperature at the top of the dehydration tower is 85°C, the temperature of the bottom of the dehydration tower is 110°C, the reflux ratio is 2, and the pressure is 0.2mPa. The formaldehyde component is obtained at the bottom of the dehydration tower, of which n-butanol The content is controlled at about 100ppm, and the formaldehyde component is stored in the formaldehyde storage tank; the mixed component of n-butanol, water an...
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