A method and device for separating various phenols from medium and low temperature coal tar crude phenols
A technology of low-temperature coal tar and crude phenol, which is applied in the field of coal chemical industry, can solve problems such as inability to separate, and achieve the effect of improving the separation effect
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Embodiment 1
[0031] The crude phenol refining method of medium and low temperature coal tar crude phenol provided in this example is as follows: the crude phenol raw material obtained from medium and low temperature coal tar includes the following components: 9.71wt% of water, 3.18wt% of pyridine compounds, 17.60wt% of phenol, ortho Cresol 12.39wt%, m-p-cresol 31.86wt%, xylenol 15.91wt%, tricresol 0.30wt%, phenol residue, high boiling point phenol and tar 9.05%. According to the medium and low temperature coal tar crude phenol refining method provided by the present invention, the above-mentioned crude phenol raw material is sent to the dehydration tower 1, the operating pressure at the top of the tower is 30KPa, the operating pressure at the bottom of the tower is 55KPa, the temperature at the top of the tower is 60°C, and the temperature at the bottom of the tower is Under the conditions of 140°C, a reflux ratio of 2, and a plate number of 65, the top of the dehydration tower 1 is separat...
Embodiment 2
[0033]The crude phenol refining method of medium and low temperature coal tar crude phenol provided in this example is as follows: the crude phenol raw material obtained from medium and low temperature coal tar includes the following components: water 12.31wt%, pyridine compounds 2.70wt%, phenol 18.30wt%, ortho Cresol 10.29wt%, m-p-cresol 34.48wt%, xylenol 12.64wt%, tricresol 0.16wt%, phenol residue, high boiling point phenol and tar 9.12%. According to the medium and low temperature coal tar crude phenol refining method provided by the present invention, the above-mentioned crude phenol raw material is sent to the dehydration tower 1, the operating pressure at the top of the tower is 40KPa, the operating pressure at the bottom of the tower is 64kPa, the temperature at the top of the tower is 71 ° C, and the temperature at the bottom of the tower is Under the conditions of 145°C, a reflux ratio of 3, and a plate number of 65, the top of the dehydration tower 1 is separated to o...
Embodiment 3
[0035] The crude phenol refining method of medium and low temperature coal tar crude phenol provided in this example is as follows: the crude phenol raw material obtained from medium and low temperature coal tar includes the following components: 9.71wt% of water, 3.18wt% of pyridine compounds, 17.60wt% of phenol, ortho Cresol 12.39wt%, m-p-cresol 31.86wt%, xylenol 15.91wt%, tricresol 0.30wt%, phenol residue, high boiling point phenol and tar 9.05%. According to the medium and low temperature coal tar crude phenol refining method provided by the present invention, the above-mentioned crude phenol raw material is sent to the dehydration tower 1, the operating pressure at the top of the tower is 30KPa, the operating pressure at the bottom of the tower is 55KPa, the temperature at the top of the tower is 60°C, and the temperature at the bottom of the tower is Under the conditions of 140°C, a reflux ratio of 2, and a plate number of 65, the top of the dehydration tower 1 is separat...
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