A method and device for extracting 2,6-xylenol from crude phenol
A technology of xylenol and crude phenol, which is applied in the field of coal chemical industry and can solve problems such as poor selectivity
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Embodiment 1
[0037] This embodiment provides a method for extracting 2,6-xylenol from crude phenol, comprising the steps of:
[0038] 1) Select the crude phenol raw material, which contains light components such as 0.18wt% phenol, 5.03wt% 2,6-xylenol, 66.51wt% m-p-cresol and 28.28wt% other dicresols in this crude phenolic raw material heavy components such as cresol, and preheat the crude phenol raw material to 155°C;
[0039] 2) The crude phenol raw material preheated in step 1) is continuously sent into the first-stage rectification column with a flow rate of 2.5t / h to carry out the first-stage rectification treatment, and the operating pressure of the first-order rectification treatment is controlled at 25KPa, and the operating temperature is The temperature is 130°C, the reflux ratio is 14, and the light components lighter than 2,6-xylenol are removed, and drawn from the top of the primary distillation tower, and the primary distillation product is collected from the bottom of the towe...
Embodiment 2
[0042] This embodiment provides a method for extracting 2,6-xylenol from crude phenol, comprising the steps of:
[0043]1) Select the crude phenol raw material, which contains light components such as 0.22wt% phenol, 2.07wt% 2,6-xylenol, 66.56wt% m-p-cresol and 31.15wt% other dicresols in this crude phenolic raw material heavy components such as cresol, and preheat the crude phenol raw material to 154°C;
[0044] 2) The crude phenol raw material preheated in step 1) is continuously sent into the first-stage rectification column with a flow rate of 2.5t / h to carry out the first-stage rectification treatment, and the operating pressure of the first-order rectification treatment is controlled to 0.5Pa. The temperature is 160°C, the reflux ratio is 5, and the light components lighter than 2,6-xylenol are removed, and drawn from the top of the first-stage rectification tower, and the first-stage rectification product is collected from the bottom of the tower, and the first-stage re...
Embodiment 3
[0047] This embodiment provides a method for extracting 2,6-xylenol from crude phenol, comprising the steps of:
[0048] 1) Select the crude phenol raw material, which contains light components such as 0.05wt% phenol, 15wt% 2,6-xylenol, 60wt% m-p-cresol and 24.5wt% other xylenols in this crude phenolic raw material Equal weight components, and preheat the crude phenol raw material to 153°C;
[0049] 2) The crude phenol raw material preheated in step 1) is continuously sent into the first-stage rectification column with a flow rate of 2.5t / h to carry out the first-stage rectification treatment, and the operating pressure of the first-order rectification treatment is controlled at 50KPa, and the operating temperature is The temperature is 100°C, the reflux ratio is 20, and the light components lighter than 2,6-xylenol are removed, and drawn from the top of the primary distillation tower, and the primary distillation product is collected from the bottom of the tower, and the prim...
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Abstract
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