Method of purifying tetrahydronaphthalene in coking crude benzene hydrogenation solution
A technology for coking crude benzene and tetralin, applied in the field of rectification and separation, can solve the problems of poor quality of tetralin, low content of tetralin, low purity of tetralin, etc., to reduce the difficulty of purification and increase the extraction rate , Improve the effect of difficult purification
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Embodiment 1
[0012] A method for purifying tetralin from coking crude benzene hydrogenation solution, specifically comprises the following steps:
[0013] A method for purifying tetralin from coking crude benzene hydrogenation solution, is characterized in that, specifically comprises the following steps:
[0014] Vacuum distillation: send the still liquid produced by coking crude benzene after hydrodesulfurization into the primary rectification tower, control the vacuum degree in the tower at 0.06MPa, the temperature of the tower bottom is 135°C, and the temperature of the tower top is 120°C, carry out vacuum distillation under the condition that the reflux ratio is 2:1, extract the light component products in the still liquid from the top of the tower, and obtain the crude tetralin from the bottom of the tower;
[0015] Esterification reaction: add tetralin crude product, pure benzene and acetic acid with a concentration of 99.5% to the reaction tank in a volume ratio of 1:0.9:0.13, ...
Embodiment 2
[0020] A method for purifying tetralin from coking crude benzene hydrogenation solution, specifically comprises the following steps:
[0021] Vacuum distillation: send the still liquid produced by coking crude benzene after hydrodesulfurization into the primary rectification tower, control the vacuum degree in the tower at 0.065MPa, the temperature of the tower bottom is 140°C, and the temperature of the top of the tower is 125°C, carry out vacuum distillation under the condition that the reflux ratio is 2:1, extract the light component products in the still liquid from the top of the tower, and get the crude tetralin from the bottom of the tower;
[0022] Esterification reaction: Add crude tetralin, pure benzene and acetic acid with a concentration of 99.5% to the reaction tank in a volume ratio of 1:1:0.14, and then add 2.2g of tetralin per 100mL of crude tetralin Add toluenesulfonic acid, add iron filings at a rate of 0.2 g per 100 mL of crude tetralin, and finally heat...
Embodiment 3
[0027] A method for purifying tetralin from coking crude benzene hydrogenation solution, is characterized in that, specifically comprises the following steps:
[0028] Vacuum distillation: send the still liquid produced by coking crude benzene after hydrodesulfurization into the primary rectification tower, control the vacuum degree in the tower at 0.07MPa, the temperature of the tower kettle is 145°C, and the temperature of the tower top is 130°C, carry out vacuum distillation under the condition that the reflux ratio is 2:1, extract the light component products in the still liquid from the top of the tower, and obtain crude tetralin from the bottom of the tower;
[0029] Esterification reaction: Add crude tetralin, pure benzene and acetic acid with a concentration of 99.5% to the reaction tank in a volume ratio of 1:1.1:0.15, and then add 2.3g of tetralin per 100mL of crude tetralin Add toluenesulfonic acid, add iron filings at a rate of 0.3g per 100mL of crude tetralin, ...
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