Apparatus for reducing arene extraction solvent sulfolane, and application thereof
A technology for the extraction and application of aromatics, which is applied in the direction of organic chemistry, can solve the problems of low operating cost, unresolved defects, degraded sulfolane energy consumption and high power consumption, so as to improve economic benefits, strong anti-organic pollution ability, eliminate The effect of safety hazards
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Embodiment 1
[0033] The volumetric space velocity of sulfolane entering the resin tower is controlled by a flow meter to be 1.5h -1 , adjust the flow of cooling water in the cooler, and control the temperature of the poor sulfolane solvent entering the resin tower to 60°C. The sulfolane poor solvent entering the resin exchange tower pH4.3, Cl - Content 5.9mg / kg. Sampling the sulfolane poor solvent flowing out of the resin tower, analyzing Cl - Content, pH value, the results are shown in Table 2.
Embodiment 2
[0035] The volume space velocity of sulfolane entering the resin tower is controlled by a flow meter to be 9.0h -1 , adjust the flow of cooling water in the cooler, and control the temperature of the poor sulfolane solvent entering the resin tower to 55°C. The sulfolane poor solvent entering the resin exchange tower pH4.3, Cl - content of 5.9mg / kg, the sulfolane poor solvent flowing out of the resin tower is sampled, and the Cl -- Content, pH value, the results are shown in Table 2.
Embodiment 3
[0037] The volumetric space velocity of sulfolane entering the resin tower is controlled by a flow meter to be 4.5h -1 , adjust the flow of cooling water in the cooler, and control the temperature of the poor sulfolane solvent entering the resin tower to 50°C. The sulfolane poor solvent entering the resin exchange tower pH4.3, Cl - Content 5.9mg / kg. Sampling the sulfolane poor solvent flowing out of the resin tower, and analyzing its Cl - Content, pH value, the results are shown in Table 2.
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