Method for extracting and separating cresol from phenol-containing oil by using imidazolium-based ionic liquid
An ionic liquid, imidazole-based technology, applied in the field of chemical separation, can solve the problems of organic extractant polluting the environment, unfavorable to environmental protection, high cost of separation process, and achieve the effects of large-scale industrial production, reasonable equipment and improved purity.
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Embodiment 1
[0034] The phenol-containing oil raw material obtained from coal tar comprises the following components: 60wt% n-hexane, 10wt% toluene, 10wt% p-cresol, 10wt% o-cresol, and 10wt% m-cresol. The mass ratio of phenolic oil to extraction solvent was 10:1, and the ionic liquid extraction agent was [EMIM][SCN]. The operating temperature of the liquid-liquid extraction tower is 25°C, the pressure is 1 atm, and the number of theoretical plates is 4. The phenolic oil is fed at the bottom of the tower, and the extractant is fed at the top of the tower. The vacuum rectification column has 35 theoretical plates, feeds in the middle section of the rectification column, the column pressure is 20kpa, and the reflux ratio is 1.0. 99.16wt% of the cresol product was extracted from the top of the tower, and the extraction efficiency was 92.36%. 99.56wt% ionic liquid is extracted from the bottom of the tower, and the recovery rate is 98.50%. The ionic liquid is circulated back to the liquid-liqui...
Embodiment 2
[0036] The phenol-containing oil raw material obtained from coal tar comprises the following components: 60wt% n-hexane, 10wt% toluene, 10wt% p-cresol, 10wt% o-cresol, and 10wt% m-cresol. The mass ratio of phenolic oil to extraction solvent is 5:1, and the ionic liquid extraction agent is [EMIM][CH 3 SO 4 ]. The operating temperature of the liquid-liquid extraction tower is 30°C, the pressure is 1 atm, and the number of theoretical plates is 8. The phenolic oil is fed at the bottom of the tower, and the circulating extractant is fed at the top of the tower. The vacuum rectification column has 50 theoretical plates, feeds in the middle section of the rectification column, the column pressure is 20kpa, and the reflux ratio is 3.0. 99.34wt% cresol product was extracted from the top of the tower, and the extraction efficiency was 98.80%. 99.62wt% ionic liquid is extracted from the bottom of the tower, and the recovery rate is 99.50%. The ionic liquid is circulated back to the l...
Embodiment 3
[0038] The phenol-containing oil raw material obtained from coal tar comprises the following components: 60wt% n-hexane, 10wt% toluene, 10wt% p-cresol, 10wt% o-cresol, and 10wt% m-cresol. The mass ratio of phenolic oil to extraction solvent is 5:1, and the ionic liquid extraction agent is [EMIM][DMP]. The operating temperature of the liquid-liquid extraction tower is 35°C, the pressure is 1 atm, and the number of theoretical plates is 12. The phenolic oil is fed at the bottom of the tower, and the circulating extractant is fed at the top of the tower. The vacuum rectification column has 60 theoretical plates, feeds in the middle section of the rectification column, the column pressure is 20kpa, and the reflux ratio is 3.0. 98.15wt% cresol product was extracted from the top of the tower, and the extraction efficiency was 96.25%. 99.56wt% ionic liquid is extracted from the bottom of the tower, and the recovery rate is 99.32%. The ionic liquid is circulated back to the liquid-li...
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