Method for preparing thiophene through variable pressure azeotropic distillation
A technology of azeotropic distillation and thiophene, applied in the direction of organic chemistry, can solve the problems of difficult to obtain high-purity products, complicated process technology, harsh operating conditions, etc., and achieve the effects of unclear amplification effect, simple process flow, and avoiding subsequent treatment
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Embodiment 1
[0028] The lower content of thiophene and cyclohexane extracted from the coking crude benzene enters the first distillation column at a mass ratio of 65:35, the pressure is controlled at 0.08Mpa, the temperature at the top of the column is 65°C, and the temperature at the bottom of the column is 80°C. The first azeotrope containing thiophene and cyclohexane is extracted from the top, and under this condition, the azeotrope ratio of the extracted thiophene and cyclohexane is 68:32, and the high boiler is extracted from the bottom of the column.
[0029] The first azeotrope of thiophene and cyclohexane of 68:32 is entered into the second distillation column, the control pressure is 0.4MPa, the control column top temperature is 100°C, the column bottom temperature is 130°C, and the extraction pressure from the column top is 0.4MPa It contains the second azeotrope of thiophene and cyclohexane, the azeotrope ratio of thiophene and cyclohexane is 58:42, the second azeotrope is re-ent...
Embodiment 2
[0031] The lower content of thiophene and cyclohexane extracted from the coking crude benzene enters the first distillation column at a mass ratio of 63:37, the pressure is controlled at 0.1 Mpa, the temperature at the top of the column is 70 °C, and the temperature at the bottom of the column is 85 °C. The first azeotrope containing thiophene and cyclohexane is extracted from the top, and under this condition, the azeotrope ratio of the extracted thiophene and cyclohexane is 67:33, and the high boiler is extracted from the bottom of the tower;
[0032] The first azeotrope of thiophene and cyclohexane of 67:33 is entered into the second distillation column, the control pressure is 0.45MPa, the control column top temperature is 105°C, the column bottom temperature is 135°C, and the extraction pressure from the column top is 0.45MPa When the second azeotrope of thiophene and cyclohexane is included, the azeotrope ratio of thiophene and cyclohexane is 57:43, the second azeotrope i...
Embodiment 3
[0034] The lower content of thiophene and cyclohexane extracted from the coking crude benzene enters the first distillation column at a mass ratio of 60:40, the pressure is controlled at 0.12Mpa, the temperature at the top of the column is 75°C, and the temperature at the bottom of the column is 90°C. The first azeotrope containing thiophene and cyclohexane is extracted at the top, and under this condition, the azeotrope ratio of the extracted thiophene and cyclohexane is 65:35, and the high boiler is extracted at the bottom of the tower;
[0035] The first azeotrope of thiophene and cyclohexane of 65:35 was entered into the second distillation column, the control pressure was 0.5MPa, the temperature at the top of the column was controlled at 110°C, and the temperature at the bottom of the column was 140°C, and the extraction pressure from the top of the column was 0.5MPa. When the second azeotrope of thiophene and cyclohexane, the azeotrope ratio of thiophene and cyclohexane i...
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Abstract
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