Refined crude benzene and method for extracting thiophene
A technology of crude benzene and thiophene, which is applied in extraction and purification/separation, treatment of hydrocarbon oil, organic chemistry, etc., can solve the problems of lower production material and process requirements, lower reaction pressure and temperature, and reduce the difficulty of making reactors. Reduced material and process requirements, reduced reaction pressure and temperature, and reduced production difficulty
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Embodiment 1
[0016] Send a certain amount of crude benzene into the two-benzene tower and then send it into steam to start the temperature-raising distillation, (the theoretical plate number of the two-benzene tower is not less than 45, the pressure is controlled at -30Kpa--40KPa, the temperature at the top of the tower is controlled at 120°C, the tower The temperature of the kettle is controlled at >190°C, and the reflux ratio is 0.2-0.3.) The part with a distillation range greater than 210°C is used as a heavy benzene product and sent to storage equipment for storage; the part with a distillation range less than 210°C is sent to the next step as light benzene Grade equipment evaporator. Send light benzene into the evaporator and heat it to 100°C to change into gas phase, then send it into the first-stage hydrogenation reactor, the hydrogen purity in the hydrogenation reactor is kept above 90%, and at the same time add the catalyst NI-MO, the molar ratio of the amount of hydrogen is : NI-...
Embodiment 2
[0018]Send a certain amount of crude benzene into the two-benzene tower and then send it into steam to start the temperature-raising distillation, (the theoretical plate number of the two-benzene tower is not less than 45, the pressure is controlled at -30Kpa--40KPa, the temperature at the top of the tower is controlled at 120°C, the tower The temperature of the kettle is controlled at >190°C, and the reflux ratio is 0.2-0.3.) The part with a distillation range greater than 210°C is used as a heavy benzene product and sent to storage equipment for storage; the part with a distillation range less than 210°C is sent to the next step as light benzene Grade equipment evaporator. Send light benzene into the evaporator and heat it to 110°C to change into gas phase, then send it into the first-stage hydrogenation reactor, the hydrogen purity in the hydrogenation reactor is kept above 90%, and at the same time add the catalyst NI-MO, the molar ratio of the amount of hydrogen is : NI-M...
Embodiment 3
[0020] Send a certain amount of crude benzene into the two-benzene tower and then send it into steam to start the temperature-raising distillation, (the theoretical plate number of the two-benzene tower is not less than 45, the pressure is controlled at -30Kpa--40KPa, the temperature at the top of the tower is controlled at 120°C, the tower The temperature of the kettle is controlled at >190°C, and the reflux ratio is 0.2-0.3.) The part with a distillation range greater than 210°C is used as a heavy benzene product and sent to storage equipment for storage; the part with a distillation range less than 210°C is sent to the next step as light benzene Grade equipment evaporator. Send light benzene into the evaporator and heat it to 120°C to change into gas phase, then send it to the first-stage hydrogenation reactor, the hydrogen purity in the hydrogenation reactor is kept above 90%, and at the same time add the catalyst NI-MO, the molar ratio of the amount of hydrogen is : NI-MO...
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