Process for preparing high temperature heat transfer oil base oil by using C10 heavy aromatic residual oil
A technology of heavy aromatics and heat transfer oil, which is applied in the petroleum industry, hydrocarbon distillation, etc., can solve the problems of waste of resources, low prices, and unfavorable corporate benefits, and achieve the effect of increasing corporate benefits and improving utilization rates
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Embodiment 1
[0021] Will C 10 8,000 tons of heavy aromatic raw materials are introduced into the first rectification tower T101 with a diameter of 1.6m, a tower height of 35m, and a number of trays of 130 via pipeline 1 for rectification. The temperature at the top of the tower is controlled at 120°C, and the absolute pressure at the top of the tower is 25KPa , the reflux ratio is 1: 12, the temperature at the bottom of the tower is controlled at 150°C, 1000# aromatic hydrocarbon solvent is extracted from the top of the T101 tower through pipeline 2, the durene enriched liquid is extracted through the side line pipeline 3, and the distillate at the bottom of the tower is introduced through pipeline 4 The diameter is 1.2m, the height of the tower is 28m, and the number of trays is 118 in the second rectification tower T102 to continue rectification, the temperature of the control tower top is 120 ℃, the absolute pressure of the tower top is 25KPa, and the reflux ratio is 1: 12. The temperat...
Embodiment 2
[0023] Will C 107,800 tons of heavy aromatic raw materials are introduced into the first rectification tower T101 with a diameter of 1.6m, a tower height of 35m, and a number of trays of 130 through pipeline 1 for rectification. The temperature at the top of the tower is controlled at 130°C and the absolute pressure at the top of the tower is 20KPa , the reflux ratio is 1:9, the temperature at the bottom of the tower is controlled at 170°C, 1000# aromatic hydrocarbon solvent is extracted from the top of the T101 tower through pipeline 2, the durene enriched liquid is extracted from the side line pipeline 3, and the distillate at the bottom of the tower is introduced through pipeline 4 The diameter is 1.2m, the height of the tower is 28m, and the number of trays is 118 in the second rectifying tower T102 to continue rectification, the control tower top temperature is 130 ℃, the absolute pressure of the tower top is 18KPa, and the reflux ratio is 1: 9, The temperature at the bot...
Embodiment 3
[0025] Will C 10 7,600 tons of heavy aromatic raw materials are introduced into the first rectification tower T101 with a diameter of 1.6m, a tower height of 35m, and a number of trays of 130 via pipeline 1 for rectification. , the reflux ratio is 1: 6, the temperature at the bottom of the tower is controlled at 180°C, 1000# aromatic hydrocarbon solvent is extracted from the top of the T101 tower through pipeline 2, the durene rich liquid is extracted from the side line pipeline 3, and the distillate at the bottom of the tower is introduced through pipeline 4 The diameter is 1.2m, the height of the tower is 28m, and the number of trays is 118 in the second rectification tower T102 to continue rectification, the control tower top temperature is 140 ℃, the absolute pressure of the tower top is 10KPa, and the reflux ratio is 1: 6, The temperature at the bottom of the tower is controlled at 240°C, 1500# aromatic hydrocarbon solvent is extracted from the top of the T102 tower throu...
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Abstract
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