A kind of production device and production method of intermediate temperature modified asphalt without mesophase
A modified asphalt and production method technology, applied in the field of coal chemical industry, can solve the problems of high reaction temperature, reduce the bonding strength of coal tar pitch and solid carbonaceous materials, and increase the strength of unfavorable carbon materials, so as to achieve the effect of saving resources and energy
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Embodiment 1
[0038] Such as figure 1 As shown, a medium-temperature modified asphalt production device without mesophase includes a main tower and a reactor connected to the main tower. The main tower 1 is connected to several normal-pressure reactors 3 connected in series through a delivery pump 2; the reactor 3 is provided with an agitator 4, and each reaction kettle 3 is provided with a heating device 5; the upper part of the reaction kettle 3 is connected with an immersion cooler 8, and the immersion cooler 8 is connected with a gas-liquid separator 9, and the gas-liquid separation The lower part of the device 9 is connected with a flash oil tank 10; the lower part of the reactor 3 is connected with the asphalt intermediate tank 7 through an inverted U-shaped pipe 6, and the function of the inverted U-shaped pipe is to keep the liquid level in the reactor constant.
[0039] The gas-liquid separator 9 is connected to a liquid seal tank 11 , and the liquid seal tank 11 is connected to t...
Embodiment 2
[0043] Such as figure 1As shown, a medium-temperature modified asphalt production device without mesophase includes a secondary evaporator 1 and a reaction kettle connected to the secondary evaporator 1. The secondary evaporator 1 is connected to several normal-pressure reaction kettles 3 connected in series through gravity flow. connected; the reactor 3 is provided with a stirrer 4, and each reactor 3 is provided with a heating device 5; the upper part of the reactor 3 is connected with an immersion cooler 8, and the immersion cooler 8 is connected with a gas-liquid separator 9 The lower part of the gas-liquid separator 9 is connected to a flash oil tank 10; the lower part of the reactor 3 is connected to the asphalt intermediate tank 7 through an inverted U-shaped pipe 6, and the function of the inverted U-shaped pipe is to keep the liquid level in the reactor constant.
[0044] The gas-liquid separator 9 is connected with a liquid seal tank 11 , and the liquid seal tank 11...
Embodiment 3
[0048] The high-temperature tar is distilled under normal pressure, and the medium-temperature pitch is discharged from the secondary evaporator 1. The SP is 75°C, the TI is 14%, the QI is 4%, and the CV is 47%. Medium-temperature asphalt passes through three series-connected normal-pressure reactors in sequence. The reactors are heated and kept warm by high-temperature exhaust gas. The reaction temperature of the first kettle is 375°C, the second kettle is 380°C, and the third kettle is 375°C. The reaction time is 3 hours each (9 hours in total). Obtain medium temperature modified asphalt. SP is 93°C, TI is 27%, QI is 7%, CV is 54%, and there is no mesophase. The medium-temperature modified asphalt enters the asphalt middle tank through the inverted U-shaped pipe.
[0049] Others are the same as embodiment 2.
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Abstract
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