Production process for producing modified asphalt from medium-low-temperature coal tar heavy components
A technology of low-temperature coal tar and modified asphalt, which is applied in the direction of chemically processing tar pitch/petroleum pitch/natural pitch, tar processing by distillation method, etc., to achieve the effects of controllable product quality and simple production process
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Embodiment 1
[0038] The medium and low temperature coal tar heavy components produced in the medium and low temperature coal tar processing process are used as raw materials. The indicators: toluene insolubles 4.4%, quinoline insolubles 1.9%, softening point 86.5°C, coking value 29.8%, ash 0.2%, passed The asphalt pump is heated to 175°C through the asphalt heat exchanger, mixed with the asphalt from the asphalt circulation pump, enters the modified asphalt heating furnace to be heated to 400°C, and then enters the modified asphalt reactor for modification. A part of the light oil flashes into the flash oil condenser to condense and then enters the heavy oil intermediate tank. A part of the modified bitumen is recycled, and a part is recovered. The recovered part enters the vacuum flash evaporator, and the heavy oil is removed under a vacuum degree of 85kPa to obtain Products Modified Bitumen. The vacuum flash oil gas is condensed by the heavy oil condenser, enters the heavy oil separator ...
Embodiment 2
[0041] The medium and low temperature coal tar heavy components produced in the medium and low temperature coal tar processing process are used as raw materials. The indicators: toluene insoluble matter 5.3%, quinoline insoluble matter 2.4%, softening point 90°C, coking value 32.5%, ash content 0.2%, passed The asphalt pump is heated to 170°C through the asphalt heat exchanger, mixed with the asphalt from the asphalt circulation pump, enters the modified asphalt heating furnace to be heated to 390°C, and then enters the modified asphalt reactor for modification. A part of the light oil flashes into the flash oil condenser to condense and then enters the heavy oil intermediate tank. A part of the modified bitumen is recycled, and a part is recovered. The recovered part enters the vacuum flash evaporator, and the heavy oil is removed under a vacuum degree of 85kPa to obtain Products Modified Bitumen. The vacuum flash oil gas is condensed by the heavy oil condenser, enters the he...
Embodiment 3
[0044]The medium and low temperature coal tar heavy components produced in the medium and low temperature coal tar processing process are used as raw materials. The indicators: toluene insolubles 4.1%, quinoline insolubles 1.6%, softening point 85.5°C, coking value 26.8%, ash 0.2%, passed The asphalt pump is heated to 175°C through the asphalt heat exchanger, mixed with the asphalt from the asphalt circulation pump, enters the modified asphalt heating furnace to be heated to 400°C, and then enters the modified asphalt reactor for modification. A part of the light oil flashes into the flash oil condenser to condense and then enters the heavy oil intermediate tank. A part of the modified bitumen is recycled, and a part is recovered. The recovered part enters the vacuum flash evaporator, and the heavy oil is removed under a vacuum degree of 85kPa to obtain Products Modified Bitumen. The vacuum flash oil gas is condensed by the heavy oil condenser, enters the heavy oil separator f...
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