Method for removing quinoline insoluble substances in coal tar pitch and system used in method
A technology of coal tar pitch and quinoline, applied in the processing of tar pitch/petroleum pitch/natural pitch, processing tar pitch/petroleum pitch/natural pitch by distillation, processing tar pitch/petroleum pitch/natural pitch by selective extraction, etc. , can solve the problems of low yield of refined asphalt, low yield of refined asphalt, long settling time, etc., and achieve the effect of increasing yield and mixed solvent recovery, reducing volatilization of light components, and increasing economic benefits
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Embodiment 1A
[0049] A system used in a method for removing quinoline insolubles in coal tar pitch, characterized in that:
[0050] The system includes: a pressurized extraction and sedimentation device 1, a distillation tower 4;
[0051] There is a stirring device 102 inside the pressurized extraction and sedimentation device 1, a coal tar pitch inlet 101 is provided at the right end of the top of the pressurized extraction and sedimentation device 1, and a compressed gas inlet 103 and a pressure gauge 104 are provided at the left end of the top of the pressurized extraction and sedimentation device 1;
[0052] There is a tar residue outlet 107 at the left end of the lower part of the pressurized extraction and sedimentation device 1, and a heating medium outlet 106 is arranged at the middle part of the left end, and there is a mixed solvent inlet 105 at the left end of the upper part of the pressurized extraction and sedimentation device 1, and there is a gap between the mixed solvent inlet ...
Embodiment 1B
[0057] Washing oil is used as the aromatic hydrocarbon solvent, kerosene is used as the aliphatic hydrocarbon solvent, and the mixed solvent is prepared by mixing at a weight ratio of 0.25:1;
[0058] Then mix the medium-temperature coal tar pitch and the mixed solvent in a weight ratio of 1:3, place it in the pressurized extraction and sedimentation device 1, fill it with air or nitrogen at a certain pressure, and increase the pressure of the system by heating the solvent to 110 °C, control the pressure inside the tank of the pressurized extraction and settling device 1 to 0.5Mpa, and control the temperature for 1 hour of extraction, then settling at constant temperature and pressure for 2 hours.
[0059] After standing and settling, the solvent in the upper layer is distilled under reduced pressure, and the mixed solvent is recycled. The recovery rate can reach more than 90%. After removing the quinoline insoluble matter, the content of the quinoline insoluble matter in aspha...
Embodiment 2
[0062] The mixed solvent is prepared by mixing aromatic hydrocarbon solvent as washing oil and aliphatic hydrocarbon solvent as kerosene at a weight ratio of 0.3:1. Mix medium-temperature coal tar pitch and mixed solvent in a weight ratio of 1:2, place in a pressurized extraction tank, fill with air or nitrogen at a certain pressure, control the pressure in the tank to 0.7Mpa, raise the temperature to 100°C, and control the temperature After 1 hour of extraction under low pressure, it was allowed to settle at constant temperature and pressure for 2 hours.
[0063] After standing and settling, the solvent in the upper layer is distilled under reduced pressure, and the mixed solvent is recycled, and the recovery rate can reach more than 90%, but after removing the quinoline insolubles, the quinoline insoluble content of asphalt is 0.1%, and the yield is 82%.
[0064] According to the process of this example, due to the increased use of pressurized equipment to treat asphalt and ...
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