Purification method and system of lignite wax crude extract
A purification method and crude extraction technology are applied in the field of purification of lignite crude wax extract, and achieve the effects of low solvent residue, increased economic value and high purity
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Embodiment 1
[0072] use figure 1 The system purifies the crude montan wax extract raw material, crushes 50g of the montan wax crude extract raw material to 20-50 mesh, puts it into the extraction tank, and removes the CO in the solvent tank 2 After being pressurized to 30MPa by the solvent pump, it is preheated to 35°C by the preheater and 400mL is passed into the extraction tank; the temperature in the extraction tank is controlled at 35°C and the pressure is 30MPa. After reacting for 2 hours, the raffinate in the lower layer of the extraction tank enters the flash tower to be separated from the solvent, and asphalt is precipitated. The solvent and extract in the upper layer of the extraction tank are slowly heated to 40°C and then enter the separator I; the montan wax in the lower layer of the separator I enters the flash tower. The distillation tower I is further separated from the solvent, and the montan wax is precipitated. The solvent and extract in the upper layer of the separator I...
Embodiment 2
[0076] use figure 2 The system purifies the crude montan wax extract raw material, crushes 50g of the montan wax crude extract raw material to 20-50 mesh, puts it into the extraction tank, and the CO in the solvent tank 2 and the ethanol in the entrainer tank are respectively pressurized to 30MPa by the solvent pump and then enter the mixer to mix to obtain the extractant, CO 2 The molar ratio with ethanol is 1:0.04, the extractant is preheated to 35°C by a preheater, and then 400mL of extractant is passed into the extraction tank; the temperature in the extraction tank is controlled at 35°C and the pressure is 30MPa. After reacting for 2 hours, the raffinate in the lower layer of the extraction tank enters the flash tower for separation, and the asphalt is precipitated. The solvent and extract in the upper layer of the extraction tank are slowly heated to 40°C and then enter the separator I; the montan wax in the lower layer of the separator I enters the flash tower I is fu...
Embodiment 3
[0080] use figure 2 The system purifies the crude montan wax extract raw material, crushes 50g of the montan wax crude extract raw material to 20-50 mesh, puts it into the extraction tank, and the CO in the solvent tank 2 and the ethanol in the entrainer tank are respectively pressurized to 30MPa by the solvent pump and then enter the mixer to mix to obtain the extractant, CO 2 The molar ratio with ethanol is 1:0.04, the extractant is preheated to 40°C by a preheater, and then 400mL of extractant is passed into the extraction tank; the temperature in the extraction tank is controlled at 40°C and the pressure is 30MPa. After reacting for 4 hours, the raffinate in the lower layer of the extraction tank enters the flash tower for separation, and the asphalt is precipitated. The solvent and extract in the upper layer of the extraction tank are slowly heated to 40°C and then enter the separator I; the montan wax in the lower layer of the separator I enters the flash tower I is fu...
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