System and method for separating waste catalyst in Fischer-Tropsch synthesis residue wax
A waste catalyst and Fischer-Tropsch synthesis technology, applied in chemical instruments and methods, magnetic separation, solid separation, etc., can solve the problems of poor operation continuity, complicated process, and low recovery rate of synthetic wax, and achieve recovery and easy operation Effect
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Embodiment 1
[0082] Synthesis gas is subjected to Fischer-Tropsch synthesis reaction in a slurry bed Fischer-Tropsch synthesis reactor (pressure 3.0 MPa, temperature 260°C) using an iron-based catalyst, and the obtained slurry containing catalyst and heavy wax is discharged to the slag with agitator. In the wax flash tank, the pressure of the slag wax flash tank is 0.5MPa. As the pressure decreases, the dissolved synthesis gas and low-carbon hydrocarbons in the slurry volatilize to obtain Fischer-Tropsch synthesis slag wax. The temperature of the slag wax flash tank is 150° C., and the mass fraction of spent catalyst in the slag wax is 15%.
[0083] The slag wax is introduced into the feed port of the primary magnetic separator E1, and the feed rate is 300kg / h. In the primary magnetic separator E1; the diameter of the drum 6 is 600 mm, and the length is 800 mm; the first magnet 3 is a permanent magnetic pole, a fan-shaped columnar body, and the central angle of the fan is 280 °; the box b...
Embodiment 2
[0088] Synthesis gas is subjected to Fischer-Tropsch synthesis reaction in a slurry bed Fischer-Tropsch synthesis reactor (pressure 2.0 MPa, temperature 300°C) using an iron-based catalyst, and the obtained slurry containing catalyst and heavy wax is discharged to the slag with agitator. In the wax flash tank, the pressure of the slag wax flash tank is 0.3MPa. As the pressure decreases, the dissolved synthesis gas and low-carbon hydrocarbons in the slurry volatilize to obtain Fischer-Tropsch synthesis slag wax. The temperature of the slag wax flash tank is 200° C., and the mass fraction of spent catalyst in the slag wax is 10%.
[0089] The slag wax is introduced into the feed port of the primary magnetic separator E1, and the feed rate is 600kg / h. In the primary magnetic separator E1; the diameter of the drum 6 is 600 mm, and the length is 800 mm; the first magnet 3 is a permanent magnetic pole, a fan-shaped columnar body, and the central angle of the fan is 300 °; the box b...
Embodiment 3
[0094] The synthesis gas is subjected to Fischer-Tropsch synthesis reaction in a slurry bed Fischer-Tropsch synthesis reactor (pressure 2.6MPa, temperature 280°C) using an iron-based catalyst, and the obtained slurry containing catalyst and heavy wax is discharged to the slag with agitator. In the wax flash tank, the pressure of the slag wax flash tank is 1.0MPa. As the pressure decreases, the dissolved synthesis gas and low-carbon hydrocarbons in the slurry volatilize to obtain Fischer-Tropsch synthesis slag wax. The temperature of the slag wax flash tank is 180° C., and the mass fraction of spent catalyst in the slag wax is 20%.
[0095] The slag wax is introduced into the feed port of the primary magnetic separator E1, and the feed rate is 600kg / h. In the first-stage cylindrical magnetic separator E1; the diameter of the drum 6 is 600 mm, and the length is 800 mm; the first magnet 3 is a permanent magnetic pole, a fan-shaped columnar body, and the central angle of the fan ...
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