A kind of recovery method of Fischer-Tropsch synthesis iron series catalyst
A recovery method and a technology of Fischer-Tropsch synthesis, applied in the direction of carbon compound catalysts, catalysts, chemical instruments and methods, etc., can solve problems such as complex products, difficulty in pure catalysts, and complex surface properties of spent catalysts
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Embodiment 1
[0027] The recovery method of the Fischer-Tropsch synthesis iron-based catalyst of the present embodiment comprises the following steps:
[0028] (1) Add ethyl acetate, cyclohexane and morpholine sequentially to the waste catalyst raw material, the heating temperature of the first stage is 60-100°C, the heating rate is 15°C / hour, and the heating temperature of the second stage is 100-100°C 140°C, the heating rate is 20°C / hour, the heating temperature of the third stage is 140-200°C, the heating rate is 20°C / hour, the stirring rate is 200r / min, and the extraction is carried out, and the organic solvent will remove the waste catalyst raw material surface The hydrocarbon compound is dissolved and extracted to leave the mixture system to obtain the intermediate treatment product A;
[0029] Wherein, the volume mass ratio of ethyl acetate to the spent catalyst raw material is 100mL: 1mg, the volume mass ratio of cyclohexane to the spent catalyst raw material is 100mL: 1mg, and the ...
Embodiment 2
[0050] The recovery method of the Fischer-Tropsch synthesis iron-based catalyst of the present embodiment comprises the following steps:
[0051] (1) Add ethyl acetate and morpholine sequentially to the waste catalyst raw material, the heating temperature of the first stage is 60-100°C, the heating rate is 15°C / hour, the heating temperature of the second stage is 100-140°C, and the heating The rate is 20°C / hour, the heating temperature of the third stage is 140-200°C, the heating rate is 20°C / hour, the stirring rate is 200r / min, and the extraction is carried out, and the organic solvent dissolves the hydrocarbon compounds on the surface of the spent catalyst raw material And extract and leave the mixture system to obtain intermediate treatment A;
[0052] Wherein, the volume mass ratio of ethyl acetate to the spent catalyst raw material is 100mL: 1mg, and the volume mass ratio of morpholine to the spent catalyst raw material is 70mL: 1mg.
[0053] Other steps in this embodime...
Embodiment 3
[0055] The recovery method of the Fischer-Tropsch synthesis iron-based catalyst of the present embodiment comprises the following steps:
[0056] (1) Add cyclohexane and morpholine sequentially to the waste catalyst raw material, the heating temperature of the first stage is 60-100°C, and the heating rate is 15°C / hour, the heating temperature of the second stage is 100-140°C, and the heating The rate is 20°C / hour, the heating temperature of the third stage is 140-200°C, the heating rate is 20°C / hour, the stirring rate is 200r / min, and the extraction is carried out, and the organic solvent dissolves the hydrocarbon compounds on the surface of the spent catalyst raw material And extract and leave the mixture system to obtain intermediate treatment A;
[0057] Wherein, the volume mass ratio of cyclohexane to the spent catalyst raw material is 100 mL:1 mg, and the volume mass ratio of morpholine to the spent catalyst raw material is 70 mL:1 mg.
[0058] Other steps in this embodi...
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