In-fluid-bed reactivation method for catalyst for direct preparation of low-carbon olefins from synthesis gas
A technology for low-carbon olefins and synthesis gas, which is used in physical/chemical process catalysts, hydrocarbon production from carbon oxides, chemical instruments and methods, etc., and can solve the problems of over-temperature, recovery as before, and performance degradation of Fischer-Tropsch synthesis catalysts, etc. To achieve the effect of simple operation, avoid over temperature, good heat dissipation
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Embodiment 1
[0020] (1) 1.5 inches, containing 100g of original iron-based catalyst (the catalyst is prepared by co-precipitation spray drying, and the composition is 100Fe / 80Mn / 5K / 80SiO in atomic ratio 2 ) And it has been reacted for about 1500 hours, and the inlet air of the fluidized bed reactor with decreased activity is switched to the space velocity of 300h -1 的nitrogen;
[0021] (2) Adjust the pressure of the reactor to normal pressure, adjust the temperature of the reactor to 280°C, and stay in this atmosphere and this temperature and pressure for 3 hours.
[0022] (3) Adjust the temperature of the reactor to 230°C and the pressure to 0.01MPa;
[0023] (4) Switch the intake air to an airspeed of 300h -1 A mixture of nitrogen and hydrogen, stay in this atmosphere and temperature and pressure for 3 hours, where the volume ratio of nitrogen to hydrogen is N 2 : H 2 =10:1;
[0024] (5) Keep the previous temperature and space velocity unchanged, and increase the reactor pressure to 0.2MP;
[0025...
Embodiment 2
[0029] (1) 1.5 inches, containing 100g of original iron-based catalyst (the catalyst is prepared by co-precipitation spray drying, and the composition is 100Fe / 80Mn / 5K / 80SiO in atomic ratio 2 ) And it has been reacted for about 1500 hours, and the inlet air of the fluidized bed reactor with decreased activity is switched to the space velocity of 10000h -1 Of helium
[0030] (2) Adjust the pressure of the reactor to normal pressure, adjust the temperature of the reactor to 520℃, and stay in this atmosphere and this temperature and pressure for 30h;
[0031] (3) Adjust the temperature of the reactor to 480°C and the pressure to 5.0MPa;
[0032] (4) Switch the intake air to an airspeed of 10000h -1 Hydrogen, stay in this atmosphere and this temperature and pressure for 60 hours;
[0033] (5) Keep the previous temperature and space velocity unchanged, and increase the reactor pressure to 10MP;
[0034] (6) Switch the activation gas to a mixed gas of helium, carbon monoxide and propylene, th...
Embodiment 3
[0038] (1) 1.5 inches, containing 100g of original iron-based catalyst (the catalyst is prepared by co-precipitation spray drying, and the composition is 100Fe / 80Mn / 5K / 80SiO in atomic ratio 2 ) And it has been reacted for about 1500 hours, and the inlet air of the fluidized bed reactor with decreased activity is switched to the space velocity of 1000h -1 的argon;
[0039] (2) Adjust the pressure of the reactor to normal pressure, adjust the temperature of the reactor to 300°C, and stay in this atmosphere and this temperature and pressure for 5 hours.
[0040] (3) Adjust the temperature of the reactor to 245°C and the pressure to 0.1MPa;
[0041] (4) Switch the intake air to an airspeed of 1000h -1 A mixture of argon and hydrogen, stay in this atmosphere and this temperature and pressure for 10 hours, where the volume ratio of argon to hydrogen is argon: H 2 =1:1;
[0042] (5) Keep the previous temperature and space velocity unchanged, and increase the reactor pressure to 0.6MPa;
[0043]...
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