Preparation method of catalyst for lightening of biomass tar heavy component
A technology for heavy components and catalysts, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, naphtha catalytic reforming, etc., to achieve low production costs, improve utilization efficiency, and realize Lightweight effect
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Embodiment 1
[0021] Put 50g of dried and sieved coal sample and 100ml of 12wt% nitrate solution (the molar ratio of Fe and Mn metal elements is 7:3) in a stainless steel reaction kettle at 213°C, keep it at a constant temperature for 5h, and then suction filter , washed, dried in a vacuum oven at 80°C to constant weight, and then in N 2 Under the atmosphere, the heating rate was raised to 500 °C at a rate of 10 °C / min, and the constant temperature was pyrolyzed for 4 hours to obtain 26 g of carbon-based desulfurization adsorbent. The carrier was semi-coke, and the active components were 11.0 wt % iron oxide and 5.0 wt % A mixture of manganese oxides. Use this adsorbent to adsorb H in the gas at 400°C 2 After S, the spent carbon-based desulfurizer is obtained.
[0022] The gained spent charcoal-based desulfurizer was mixed in 40ml of 10wt% Mg(HCO 3 ) 2 Immerse in the solution for 4h, then suction filter, and dry in a vacuum oven at 50°C for 6h; at 750°C and N 2 Roasting under the atmos...
Embodiment 2
[0025] Put 50g of dried and sieved coal sample and 100ml of 15wt% nitrate solution containing iron, manganese and cerium metal active components (the molar ratio of Fe, Mn and Ce metal elements is 6:4:1) In a stainless steel reaction kettle at 213°C, place it at a constant temperature for 5 hours, then filter it with suction, wash it, dry it in a vacuum oven at 80°C to constant weight, and then place it under N 2 Under the atmosphere, the heating rate was raised to 500°C at a rate of 10°C / min, and the constant temperature was pyrolyzed for 4 hours to obtain 27g of carbon-based desulfurization adsorbent. The carrier was semi-coke, and the active components were mixed oxides of Fe, Mn, and Ce. Adsorb H in the gas with this adsorbent 2 After S, the spent carbon-based desulfurizer is obtained.
[0026] The gained spent charcoal-based desulfurizer was mixed in 40ml of 10wt% Mg(HCO 3 ) 2 Immerse in the solution for 4h, then suction filter, and dry in a vacuum oven at 50°C for 6h;...
Embodiment 3
[0029] Weigh 5g of the lightweight catalyst prepared in Example 2, put it into a fixed-bed reactor at normal pressure, the reactor temperature is 500°C, nitrogen is used as the carrier gas, hydrogen and water vapor are used as the reforming reaction gas, and the total gas flow rate is 300ml / min, where the volume concentration of hydrogen is 7%, and the volume concentration of water vapor is 16%. Biomass tar is injected into the reactor through an air-cooled probe at a sample amount of 150 mg / min by a syringe pump, and fully contacted with the light weight catalyst. The relative content of light components in the biomass tar after catalytic reforming Increased from 40% to 95%.
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