Method for producing high-calorific-value combustible gas through in-situ catalysis of biomass pyrolysis volatile component
A biomass pyrolysis and in-situ catalysis technology, which is applied in chemical instruments and methods, molecular sieve catalysts, chemical/physical processes, etc. The effect of large contact area, increased calorific value and quality
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Embodiment 1
[0027] Weigh 50g γ-Al 2 o 3 The carrier was calcined in a muffle furnace at 550°C for 4 hours. Take La(NO 3 ) 3 ·6H 2 O5.63g, Ni(NO 3 ) 2 ·6H 2 O3.78g was dissolved in 30mL deionized water, stirred and dissolved, and another 5.46g monohydrate citric acid was dissolved in 20mL deionized water, stirred and dissolved (wherein n(La 3+ ): n(Ni 2+): n (citric acid) = 1:1:2), the citric acid monohydrate solution was dropped into the mixed metal salt solution at a constant rate of 2 drops per second, stirred in a water bath at 80°C for 8 hours to obtain a gel-like substance, and then The gel-like substance was dried in an oven at 105°C for 24 hours until completely dried. Take 3.19g of the dried precursor and dissolve it in 40mL deionized water to make an impregnation solution, pour the impregnation solution into the roasted γ-Al 2 o 3 In the carrier, impregnate the load at 25°C for 5h, then bake in an oven at 65°C for 24h until the moisture is completely dried, and finally...
Embodiment 2
[0029] Weigh the corresponding quality of the reagent, and the operation steps are the same as in Example 1 to obtain the finished catalyst B. The mass percentage of each component in the catalyst consists of: LaFe 0.5 Ni 0.5 o 3 : 3%; TiO 2 : 97%, the calcination condition is 800 ℃ constant temperature 6h. Weigh 100g of this catalyst and place it in the lower section of the fixed-bed reactor. The upper section of the reactor is equipped with 180g of walnut shells as the reaction raw material, wherein the walnut shells are rich in lignin components. Lignin is a molecular structure containing oxyphenylpropane Aromatic high polymer of structural units of alcohol and its derivatives. Under the conditions of pyrolysis furnace temperature of 600°C, nitrogen protection, normal pressure, and catalyst temperature of 600°C, the same temperature and synchronous in-situ catalytic methanation of volatile matter was carried out, and the evaluation of dry distillation catalytic pyrolysi...
Embodiment 3
[0031] The corresponding mass of reagents was weighed, and the operation steps were the same as in Example 1 to obtain the finished catalyst C. The mass percentage of each component in the catalyst consists of: LaCu 0.3 Ni 0.7 o 3 : 9%; ZrO 2 : 91%, the calcination condition is 700 ℃ constant temperature 6h. Weigh 10g of the catalyst and place it in the lower section of the fixed-bed reactor, and the upper section of the reactor is equipped with 20g of birch wood chips as the reaction raw material, wherein the birch wood chips are rich in carbon-containing polymers such as lignin and cellulose. Under the conditions of pyrolysis furnace temperature of 650°C, nitrogen protection, normal pressure, and catalyst temperature of 650°C, the same temperature and synchronous in-situ catalytic methanation of volatile matter was carried out, and the evaluation of dry distillation catalytic pyrolysis reaction was carried out: thermal After the combustible gas is collected, it is analyz...
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