Method for performing catalytic pyrolysis on tar in biomass gasifier
A catalytic cracking and biomass technology, applied in the field of energy and chemical industry, can solve the problems of increased gas flow resistance, complex gasification furnace design, accelerated catalyst deactivation, etc., to achieve improved efficiency, long contact time, and high dispersion Effect
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Embodiment 1
[0025] (1), the attapulgite clay is pre-stocked and homogenized, and then water is added. The weight percentage of water and attapulgite clay is 30-50%: 50-70%. Cutting and extruding into attapulgite clay flakes to promote the depolymerization and dispersion of attapulgite crystal bundles;
[0026] (2), drying the attapulgite-type clay flakes and pulverizing them into attapulgite clay powders passing through a 200-mesh sieve (that is, the particle size is less than 0.075mm);
[0027] (3), the attapulgite clay powder and biomass are uniformly mixed in a weight ratio of 5: 100, and enter the moving bed biomass gasifier through a screw feeder to carry out catalytic cracking tar reaction, and the heat in the gasifier The solution temperature is 900-1000°C. The simulated experimental results of attapulgite clay catalytic pyrolysis of tar are shown in figure 1 .
Embodiment 2
[0029] (1), pulverizing dolomite attapulgite clay into dolomite attapulgite clay powder by 200 mesh sieve (that is, particle diameter is less than 0.075mm);
[0030] (2), uniformly mix dolomite attapulgite clay powder and biomass at a weight ratio of 3:100, enter the moving bed biomass gasifier through a screw feeder for catalytic cracking tar reaction, and The pyrolysis temperature is 900-1000°C. The simulation experiment results of the catalytic cracking of tar with dolomite attapulgite clay are shown in figure 2 .
Embodiment 3
[0032] (1), pulverizing the calcined magnesite into a calcined magnesite powder passing through a 200-mesh sieve (that is, the particle size is less than 0.075 mm);
[0033] (2), calcined magnesite powder and biomass are uniformly mixed in a weight ratio of 3:100, and enter the moving bed biomass gasifier through a screw feeder to carry out catalytic cracking tar reaction, and the heat in the gasifier The solution temperature is 900-1000°C. The simulation experiment results of calcined magnesite catalytic cracking tar are shown in image 3 .
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