Biomass gasification gas tar catalytic cracking purification process and its device
A technology for catalytic cracking and biomass, which is applied in the field of biomass gasification gas tar catalytic cracking purification process and its devices, can solve the problems of difficult continuous and stable operation of the process, low thermal efficiency, and reduced gasification efficiency, so as to improve the gasification efficiency. and system heat utilization, improving system heat efficiency, and the effect of simple purification device
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Embodiment 1
[0045] This embodiment provides a biomass gasification gas tar catalytic cracking purification process, such as figure 1 The shown device, the specific tar catalytic cracking purification process includes the following steps:
[0046] Step 1, open the second valve V2, the fourth valve V4, the fifth valve V5, the seventh valve V7, close the first valve V1, the third valve V3, the sixth valve V6, and the eighth valve V8, so that the first drum The bubbling fluidized bed 3 operates in the tar catalytic cracking mode, so that the second bubbling fluidized bed 4 is operated in the catalyst regeneration mode;
[0047] Step 2, the crude gasification gas a is dedusted by the first cyclone separator 1 to obtain dedusted gasification gas b, and the dedusted gasification gas b is heated to above 800°C through the regeneration flue gas heat exchanger 2 to obtain heated gasification Gas c, and then the heated gasification gas c enters the first bubbling fluidized bed 3 for tar catalytic c...
Embodiment 2
[0057] This embodiment provides a biomass gasification gas tar catalytic cracking purification device, the device is configured with two bubbling fluidized beds 3 and 4 for intermittently alternately operating in the tar catalytic cracking mode and catalyst oxidation regeneration mode, flow A wind cap is installed at the bottom of the fluidized bed for air distribution, and the bed material of the fluidized bed is the catalyst required for catalytic cracking of tar, which can be dolomite, metal-based catalysts, etc. Specifically, such as figure 1 As shown, it includes a flue gas heat exchanger 2, a first bubbling fluidized bed 3, a second bubbling fluidized bed 4, a heat exchanger 7, a spray tower 8 and a gas-liquid separator 11, wherein:
[0058] The air inlet at the bottom of the first bubbling fluidized bed 3 is provided with a first valve V1 and a second valve V2 in parallel, and the bottom of the second bubbling fluidized bed 4 is provided with a third valve V3 and a four...
Embodiment 3
[0066] Such as figure 1 As shown, in this application example, the inlet condition of crude gasification gas a is 700°C, the tar content is about 1g / Nm3, and the tar components are mainly monophenols, heterocyclic phenols and polycyclic aromatic hydrocarbons.
[0067] The second valve V2, the fourth valve V4, the fifth valve V5, and the seventh valve V7 are set to be open, and the first valve V1, the third valve V3, the sixth valve V6, and the eighth valve V8 are set to be closed. After being dedusted by the first cyclone dust collector 1, the crude gasification gas a is heated to 800°C by the regenerative flue gas heat exchanger 2, and then enters the first bubbling fluidized bed 3 for tar catalytic cracking, and the temperature drops to 600-600°C after cracking. 700°C, the air e is further heated through the heat exchanger 7, and the temperature of the gas is lowered to 500-600°C and then passed into the spray tower 8 for quenching. The air e preheated to 500° C. is passed ...
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