Process and device for performing gasification energy conversion on biomass recycled from construction wastes
A technology for construction waste and biomass, applied in the field of biomass, can solve the problems of inability to use interchangeably, affect combustion, toxic substances, etc., and achieve the effects of low cost, elimination of leakage, and reduction of investment.
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Embodiment 1
[0041] The present invention will be further described below in conjunction with the accompanying drawings.
[0042] A kind of construction waste recycling combustible biomass gasification device of the present invention comprises cracking furnace 1, primary purifier 2, secondary purifier 3, primary separator 4, secondary separator 5, Roots blower 6 and theirs Connecting pipelines, the outer wall of the cracking furnace is provided with a spiral flue, the flue is connected with the input end of the thermostat arranged on the cracking furnace 1, and the output end of the thermostat is connected with the primary purifier 2, The front end of the secondary purifier 3 is connected to the primary purifier 2, and the rear end is connected with the primary separator 2. The secondary purifier 3 is provided with a cyclone separator, and the cyclone separator is connected with the secondary purifier 3. The steam outlets are connected; the Roots blower is connected with the secondary sepa...
Embodiment 2
[0045] Use the device of embodiment 1 to carry out the gasification of the biomass recovered from construction waste, wherein the biomass recovered from construction waste is cracked and gasified in a cracking furnace, followed by primary purification and secondary purification, and then a secondary purification Stage separation and secondary separation. After secondary separation, exhaust gas is led out by fan. The construction waste is waste from building demolition, and its biomass includes wood products, plastics, textiles and the like. The catalyst used in the cracking process includes a carrier and active components loaded on the carrier, wherein the carrier is fly ash, and the catalytically active components are NiO, CuO, Fe 2 o 3A composite oxide of three oxides, the catalyst is expressed as NiO-CuO-Fe 2 o 3 / fly ash, wherein the molar ratio of Ni, Cu, Fe is 5:1:15, based on the total weight of the catalyst, NiO-CuO-Fe 2 o 3 The content of the composite oxide was...
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Abstract
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