A method for catalyzing biomass pyrolysis using heat treatment products of waste lithium batteries
A waste lithium battery and biomass pyrolysis technology, which is applied in special forms of dry distillation, coke oven, petroleum industry, etc., can solve the problems of short cycle life, increase yield, reduce oxygen-containing compound content, and increase H2O content Effect
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Embodiment 1
[0023] Embodiment 1, a method for utilizing waste lithium battery heat treatment products to catalyze biomass pyrolysis, the method comprises the following steps:
[0024] Step 1, pretreating the waste lithium battery to obtain cathode and anode electrode materials of the waste lithium battery; specifically: first removing the hard shell of the waste lithium battery, grinding, and sieving to obtain the cathode and anode electrode materials.
[0025] Step 2: Pyrolyzing the cathode and anode electrode materials to obtain electrode material heat treatment products, namely mixed metal element and oxide, the main components of which include Ni, Co, Mn and Fe.
[0026] Step 3, using wheat straw as the original biomass, mix the wheat straw with the electrode material heat treatment product, and mix the mixed sample at 500°C under the carrier gas N 2 When the flow rate is 300mL / min, pyrolysis is rapid until the reaction is complete. The yield of bio-oil collected was 47.13%, and the ...
Embodiment 2
[0027] Embodiment 2 is different from Embodiment 1:
[0028] Step 3: Taking wheat straw as the biomass as it is, mixing the wheat straw and the electrode material heat treatment product, and mixing the mixed sample at 600°C under the carrier gas N 2 When the flow rate is controlled at 1000mL / min, pyrolysis is rapid until the reaction is complete. The collected bio-oil yield was 46.35%. The chemical composition of the bio-oil was analyzed, and the ester content was only 8.08%, and the hydrocarbon content rose to 5.77%. H in the test gas product composition 2 The concentration ratio is 26.02%, and the generated H 2 The total mass is 3.73 mg / g wheat straw.
Embodiment 3
[0029] Embodiment 3 is different from Embodiment 1:
[0030] Step 3, using rice straw as biomass, mix rice straw and electrode material heat treatment product, and mix the sample at 400°C under carrier gas N 2 When the flow rate is controlled at 100mL / min, pyrolysis is rapid until the reaction is complete. The collected bio-oil yield was 42.74%. The chemical composition of the bio-oil was analyzed, and the ester content was only 9.61%, and the hydrocarbon content rose to 9.29%. H in the test gas product composition 2 The concentration ratio is 17.53%. Generated H 2 The total mass is 1.66 mg / g rice straw.
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