A method for directional preparation of aromatics by pyrolysis of biomass and plastic waste
A biomass pyrolysis and biomass technology, which is used in the preparation of liquid hydrocarbon mixtures, the treatment of hydrocarbon oil, and hydrocarbon oil treatment products, etc., can solve the problems of poor tunability of reaction parameters, low yield of target products, and easy coking of catalysts, etc. problems, to achieve good environmental and economic benefits, improve yield and selectivity, and prolong catalyst life.
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Embodiment 1
[0034] First, the biomass (straw) is pyrolyzed in a pyrolysis reactor at 700°C and 10MPa to produce biomass pyrolysis products mainly composed of macromolecular oxygenates; at the same time, the plastic waste (polyethylene plastic ) is pyrolyzed in a pyrolysis reactor at 400°C under normal pressure to form plastic pyrolysis products mainly composed of long-chain hydrocarbon compounds; wherein, the feed mass ratio of biomass to plastic waste is biomass : Plastic = 1:10. Secondly, the biomass pyrolysis product is passed through the ZrO in the catalytic cracking reactor 2 Based on super strong solid acid catalyst bed, under the condition of 700℃, 10Mpa, catalyst:biomass = 1:10, the primary catalytic cracking is carried out to form primary catalytic cracking products of biomass mainly composed of small molecule oxygen-containing compounds; at the same time Pass the plastic pyrolysis product through SiO in the catalytic cracking reactor 2 ·Al 2 o 3 The catalyst bed is subjected...
Embodiment 2
[0036] The present embodiment adopts the same experimental method and steps as in Example 1, the difference is:
[0037] The feed ratio of biomass (rice husk) and plastic waste (polyvinyl chloride) is biomass: plastics=10:1;
[0038] Biomass pyrolysis reaction conditions are 350°C and normal pressure;
[0039] The pyrolysis reaction conditions of plastic waste are 900°C and 10MPa;
[0040] The primary catalytic cracking reaction of biomass pyrolysis products uses Fe 2 o 3 Based on a super strong solid acid catalyst, the reaction conditions are 300 ° C, normal pressure, catalyst: biomass = 10:1;
[0041] One-stage catalytic cracking reaction of plastic waste pyrolysis products using γ-Al 2 o 3 Catalyst, the reaction conditions are 700°C, 10Mpa, catalyst: plastic waste = 1:10;
[0042] The reaction condition of the secondary shape-selective catalytic reaction of the mixture of the primary catalytic cracking product of biomass and the pyrolysis product of primary cracking o...
Embodiment 3
[0044] The present embodiment adopts the same experimental method and steps as in Example 1, the difference is:
[0045] The feed ratio of biomass (wood chips) to plastic waste (polystyrene) is biomass: plastic = 1:1;
[0046] Biomass pyrolysis reaction conditions are 550°C, 5MPa;
[0047] The pyrolysis reaction conditions of plastic waste are 550°C and 5MPa;
[0048] The primary catalytic cracking reaction of biomass pyrolysis products uses SiO 2 ·Al 2 o 3 Catalyst, the reaction conditions are 550°C, 5MPa, catalyst: biomass = 1:1;
[0049] The primary catalytic cracking reaction of plastic waste pyrolysis products uses CaO catalyst, the reaction conditions are 550 ° C, 5 MPa, catalyst: plastic waste pyrolysis products = 1:1;
[0050] The reaction condition of the secondary shape-selective catalytic reaction of the mixture of the primary catalytic cracking product of biomass and the primary catalytic cracking product of plastic is 550° C., 5 MPa, catalyst: (biomass + plas...
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