Device and method for directionally depolymerizing biomass and converting biomass into aviation oil cycloalkane component
A technology of oil cycloalkane and biomass, which is applied in the field of biomass resource utilization, can solve problems such as increased difficulty, and achieve the effects of directional production, increased yield, and extended service life
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Embodiment 1
[0037] The invention provides a device and method for directional depolymerization and conversion of biomass into naphthenic components of aviation oil. The method uses biomass as raw material to produce C6-C8 low-carbon aromatics through pyrolysis and catalytic reforming, C8-C15 aromatics are prepared by alkylation of C6-C8 low-carbon aromatics, and aviation fuel is directly produced by hydrogenation and saturation of C8-C15 aromatics. range of naphthenic components.
[0038] Such as figure 1As shown, the device consists of five systems, including biomass directional depolymerization reaction system, aromatics alkylation system, hydrogenation saturation reaction system, rectification system and waste heat recovery and utilization system. The above five systems are connected with each other and together constitute a device for directional depolymerization of biomass and conversion into naphthenic components of aviation oil.
[0039] Biomass directional depolymerization react...
Embodiment 2
[0046] This example provides a method for directional depolymerization of biomass and conversion into naphthenic components of aviation oil, including:
[0047] Step 1: directional depolymerization of biomass into C6-C8 low-carbon aromatics;
[0048] In one embodiment, the biomass raw material is Chinese fir particles with an initial moisture content of 15%, and the dried biomass is added from the bottom of the fluidized bed, and rapidly pyrolyzed under normal pressure and 500-600°C to obtain oxygen-containing Compound high-temperature steam and solid coke; high-temperature steam and solid coke enter the cyclone separator, and the coke stays in the cyclone separator; high-temperature steam enters the fixed bed, and the reforming reaction occurs under normal pressure, catalyst, and 500~800 ° C conditions, the catalyst HZSM-5 or CaO / HZSM-5 molecular sieve is used; the product after catalytic reforming enters the condenser to condense the C6-C8 low-carbon aromatics; the non-conde...
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