One-pot liquefaction process of biomass
A technology of biomass and biomass pretreatment, which is applied in the field of one-pot liquefaction of biomass, which can solve the problems of small amount of biomass transported by the pump, low yield of bio-oil, and unstable transportation, etc., to achieve smooth operation and transportation, volume reduction, and the effect of increasing the delivery volume
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Embodiment 1
[0042] A one-pot liquefaction process of biomass, comprising the steps of:
[0043] Biomass Pretreatment
[0044] Put the palm oil residue into the drier and dry at 80°C for 6h until the water content is lower than 2wt%, and then send it into the superfine pulverizer for primary crushing. The median particle size after primary crushing is 50 μm, and then the primary crushing The palm oil residue is sent to the plodder for compression extrusion molding at a temperature of 30 ° C and a pressure of 3 MPa, and then for secondary crushing. The median particle size after secondary crushing is 30 μm. After secondary crushing The bulk density of palm oil residue is 1600kg / m 3 ,spare.
[0045] Catalyst preparation
[0046] S1. After the biochar is acidified, a biochar carrier is obtained;
[0047] S2. Vibrating and grinding the oxide of Mo and the above-mentioned biomass carbon carrier to obtain the biomass carbon loaded with Mo oxide with a particle size of 400-500 μm, which is...
Embodiment 2
[0056] A one-pot liquefaction process of biomass, comprising the steps of:
[0057] Biomass Pretreatment
[0058] Send the linseed oil residue and peanut oil residue into a drier and dry at 110°C for 2 hours until the water content is lower than 2wt%, and then send them into an ultrafine pulverizer for primary crushing. The median particle size after primary crushing is 300 μm, and then The primary crushed linseed oil residue and peanut oil residue are sent to the plodder for compression extrusion molding at a temperature of 50°C and a pressure of 0.5 MPa, and then secondary crushing, the median particle size after secondary crushing is 50 μm , the bulk density of linseed oil residue and peanut oil residue after secondary crushing is 1400kg / m 3 ,spare.
[0059] Catalyst preparation
[0060] S1. After the biochar is acidified, a biochar carrier is obtained;
[0061] S2. After the oxides of W, the oxides of Fe and the above-mentioned biomass charcoal carrier are subjected...
Embodiment 3
[0070] A one-pot liquefaction process of biomass, comprising the steps of:
[0071] Biomass Pretreatment
[0072] Put saponin oil residue and rapeseed oil residue into a drier, dry at 90°C for 3 hours until the water content is lower than 2wt%, and then send them into an ultrafine pulverizer for primary crushing. The median particle size after primary crushing is 230 μm, Then the saponin oil residue and rapeseed oil residue after primary crushing are sent to a briquetting machine for compression extrusion molding at a temperature of 40°C and a pressure of 1.5MPa, and then secondary crushing is carried out. The particle size is 40μm, and the bulk density of saponin oil residue and rapeseed oil residue after secondary crushing is 1450kg / m 3 ,spare.
[0073] Preparation of biochar loaded with Mo oxide and Pd oxide
[0074] S1. After the biochar is acidified, a biochar carrier is obtained;
[0075] S2. Vibrating and grinding Mo oxides, Pd oxides, and the above-mentioned bio...
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