Catalyst carrier for preparing high-energy-density fuel as well as preparation method and application of catalyst carrier
A technology with high energy density and catalyst support, which is applied in the direction of catalyst support, catalyst activation/preparation, chemical instruments and methods, etc., can solve the problems of high specific surface area and single catalyst function, and achieve the improvement of hydrodeoxygenation performance and Effects of benzene ring saturation, increased added value, and high specific surface area
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Embodiment 1-9
[0065] Embodiment 1-9 provides a kind of Nb / ZrO respectively 2 Catalyst carrier and preparation method thereof, preparation method comprises the following steps,
[0066] (1) Mix zirconium nitrate, stabilizer and 100mL ethanol to form solution A; mix niobium oxalate and 100mL oxalic acid aqueous solution to form solution B; mix template agent and 100mL ethanol to form solution C;
[0067] (2) Add solution A and solution B dropwise to solution C at the same time to obtain a mixed solution, add ammonia water to the mixed solution to adjust the pH to 3-6, stir and react at 25°C, take it out, filter, and dry at 100°C 10h, and then calcined for 6h to obtain Nb-doped ZrO 2 Catalyst carrier, denoted as Nb / ZrO 2 .
[0068] The difference between Examples 1-9 lies in the molar concentration of zirconium ions in the mixed solution, the mass concentration of the stabilizer in the mixed solution, the molar concentration of niobium ions in the mixed solution, the mass concentration of t...
Embodiment 10-20
[0075] Embodiments 10-20 respectively provide a method for preparing high energy density fuel, comprising the following steps,
[0076] Disperse the lignin and catalyst in 100mL water, then place it in a 300mL autoclave, pour 0.5-5MPa of hydrogen into it, raise the temperature to 250-350°C, stir and react for 0.5-12h, after the reaction is over, filter and rotary steam Solvent removal yields high energy density fuels.
[0077] Among them, the difference between Examples 10-20 lies in the amount of lignin, catalyst amount, catalyst type, hydrogen pressure, reaction temperature, and reaction time. The process parameters in Examples 10-20 are shown in Table 2.
[0078] Process parameter in table 2 embodiment 10-20
[0079]
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