Method for preparing renewable dodecanol and branched alkanes in an aviation kerosene range
A technology for aviation kerosene and branched-chain alkane, which is applied in the field of preparation of branched-chain alkanes in the range of renewable dodecanol and aviation kerosene, can solve the problem of high cost
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Embodiment 1-14
[0028] 1. Preparation of catalyst:
[0029] 1) Preparation of solid acid catalysts: Nafion and Amberlyst resins, Y-type molecular sieves, montmorillonite K-10 and KSF are commercial catalyst products purchased directly.
[0030] Phosphorylated zirconium oxide (ZrP) catalyst is mixed with 1mol / L zirconium oxychloride and ammonium dihydrogen phosphate aqueous solution at a volume ratio of 2:1, and the obtained precipitate is washed and filtered repeatedly, dried at 120°C for 10 hours, and then placed in Calcined at 400°C for 4h.
[0031] 2) Preparation of solid base catalysts: alkaline earth oxides (MgO, CaO, SrO) and rare earth oxides (La 2 o 3 , CeO 2 ) respectively by the corresponding nitrate in N 2 Calcined under atmosphere for 8h.
[0032] Magnesium aluminum hydrotalcite is the mass of 0.093mol Mg(NO 3 ) 2 ·6H 2 O and 0.0465mol Al(NO 3 ) 3 9H 2 O is dissolved in 100ml of water, and the solution is mixed with 0.219mol NaOH and 0.0565mol NaOH in a water bath at 70...
Embodiment 13
[0043] Sedimentation and precipitation method: Prepare 0.0175M nickel nitrate solution and divide it into two parts A and B in equal volume. Add silica, H-ZSM-5, H-MOR, silicon-aluminum composite carrier, H-β molecular sieve, oxidation One kind of aluminum and an appropriate amount of concentrated nitric acid, 0.0525M urea was added to B, B was slowly added dropwise to A in a water bath at 80°C, the temperature was raised to 90°C, stirred for 10 hours, filtered and washed, dried overnight at 80°C, and air roasted at 500°C for 2 hours. The calcined catalyst was reduced in situ with hydrogen at 500 °C for 2 h in a fixed bed. (See Table 1, Examples 14-16, 16A, 16B)
[0044] Table 1 Supported metal A / X type bifunctional catalyst
[0045]
[0046]
[0047] 2 Self-condensation reaction: In a fixed-bed reactor, put 1.0g of catalyst into the reaction tube, keep the hydrogen pressure in the reactor at 0.6MPa, and the hydrogen flow rate at 150mL / min. mL / min was pumped into the r...
Embodiment 36-41
[0055] Taking palladium-doped magnesium aluminum hydrotalcite (Pd-MgAl-HT) as an example, the optimization of reaction conditions was explored.
[0056] 1) The effect of palladium / magnesium molar ratio on the yield of propylidene acetone self-condensation reaction
[0057] The influence of table 4 catalyst mass fraction on product yield
[0058]
[0059]
[0060] As can be seen from Table 4, when the palladium / magnesium mol ratio is 0.02, the total product yield is the highest.
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