Method of using renewable raw materials to prepare jet fuel
A jet fuel and renewable raw material technology, applied in the preparation of biological raw materials, liquid hydrocarbon mixtures, petroleum industry, etc., can solve the problems of low yield of jet fuel, small freezing point depression, etc., to reduce freezing point, reduce reaction load, hydrogen consumption reduction effect
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Embodiment 1
[0053] The raw material oil is Chinese tallow tree oil, and its properties are shown in Table 1. By adopting the method provided by the present invention, the palm oil successively passes through the hydrotreating reaction zone, the hydroisomerization depressing zone A zone, the hydroisomerization depressing zone B zone and the hydrofining reaction zone to react to obtain the hydrofining reaction product, wherein, taking Chinese tallow oil as a benchmark, the mass content of water entering the hydrotreating reaction zone is 8%, and in the hydroisomerization depreciation reaction zone, the A zone and the B zone The catalyst loading ratio is 1:1. After the gas-liquid separation of the hydrofining reaction product, its liquid phase flow enters the distillation zone, and jet fuel and solvent oil are obtained after fractional distillation.
[0054] The hydrogenation reaction conditions are shown in Table 2, and the product distribution and properties are shown in Table 3 and Table ...
Embodiment 2
[0056] Jatropha oil is used as raw material oil, and its properties are shown in Table 1. By adopting the method provided by the present invention, waste catering oil is sequentially passed through the hydrotreating reaction zone, hydroisomerization depressing zone A, hydroisomerization depreciation zone B and hydrogenation The reaction is carried out in the refining reaction zone to obtain a hydrofining reaction product. Among them, based on jatropha oil, the mass content of water entering the hydrotreatment reaction zone is 6%, and in the hydroisomerization decondensation reaction zone, the catalyst loading ratio of zone A and zone B is 1:1. After the gas-liquid separation of the hydrofining reaction product, its liquid phase flow enters the distillation zone, and jet fuel and solvent oil are obtained after fractional distillation.
[0057] The hydrogenation reaction conditions are shown in Table 2, and the product distribution and properties are shown in Table 3 and Table 4. ...
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