Preparation method of castor-oil plant based biological aircraft fuel
An aviation fuel and castor-based technology, which is applied in the field of bio-aviation fuel preparation, can solve problems such as no bio-aviation fuel, and achieve the effects of stable source of raw materials, excellent performance at low temperature and high product quality.
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Embodiment 1
[0022] In a fixed bed reactor, with Ni-Mo / Al 2 o 3 As a catalyst, the raw material castor oil is subjected to hydrodeoxygenation reaction. The reaction temperature is controlled at 340°C-360°C, the pressure is 2-4MPa, the LHSV is 1.0-1.5 / h, and the hydrogen-oil ratio is 600 Nm 3 / m 3 . After the reaction, the liquid product was collected in a sample bottle.
[0023] In a fixed-bed reactor, Pt / SAPO-11 was used as a catalyst to carry out hydroisomerization reaction on the hydrodeoxygenated liquid product, and the catalyst was reduced with hydrogen for 2 hours before use. The reaction temperature of the isomerization reaction is 384°C, the reaction pressure is 3MPa, the reaction volume space velocity is 3 / h, and the hydrogen-to-oil molar ratio is 12:1. After the reaction, the corresponding liquid product was collected.
[0024] The liquid product of hydroisomerization is fractionated, and the fraction between 200-300°C is taken as the final product.
[0025]
Embodiment 2
[0027] In a fixed bed reactor, with Ni / Al 2 o 3 As a catalyst, the raw material castor oil is subjected to hydrodeoxygenation reaction. The reaction temperature is controlled at 334°C-362°C, the pressure is 2.3-4.0MPa, the LHSV is 0.9-1.6 / h, and the hydrogen-oil ratio is 850 Nm 3 / m 3 . After the reaction, the liquid product was collected in a sample bottle.
[0028] In a fixed-bed reactor, Pd / ZSM-5 was used as a catalyst to carry out hydroisomerization reaction on the hydrodeoxygenated liquid product, and the catalyst was reduced with hydrogen for 2 hours before use. The reaction temperature of the isomerization reaction is 335°C, the reaction pressure is 3.9MPa, the reaction volume space velocity is 2.2 / h, and the hydrogen-to-oil molar ratio is 11.7:1. After the reaction, the corresponding liquid product was collected.
[0029] The hydroisomerized liquid product is distilled, and the fraction between 200-300°C is taken as the final product.
[0030]
Embodiment 3
[0032] In a fixed bed reactor, with Ni-Mo / Al 2 o 3 -MgAl 2 o 4 As a catalyst, the raw material castor oil is subjected to hydrodeoxygenation reaction. The reaction temperature is controlled at 346°C-380°C, the pressure is 2.1-3.9MPa, the LHSV is 0.6-1.0 / h, and the hydrogen-oil ratio is 950 Nm 3 / m 3 . After the reaction, the liquid product was collected in a sample bottle.
[0033] In a fixed-bed reactor, Pt / SAPO-41 was used as a catalyst to carry out hydroisomerization reaction on the hydrodeoxygenated liquid product, and the catalyst was reduced with hydrogen for 2 hours before use. The reaction temperature of the isomerization reaction is 340°C, the reaction pressure is 3.7MPa, the reaction volume space velocity is 2.2 / h, and the molar ratio of hydrogen to oil is 14.0:1. After the reaction, the corresponding liquid product was collected.
[0034] The hydroisomerized liquid product is distilled, and the fraction between 200-300°C is taken as the final product.
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