A method for catalytically cracking vegetable asphalt to prepare bio-jet fuel
A plant asphalt and catalytic cracking technology, which is applied in the preparation of liquid hydrocarbon mixture, the treatment of multi-stage series refining and cracking process, waste fuel, etc. It can solve the problems of complex waste oil components, influence of catalyst activity, and catalyst coking. , to achieve the effect of low equipment requirements, reduced raw material costs, and strong adaptability
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Embodiment 1
[0028] A certain amount of magnesium nitrate, nickel nitrate, cerium nitrate (Mg / Ni / Ce molar ratio 3:2:0.5) and urea (2 times the amount of nitrate substance) were dissolved in deionized water, and added dropwise to In a stainless steel bottle, after the dissolution is complete, hydrothermally react at 120°C for 24 hours, let it stand and cool to room temperature, vacuum filter, wash the filter cake with deionized water until neutral to obtain a solid product, and mix the solid product and nano-ferric oxide by pressing After mixing evenly with a mass ratio of 100:5, a magnetically modified hydrotalcite catalyst was obtained after calcining at 400°C, which was recorded as magnetic Fe-Ce-LDO.
[0029] Mix plant asphalt and 1% magnetic catalyst evenly, then add it to the cracking reactor, set the furnace temperature to 450°C, and the nitrogen flow rate to 80mL / min, collect the cooled liquid after cracking, and heat up the obtained liquid to rectify. Collect products with fraction...
Embodiment 2
[0032] Dissolve a certain amount of magnesium nitrate, nickel nitrate and cerium nitrate (Mg / Ni / Ce molar ratio is 3:2:0.75) and urea (3 times the amount of nitrate substance) in water, and add it dropwise to the stainless steel bottle , hydrothermally reacting at 150°C for 15h, standing to cool to room temperature, vacuum filtering, washing the filter cake with deionized water until neutral to obtain a solid product, and combining the solid product and nano-ferric oxide at a mass ratio of 100:7 After mixing evenly, a magnetically modified hydrotalcite catalyst was obtained after calcining at 300°C, which was recorded as magnetic Mg / Ni / Ce-LDO.
[0033] Mix plant asphalt and a certain amount of magnetic Mg / Ni / Ce-LDO evenly, the amount of magnetic Mg / Ni / Ce-LDO is 5%, and then pump it into the tubular cracking furnace, the furnace temperature is set at 500 °C, and the nitrogen flow rate The pyrolysis time is 80mL / min, and the pyrolysis time is 10 minutes. The product obtained from...
Embodiment 3
[0036] A certain amount of magnesium nitrate, nickel nitrate, cerium nitrate (Mg / Ni / Ce molar ratio 3:2:1) and urea (4 times the amount of nitrate substance) were dissolved in deionized water, and added dropwise to In a stainless steel bottle, after the dissolution is complete, hydrothermally react at 180°C for 18 hours, let stand and cool to room temperature, vacuum filter, wash the filter cake with deionized water until neutral to obtain a solid product, and combine the solid product and nano-ferric oxide by pressing After mixing evenly with a mass ratio of 100:10, a magnetically modified hydrotalcite catalyst was obtained after calcining at 350°C, which was recorded as magnetic Mg / Ni / Ce-LDO.
[0037] Mix plant asphalt and a certain amount of magnetic Mg / Ni / Ce-LDO evenly, the amount of magnetic Mg / Ni / Ce-LDO is 8%, and then pump it into the tubular cracking furnace, the furnace temperature is set at 600 °C, and the nitrogen flow rate The pyrolysis time is 80mL / min, and the pyr...
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