Preparation method for environment-friendly fuel from hydrodesulfurized residue oil
A hydrodesulfurization and environment-friendly technology, which is applied in the preparation of environmentally friendly fuels and the field of hydrodesulfurization residue, can solve the problems of low added value, low utilization rate of petrochemical by-products, energy waste, etc., and achieve short production cycle, The effect of wide application range and low cost
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Embodiment 1
[0013] (1) Utilize the fixed-bed residual oil hydrotreating device to carry out residual oil hydrodesulfurization, the carrier is alumina, under the catalysis of 1% by weight of metal oxide NiO, CoO, the hydrogen partial pressure is at 10MPa, and the reaction temperature is at 300 °C; the reaction time is 6 hours to obtain the residual oil after hydrodesulfurization;
[0014] (2) Separate the modified residual oil obtained in step (1) into a rapid stirring reactor, the content of the residual oil is 50 parts by weight as the main raw material, raise the temperature of the reactor to 90 ° C, stir rapidly, and pour it into the reactor Add 20 parts by weight of hydrocarbon ethylene glycol dimethyl ether with small molecular weight as a igniter, then add 0.1 parts by weight of OPE-4 as an emulsifier and 0.5 parts by weight of sodium stearate as a stabilizer, and the balance is water , high-speed stirring and mixing for 8 hours, and cooling to obtain residual fuel oil.
Embodiment 2
[0016] (1) Utilize the fixed-bed residual oil hydrotreating device to carry out residual oil hydrodesulfurization, the carrier is alumina, under the catalysis of 1% by weight of metal oxide NiO, CoO, the hydrogen partial pressure is at 15MPa, and the reaction temperature is at 350 °C; the reaction time is 6 hours to obtain the residual oil after hydrodesulfurization;
[0017] (2) Separate the modified residual oil obtained in step (1) into a rapid stirring reactor, the content of the residual oil is 60 parts by weight as the main raw material, raise the temperature of the reactor to 90°C, stir rapidly, and pour it into the reactor Add 20 parts by weight of hydrocarbon ethylene glycol dimethyl ether with small molecular weight as a igniter, then add 0.1 parts by weight of OPE-4 as an emulsifier and 0.5 parts by weight of sodium stearate as a stabilizer, and the balance is water , high-speed stirring and mixing for 8 hours, and cooling to obtain residual fuel oil.
Embodiment 3
[0019] (1) Utilize the fixed-bed residual oil hydrotreating device to carry out residual oil hydrodesulfurization, the carrier is aluminum oxide, 1% by weight of metal oxide NiO, CoO, MoO Under the catalysis, the hydrogen partial pressure is at 15MPa, and the reaction temperature At about 350°C; the reaction time is 6 hours to obtain the residual oil after hydrodesulfurization;
[0020] (2) Separate the modified residual oil obtained in step (1) into a rapid stirring reactor, the content of the residual oil is 60 parts by weight as the main raw material, raise the temperature of the reactor to 90°C, stir rapidly, and pour it into the reactor Add 20 parts by weight of hydrocarbon ethylene glycol dimethyl ether with a small molecular weight as a igniter, then add 0.5 parts by weight of NPE50 as an emulsifier and 0.5 parts by weight of sodium stearate as a stabilizer, and the balance is water. Stir and mix for 8 hours, then cool to obtain residual fuel oil.
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