Coal tar and residual oil combined treatment process
A treatment process, coal tar technology, applied in hydroprocessing process, petroleum industry, hydrocarbon oil treatment, etc., can solve problems such as low liquid yield, easy blockage of filter, incomplete removal of catalyst powder, etc.
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Embodiment 1
[0052] Embodiment 1 uses residual oil and coal tar whole distillate as raw materials, adopts coal tar and residual oil combined treatment process of the present invention, and residual oil and coal tar heavy fraction enters the first hydroprocessing unit (the first hydroprocessing unit adopts fixed bed Reactor), hydrogenation reaction is carried out in the presence of hydrogen and the first hydrotreating catalyst; the liquid phase effluent obtained after the reaction directly enters the catalytic cracking unit without fractionation, and the reaction product is separated to obtain dry gas, liquefied gas, catalytic Gasoline, catalytic diesel, catalytic heavy cycle oil and catalytic oil slurry; the catalytic oil slurry is firstly mixed with the first additive coal tar distillate oil, the ratio of catalytic oil slurry to the first additive is 19:1, and the catalytic oil slurry and the second additive The mixing treatment temperature and mixing treatment time of the first auxiliary ...
Embodiment 2
[0054] Embodiment 2 uses residual oil and coal tar whole distillate as raw materials, adopts coal tar and residual oil combined treatment process of the present invention, and residual oil and coal tar heavy fraction enters the first hydroprocessing unit (the first hydroprocessing unit adopts fixed bed Reactor), hydrogenation reaction is carried out in the presence of hydrogen and the first hydrotreating catalyst; the liquid phase effluent obtained after the reaction directly enters the catalytic cracking unit without fractionation, and the reaction product is separated to obtain dry gas, liquefied gas, catalytic Gasoline, catalytic diesel, catalytic heavy cycle oil and catalytic oil slurry; catalytic oil slurry is first mixed with the first additive coal tar distillate and the second additive decahydronaphthalene, and the catalytic oil slurry is mixed with the first additive and the second additive The ratios are 20:1 and 70:1 respectively, the mixing treatment temperature and...
Embodiment 3
[0056] Embodiment 3 uses residual oil and coal tar whole distillate as raw materials, adopts coal tar and residual oil combined treatment process of the present invention, and residual oil and coal tar heavy fraction enters the first hydroprocessing unit (the first hydroprocessing unit adopts fixed bed Reactor), hydrogenation reaction is carried out in the presence of hydrogen and the first hydrotreating catalyst; the liquid phase effluent obtained after the reaction directly enters the catalytic cracking unit without fractionation, and the reaction product is separated to obtain dry gas, liquefied gas, catalytic Gasoline, catalytic diesel oil, catalytic heavy cycle oil and catalytic oil slurry; the catalytic oil slurry is mixed with the first additive coal tar distillate oil, the ratio of catalytic oil slurry to the first additive is 21:1, and the catalytic oil slurry and the second additive The mixing treatment temperature and mixing treatment time of the first auxiliary agen...
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