Process for producing low oil wax and high viscosity index base oils
A high-viscosity, oil-containing wax technology, which is applied in the treatment of hydrocarbon oil, petroleum industry, hydrocarbon oil treatment products, etc., can solve the problems of poor economic benefit and low product yield
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Embodiment 1
[0070] This example is used to illustrate the method for producing low oil content wax and high viscosity index base oil from Fischer-Tropsch synthetic wax provided by the present invention.
[0071] The >350°C distillate of Fischer-Tropsch synthetic wax is used as the raw material, and the properties of the raw material are shown in Table 1.
[0072] See Table 2 for the solvent deoiling conditions, properties of the dewaxed oil and the underwax oil of the >350°C fraction of the Fischer-Tropsch synthetic wax.
[0073] At a deoiling filtration temperature, the ratio of the refractive index of the deoiling solvent to the refractive index of the mixture of the liquid components in the raw oil and the deoiling solvent at the filtration temperature is 0.97.
[0074] Table 3 shows the reaction conditions of the first hydrofinishing, hydroisomerization and second hydrofinishing of the underwax oil and the properties of the second hydrofinishing products.
[0075] Table 4 shows the p...
Embodiment 2
[0077] This example is used to illustrate the method for producing low oil content wax and high viscosity index base oil from Fischer-Tropsch synthetic wax provided by the present invention.
[0078] The 350°C-400°C fraction of Fischer-Tropsch synthetic wax is used as the raw material, and the properties of the raw material are shown in Table 1.
[0079] See Table 2 for the solvent deoiling conditions, properties of dewaxed oil and underwax oil of the 350°C-400°C fraction of Fischer-Tropsch synthetic wax.
[0080] At a deoiling filtration temperature, the ratio of the refractive index of the deoiling solvent to the refractive index of the mixture of the liquid components in the raw oil and the deoiling solvent at the filtration temperature is 0.995.
[0081] See Table 3 for the reaction conditions and base oil properties of the first hydrofinishing, hydroisomerization and second hydrofinishing of waxy oil.
Embodiment 3
[0083] This example is used to illustrate the method for producing low oil content wax and high viscosity index base oil from Fischer-Tropsch synthetic wax provided by the present invention.
[0084] The 400°C-450°C distillate of Fischer-Tropsch synthetic wax is used as the raw material, and the properties of the raw material are shown in Table 1.
[0085] See Table 2 for the solvent deoiling conditions, properties of dewaxed oil and underwax oil of the 400°C-450°C fraction of Fischer-Tropsch synthetic wax.
[0086] At a deoiling filtration temperature, the ratio of the refractive index of the deoiling solvent to the refractive index of the mixture of the liquid components in the raw oil and the deoiling solvent at the filtration temperature is 0.99.
[0087] See Table 3 for the reaction conditions and base oil properties of the first hydrofinishing, hydroisomerization and second hydrofinishing of waxy oil.
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