Oxidative desulfurization process with continuously regenerated desulfurizer
A technology of oxidative desulfurization and desulfurization agent, applied in the direction of chemical instruments and methods, separation of dispersed particles, separation methods, etc., can solve problems such as air, water environment and water source pollution, difficulty in waste solvent treatment, human and environmental hazards, etc., to avoid Large fluctuations, improved service life, and no secondary pollution
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Embodiment 1
[0039] Properties of desulfurizer: commercially available W701 type iron oxide desulfurizer, Φ3~5×(3~15)mm round bar shape, bulk density 0.8~0.9g / ml, average radial crushing strength / N cm -1 ≥50.
[0040] The distillation range of catalytic cracking diesel oil is 240~260°C; in the solid-liquid separator: the temperature for cooling and separating sulfur is 10°C.
Embodiment 2
[0044] Properties of desulfurizer: Prepare amorphous iron oxyhydroxide desulfurizer according to CN101898108A, containing 97wt% amorphous iron oxyhydroxide, spherical shape of Φ8~10mm, bulk density of 0.9~1.0g / ml, average crush resistance of particle points / N· Pieces ≥ 30.
[0045] The distillation range of catalytic cracking diesel oil is 260~280°C; in the solid-liquid separator: the temperature for cooling and separating sulfur is 8°C.
Embodiment 3
[0049] Desulfurizer properties: commercially available TC-22 zinc oxide desulfurizer, Φ4×(4~10)mm round bar shape, bulk density 0.9~1.1g / ml, average radial crushing strength / N cm -1 ≥40. The distillation range of catalytic cracking diesel oil is 300~330°C; in the solid-liquid separator: the temperature for cooling and separating sulfur is 10°C.
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