Method for hydrotreating high-sulfur and high-metal residual oil
A hydrogenation treatment, high metal technology, applied in refining to remove heteroatoms, etc., can solve the problems of inability to process high metal content residue, short operation cycle, etc., to increase porosity, avoid activity decline, and slow down deactivation speed effect
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Embodiment 1
[0048] The residual oil hydrogenation unit of embodiment 1 comprises three reactors, an upflow reactor and two fixed bed reactors, the upflow reactor catalyst is filled in the upflow reactor, and the protective agent and The demetallization catalyst is filled with a desulfurization catalyst in the second fixed-bed reactor. Among them, the loading ratio of upflow reactor catalyst: protective agent: demetallization catalyst: desulfurization catalyst is 44:1.0:15:40, that is, the loading ratio of upflow reactor catalyst to fixed bed hydrogenation catalyst is 44:56.
[0049] The raw material oil A used in Example 1 is a mixture of vacuum residue, catalytic cracking decant oil and catalytic cracking heavy cycle oil, and the mass ratio of the three is 90:4:6 in sequence, and its properties are shown in Table 1. The raw material oil A is mixed with hydrogen and enters the residual oil hydrogenation unit for reaction. The reaction conditions are shown in Table 2, and the reaction prod...
Embodiment 2
[0051] The residual oil hydrogenation unit of embodiment 2 comprises three reactors, an upflow reactor and two fixed bed reactors, the upflow reactor catalyst is filled in the upflow reactor, and the protective agent and the protective agent are filled in the first fixed bed reactor The demetallization catalyst is filled with a desulfurization catalyst in the second fixed-bed reactor. The loading ratio of upflow reactor catalyst: protective agent: demetallization catalyst: desulfurization catalyst is 36:0.5:7.5:56, that is, the loading ratio of upflow reactor catalyst to fixed bed hydrogenation catalyst is 36:64.
[0052] The raw material oil B used in Example 2 is a mixture of vacuum residue, catalytic cracking decant oil and catalytic cracking heavy cycle oil, and the mass ratio of the three is 80:7:13 in turn, and its properties are shown in Table 1. The raw material oil B is mixed with hydrogen and enters the residual oil hydrogenation unit for reaction. The reaction condi...
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