Method and apparatus for catalytic modification of poor gasoline
A low-quality gasoline, catalytic upgrading technology, applied in catalytic cracking, cracking, petroleum industry and other directions, can solve the problems of complex process flow, high carbon content, poor stripping effect in stripping section, etc., and achieve strong operability. , reduce sulfur content, improve the effect of diesel-gasoline ratio
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Embodiment 1
[0027] in accordance with figure 1As shown in the inferior gasoline catalytic upgrading device of the present invention, Daqing atmospheric residual oil catalytic cracking gasoline is upgraded, and the catalytic cracking catalyst adopts LRC-99 industrial balancer. The riser catalytic raw material is pipe transport atmospheric residual oil, see Table 1 for the operating conditions; see Table 2 for the operating conditions of catalytic gasoline modified by the bed reactor to modify Daqing atmospheric residual oil, and see Table 2 for the properties of catalytic gasoline before and after upgrading in this embodiment. Table 3. The properties of gasoline after upgrading are calculated based on the properties of inferior gasoline before upgrading, and the properties of gasoline in catalytic cracking units before and after adding bed reactors or opening bed reactors through additive effects. The following examples of upgrading Post-gasoline properties are also obtained in this way. ...
Embodiment 2
[0028] The device, method, catalyst and raw materials are the same as in Example 1, except that the reaction temperature of the bed reactor is 460°C, and the operating conditions of the bed reactor for reforming Daqing atmospheric residue catalytic gasoline are shown in Table 2 , see Table 3 for the properties of the catalytic gasoline modified in this embodiment.
Embodiment 3
[0030] The device, method, catalyst and raw materials are the same as in Example 1, except that the reaction temperature of the bed reactor is 430°C, and the operating conditions of the reformed Daqing atmospheric residue catalytic gasoline by the bed reactor are shown in Table 2 , see Table 3 for the properties of the catalytic gasoline modified in this embodiment.
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