A method and system for efficiently processing inferior gasoline
A low-quality gasoline and treatment method technology, which is applied in the direction of hydrocarbon oil treatment products, hydrocarbon oil treatment, hydrogenation treatment process, etc., can solve the problems such as inability to achieve desulfurization
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Embodiment 1
[0087] This embodiment provides a sulfur content of 625.3μg·g -1 , 35.6v% olefin content, 14.4v% aromatics content, 18.2v% isoparaffin content, 0.7v% benzene content of FCC gasoline (full distillate gasoline, feed oil 1) as raw material for the method of low-quality gasoline treatment.
[0088] Wherein, based on the total weight of each catalyst, the composition ratio of each catalyst is as follows:
[0089] Oriented sulfur transfer catalyst: 12wt.% NiO, 6wt.% MoO 3 , 2wt.% La 2 o 3 , 20wt.% stepped hole HZSM-5, 60wt.% Al 2 o 3 -SiO 2 (silicon-containing alumina);
[0090] Light gasoline alkylation catalyst: 60wt.% modified β zeolite, 10wt.% HY zeolite, 8wt.% kaolin, containing 19wt.% Al 2 o 3 , P 2 o 5 3wt.%;
[0091] Medium gasoline esterification catalyst: 50wt.% HZSM-5, 50wt.% Al 2 o 3 -SiO 2 (silicon-containing alumina);
[0092] Medium gasoline extraction solvent: 90wt.% sulfolane and 10wt.% tetraethylene glycol;
[0093] One-stage selective hydrodesulfuri...
Embodiment 2
[0131] This embodiment provides a method and system for efficiently treating low-quality gasoline by using the above-mentioned raw material oil 1 as a raw material.
[0132] Such as figure 2 As shown, the system of this embodiment is basically the same as that of Embodiment 1, except that the raffinate outlet of the extraction distillation system 105 is not connected to the reaction raw material inlet of the medium gasoline esterification reactor 110 but is directly connected to the The reaction raw material inlet of the hydrocarbon isomerization / aromatization reactor 109; that is, the system of this embodiment does not have the medium gasoline esterification reactor 110, the formic acid extraction system and the coalescence dehydrator 111, but the extraction distillation system The raffinate outlet of 105 is directly connected to the reaction raw material inlet of the hydrocarbon isomerization / aromatization reactor 109 through pipelines, and the rest are the same as the afor...
Embodiment 3
[0138] This embodiment provides a sulfur content of 1230.0μg·g -1, olefin content 42.3v%, aromatics content 20.3v%, isoparaffin content 20.2v%, benzene content 1.5v% high sulfur, high olefin, high benzene FCC gasoline (stock oil 2, its properties see Table 3) as raw material A method and system for efficient processing of inferior gasoline.
[0139] Such as image 3 As shown, the system of this embodiment is basically the same as that of Embodiment 1, only a debenzene tower 112 is set on the pipeline between the extraction oil outlet of the extraction distillation system 105 and the reaction material inlet of the first-stage hydrodesulfurization reactor 106, The outlet of the extracted oil after debenzene removal in the debenzene tower 112 is connected to the first-stage hydrodesulfurization reactor 106, and the rest are the same as in Example 1.
[0140] The method for processing raw oil 2 is as follows:
[0141] Compatible with the system of this example, on the basis of ...
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