Alkali cleaning-extraction-hydrogenation combined process for producing low-sulfur-content gasoline
A technology of gasoline and alkali washing, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment, and can solve problems such as octane number loss
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Embodiment 1
[0021] Using FCC gasoline A as the raw material, first cut the raw material, the cutting point is 95°C, the heavy gasoline fraction accounts for 52% of the raw material, the gasoline raw material fraction (FCCN), light gasoline fraction (LCN), heavy gasoline fraction (HCN) The properties are shown in Table 1. The light gasoline fraction is first alkali-washed to remove mercaptans, and the alkali washing is conventional alkali washing (10% sodium hydroxide aqueous solution). After alkali washing, the mercaptan sulfur content in the light gasoline fraction is reduced to 15.3ug / g; The gasoline fraction enters the extraction and desulfurization unit to obtain the alkali washing-extraction light gasoline fraction and the extraction phase; the extraction agent is nitrogen-formylmorpholine, the solvent-oil ratio is 2:1, the number of extraction stages is 4, and the extraction temperature is 55°C. Remove thiophene, mercaptan, sulfide, and disulfide-like sulfides in light distillate ga...
Embodiment 2
[0029]Using FCC gasoline B as raw material, the light gasoline fraction is demercaptized by advanced alkali washing equipment, and the alkali washing is conventional alkali washing (10% sodium hydroxide aqueous solution), and the mercaptan sulfur content in gasoline is reduced to 22.5ug / g; The gasoline after alkali washing is cut, the cutting point is 100°C, and the light distillate gasoline is taken to investigate the desulfurization effect of the extractant. The solvent-to-oil ratio is 3:1, the number of extraction stages is 4, and the extraction temperature is 45°C to remove thiophene, mercaptan, sulfide, and disulfide-like sulfides in light fraction gasoline; the results are as follows: raw material light fraction sulfur The sulfur content is 332.4ug / g, and the sulfur content is reduced to 21.6ug / g after alkali washing and extraction, indicating that this process can produce gasoline with a sulfur content of less than 50ug / g and a sulfur content meeting the National IV stan...
Embodiment 3
[0031] The gasoline produced by catalytic cracking after hydrotreating of coker wax oil was used as raw material, the gasoline raw material was cut, and the cut point was 92°C, and the light distillate gasoline was taken to investigate the desulfurization effect of the extractant. The light gasoline fraction is demercaptanized by an advanced alkali washing device, and the alkali washing is conventional alkali washing (10% sodium hydroxide aqueous solution). After alkali washing, the mercaptan sulfur content in the light gasoline fraction is reduced to 4.2ug / g; The light gasoline fraction enters the extraction and desulfurization unit to obtain the alkali washing-extraction light gasoline fraction and the extraction phase. The extraction agent is nitrogen-formylmorpholine, the solvent-oil ratio is 2:1, the number of extraction stages is 4, and the extraction temperature is 38°C , Removal of thiophene, mercaptan, sulfide, and disulfide-like sulfides in light distillate gasoline. ...
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