Method for reducing olefin sulfur content in gasoline
A technology of sulfur content and gasoline, applied in the petroleum industry, processing hydrocarbon oil, hydrotreating process, etc., can solve problems such as difficulty in meeting the requirements of gasoline quality, decrease in gasoline octane number, etc., and achieve no loss of gasoline octane number. , The effect of reducing total hydrogen consumption and high liquid yield
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[0035] This example gives the reaction conditions and reaction results of a medium-scale test of 100,000 tons / year of catalytic cracking gasoline heavy fraction. In this embodiment, the front hydrogenation reaction system and the rear dehydrogenation reaction system each have an independent hydrogen circulation system.
[0036] The research method of the whole distillate raw material of catalytic cracking gasoline has an octane number of 90.5, an olefin content of 50.3v%, a sulfur content of 130ppm, and a flow rate of 18657kg / h.
[0037] 1. Cutting of gasoline whole distillate raw materials
[0038] The light and heavy fraction cut point is 73°C, and the cut ratio is: light fraction 33.0% by weight, heavy fraction 67.0% by weight, then the flow rate of light fraction is 6157kg / h, and the flow rate of heavy fraction is 12500kg / h.
[0039] 2. Alkali washing treatment of light gasoline fraction
[0040] The sulfur content of the light gasoline fraction is 59ppm, and the mercapt...
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