Catalytic gasoline desulfurization method capable of satisfying maximum light gasoline etherification olefin reduction demands
A technology for catalyzing gasoline and light gasoline, applied in the petroleum industry, processing hydrocarbon oil, hydrocarbon oil treatment products, etc., can solve problems such as octane number loss, reduce steam consumption, reduce construction investment, and reduce cooling water consumption Effect
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Embodiment 1
[0038] A kind of catalytic gasoline desulfurization method, its flow process is as follows figure 1 As shown, the steps are as follows:
[0039] (1) The catalytic gasoline is pre-hydrogenated to saturate the diolefins in the gasoline, and the small molecular sulfides are converted into macromolecular sulfides, which enter the heavier gasoline components; the pre-hydrogenated gasoline enters the light cutting tower.
[0040] (2) In the light cutting tower, the gasoline light fraction with a boiling point less than 80°C is cut out from the top of the tower, that is, C 5 、C 6 Distillate; the gasoline fraction with a boiling point greater than 80°C at the bottom of the tower enters the cutting tower for further cutting.
[0041] (3) In the middle of the tower, the middle fraction of gasoline at 80 ° C to 150 ° C is cut from the top of the tower, that is, C 7 ~C 9 Distillate; the bottom of the tower obtains the gasoline heavy fraction with a boiling point greater than 150°C. ...
Embodiment 2
[0047] A kind of catalytic gasoline desulfurization method, its flow process is as follows figure 1 As shown, the steps are as follows:
[0048] (1) The catalytic gasoline is pre-hydrogenated to saturate the diolefins in the gasoline, and the small molecular sulfides are converted into macromolecular sulfides, which enter the heavier gasoline components; the pre-hydrogenated gasoline enters the light cutting tower.
[0049] (2) In the light cutting tower, the gasoline light fraction with a boiling point less than 80°C is cut out from the top of the tower, that is, C 5 、C 6 Distillate; the gasoline fraction with a boiling point greater than 80°C at the bottom of the tower enters the cutting tower for further cutting.
[0050] (3) In the middle of the tower, the middle fraction of gasoline at 80 ° C to 150 ° C is cut from the top of the tower, that is, C 7 ~C 9 Distillate; the bottom of the tower obtains the gasoline heavy fraction with a boiling point greater than 150°C. ...
Embodiment 3
[0056] A kind of catalytic gasoline desulfurization method, its flow process is as follows figure 1 As shown, the steps are as follows:
[0057] (1) The catalytic gasoline is pre-hydrogenated to saturate the diolefins in the gasoline, and the small molecular sulfides are converted into macromolecular sulfides, which enter the heavier gasoline components; the pre-hydrogenated gasoline enters the light cutting tower.
[0058] (2) In the light cutting tower, the gasoline light fraction with a boiling point less than 80°C is cut out from the top of the tower, that is, C 5 、C 6 Distillate; the gasoline fraction with a boiling point greater than 80°C at the bottom of the tower enters the cutting tower for further cutting.
[0059] (3) In the middle of the tower, the middle fraction of gasoline at 80 ° C to 130 ° C is cut from the top of the tower, that is, C 7 ~C 8 Distillate; the bottom of the tower gets the gasoline heavy fraction with a boiling point greater than 130°C.
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