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Method for producing low-sulfur gasoline

A technology for gasoline and gasoline fractions, which is applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process, etc., can solve the problem of not being able to completely suppress the regeneration of mercaptans, etc. The effect of no loss of value

Active Publication Date: 2013-06-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Removal of H 2 S can reduce the H in the subsequent hydrodesulfurization reactor 2 S concentration, but the hydrodesulfurization reaction will still produce new H 2 S, cannot completely inhibit the formation of regenerated mercaptans

Method used

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  • Method for producing low-sulfur gasoline

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] (1) The hydrodesulfurization process of gasoline fraction is the same as that of Comparative Example 1.

[0035] (2) After the hydrogenation, the gasoline product 1 enters the stripping tower filled with the sweetening catalyst RSS-1A, and in the absence of hydrogen, catalytic sweetening is carried out. The operating pressure of the stripping tower is 0.8Mpa, and no stripping medium is added. The average temperature of the catalyst bed below the feed is 180° C., and the feed rate is 500 g / hour. The non-hydrodemercaptan product A1 is drawn from the bottom of the tower, and its properties are shown in Table 2.

[0036] The diameter of the stripping tower used for sulfur removal is Φ32mm and the height is 4m. Packing with a height of 1m above the feed inlet, and 0.5m high below the feed inlet, and sweetening catalyst RSS-1A in the bottom 2.5m of the stripping tower. The shape of the catalyst is a Φ3mm Raschig ring. The catalyst RSS-1A is produced by Sinopec Catalyst Chan...

Embodiment 2

[0051] (1) Same as Comparative Example 2, the fractional distillation of catalytic cracking full fraction gasoline is used to obtain gasoline light fraction and gasoline heavy fraction, and the cut point is 65°C. The cut gasoline light fraction is eluted with alkali to remove mercaptans.

[0052] (2) Same as in step (2) of Comparative Example 2, the gasoline heavy fraction is hydrodesulfurized to obtain the hydrodesulfurized gasoline heavy fraction.

[0053] (3) The heavy fraction of hydrodesulfurized gasoline enters the stripper filled with sweetening catalyst RSS-1A, and undergoes sweetening reaction in the absence of hydrogen to obtain sweetened gasoline heavy fraction A2, whose properties are shown in Table 3. The configuration of the stripper is the same as in Example 1. The operating pressure of the stripper is 1.3 MPa, the average temperature of the catalyst bed below the feed is 220° C., and the feed rate is 600 g / hour.

[0054] (4) The gasoline heavy fraction A2 aft...

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Abstract

The invention discloses a method for producing low-sulfur gasoline, which comprises: (1) introducing a gasoline raw material into a hydrogenation reactor and allowing the gasoline raw material to contact hydrogenation and desulfuration catalysts in the presence of hydrogen and undergo hydrogenation and desulfuration, separating the products of the reactions, and obtaining a hydrogen-rich gas and a gasoline fraction obtained after hydrogenation and desulfuration; and (2) introducing the gasoline fraction obtained after hydrogenation and desulfuration to a reverse flow reactor filled with a sweetening catalyst and allowing the gasoline fraction to pass through a catalyst bed layer from top down and contact with a steam stripping medium introduced from the bottom of the reactor in a reverse flow manner, wherein the regenerated mercaptan in the gasoline fraction discomposes into olefin and hydrogen sulfide on the catalyst, the hydrogen sulfide and light dydrocarbon in the fluid are transferred out of the reaction area with the steam stripping medium, the steam stripping medium which contains the hydrogen sulfide and light dydrocarbon is discharged from the upper part of the reverse flow reactor, and the gasoline product from which the mercaptan is removed is obtained from the bottom of the reactor. When the method provided by the method is used, the gasoline product of which the mercaptan sulfur content is lower than 3mu g / g can be produced, the total sulfur content of the gasoline product is reduced, and the octane number loss is small.

Description

technical field [0001] The present invention relates to a method of desulfurizing gasoline and, more particularly, to a method of refining gasoline using at least one hydrotreating process and at least one only in the absence of hydrogen. Background technique [0002] With the increasingly stringent environmental protection regulations, countries around the world have put forward stricter restrictions on the composition of engine fuels such as sulfur content, vapor pressure, benzene content, total aromatics content, and olefin content, among which the sulfur content in gasoline is particularly strict. my country plans to upgrade the quality of motor gasoline to the National III standard on December 31, 2009, requiring that the sulfur content of gasoline should not exceed 150 μg / g. Beijing has taken the lead in implementing the National IV emission standard in 2008, requiring the sulfur content of gasoline to be further reduced to below 50 μg / g. [0003] FCC gasoline is the ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G67/02
Inventor 李明丰毛俊义张占柱黄涛褚阳
Owner CHINA PETROLEUM & CHEM CORP
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