Method for producing low-sulfur gasoline by non-hydroforming sulfur and alcohol removal

A non-hydrogen sweetening and sweetening technology, which is applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process, etc., can solve the problem of reducing the total sulfur of the product, so as to improve the stripping effect and avoid the loss of octane number of the product , the effect of improving the reaction speed

Active Publication Date: 2012-05-09
CHINA PETROLEUM & CHEM CORP +1
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  • Claims
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Problems solved by technology

These macromolecular mercaptans are stable in nature. The traditional Merox catalytic oxidation of mercaptans can only convert mercaptans into disulfides to reduce the sulfur content of mercaptans, but the total sulfur of the product has not been reduced.

Method used

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  • Method for producing low-sulfur gasoline by non-hydroforming sulfur and alcohol removal
  • Method for producing low-sulfur gasoline by non-hydroforming sulfur and alcohol removal
  • Method for producing low-sulfur gasoline by non-hydroforming sulfur and alcohol removal

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Embodiment

[0041] The processes of gasoline fractionation and heavy gasoline fraction hydrodesulfurization are the same as in Comparative Example 1. The stripping tower is used as a countercurrent reactor, and the configuration is based on the stripping tower in Comparative Example 2, and a Φ3mm Raschig ceramic ring filler is filled above the feed section. The heavy gasoline product after hydrogenation is introduced into the stripping tower, the feed rate of the device is 500 g / h, the operating pressure of the stripping tower is 1.4Mpa, nitrogen is fed into the bottom of the tower as an additional stripping medium, and the feed rate of nitrogen is 3L / h. The average temperature of the catalyst bed below the feed is 240°C, and the temperature of the tower bottom is 280°C. The top product of the stripping tower is partially refluxed, with a reflux ratio of 0.3, and partially discharged, with a discharge rate of 150 g / h. The properties of the product after sweetening are shown in Table 2. ...

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Abstract

The invention relates to a method for producing low-sulfur gasoline by non-hydroforming sulfur and alcohol removal, which comprises the following steps that: (1) gasoline raw materials are fractionated into light and heavy gasoline fractions, the light gasoline fractions are subjected to alkali washing sulfur and alcohol removal, and the heavy gasoline fractions are subjected to hydrogen desulfurization; and (2) the heavy gasoline fractions after the hydrogen desulfurization are introduced into a counter flow contact reactor, sulfur and alcohol removal catalysts are filled in positions under a material inlet of the reactor, steam stripping media which do not contain hydrogen gas are introduced into the bottom of the reactor, liquid phase ingredients of the heavy gasoline fractions in the counter flow reactor are in counter flow contact with the steam stripping media, the regeneration sulfur and alcohol in the materials are decomposed into olefin and hydrogen sulphide on catalysts, the heavy gasoline heavy ingredients after the sulfur and alcohol removal flow out from the tower bottom, heavy gasoline light ingredients, steam stripping media and hydrogen sulphide gas are discharged from the top of the reactor, the heavy gasoline light ingredients after the H2S removal, the heavy gasoline heavy ingredients after the sulfur and alcohol removal and the light gasoline fraction after the alkali washing are mixed to obtain the gasoline products. The gasoline product produced by adopting the method provided by the invention belongs to the gasoline product with the advantages that the sulfur and alcohol content is lower than 3mug/g, the sulfur content meets the Euro IV discharge standard, and in addition, the octane number loss is little.

Description

technical field [0001] The invention relates to a method for desulfurizing gasoline. More specifically, it is a method for reducing the sulfur content and mercaptan content in gasoline, especially reducing the regenerated mercaptan content in gasoline after hydrodesulfurization, and producing low-sulfur gasoline. Background technique [0002] As people's awareness of environmental protection continues to increase, the specifications of motor gasoline indicators such as oxygen content, vapor pressure, benzene content, total aromatics content, boiling point, olefin content and sulfur content will become more and more stringent, especially sulfur content. In 2008, Beijing took the lead in implementing the National IV gasoline standard, requiring the sulfur content to be less than 50 μg / g and the mercaptan content to be less than 10 μg / g. The content of total sulfur and mercaptan sulfur is also required to be further reduced. [0003] FCC gasoline in my country is the main ble...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G67/00
Inventor 毛俊义李明丰袁清张占柱褚阳屈锦华黄涛秦娅
Owner CHINA PETROLEUM & CHEM CORP
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