Method for modification by coupling hydrodesulfurization of FCC (Fluid Catalytic Cracking) gasoline and aromatization of liquefied petroleum gas

A gasoline hydrogenation and hydrodesulfurization technology, applied in hydrotreating process, petroleum industry, processing hydrocarbon oil, etc., can solve the problems of difficult gasoline cleaning, lower gasoline octane number, high catalyzed gasoline sulfur and high olefin content , to achieve the effect of increasing the product octane number without loss, increasing gasoline yield, and high gasoline desulfurization rate

Inactive Publication Date: 2013-09-11
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI +1
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Problems solved by technology

Olefins in FCC gasoline contribute a lot to the octane number of gasoline. In order to meet China IV and Euro V standards for clean gasoline, further hydrodesulfurization is required to reduce the content of sulfur and olefins in gasoline. The biggest problem in this process is the deep desulfurization process. Olefins are easily hydrogenated and saturated into alkanes, resulting in a significant drop in the octane number of gasoline
In particular, the high ratio of catalytic cracking and slag in my country's local refineries leads to high sulfur and olefin content in catalytic gasoline, making it difficult to clean gasoline
Traditional hydrorefining technology is difficult to meet its cleaning upgrade requirements
[0004] In recent years, some catalytic gasoline selective hydrodesulfurization technologies have been developed at home and abroad, such as Prime-G, Prime-GW and related gasoline hydrodesulfurization technologies of domestic scientific research institutes. In the application of gasoline hydrofinishing, there are disadvantages of rapid catalyst deactivation, high olefin saturation rate, and large loss of gasoline octane number

Method used

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  • Method for modification by coupling hydrodesulfurization of FCC (Fluid Catalytic Cracking) gasoline and aromatization of liquefied petroleum gas
  • Method for modification by coupling hydrodesulfurization of FCC (Fluid Catalytic Cracking) gasoline and aromatization of liquefied petroleum gas
  • Method for modification by coupling hydrodesulfurization of FCC (Fluid Catalytic Cracking) gasoline and aromatization of liquefied petroleum gas

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Experimental program
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Effect test

Embodiment 1

[0028] Adopt the method provided by the present invention, take FCC gasoline 1 in Table 2 as raw material, first introduce whole cut FCC gasoline 1 into selective hydrogenation reactor and pre-desulfurization reactor to react, and the diolefins in the raw material are reduced from 1.5v% To below 0.5v%, the total sulfur content is reduced from 1250μg / g to 745μg / g, and the olefin saturation is less than 3%, and then the pre-desulfurized product enters the separator-fractionation tower combination device, with 75°C as the fractionation point, LCN:HCN The weight ratio is 40:60, the total sulfur of the fractionated LCN light component is 45.5 μg / g, the fractionated HCN heavy component has a total sulfur of 1405.2 μg / g, and the total sulfur of the HCN heavy component is reduced to 38.4 μg after hydrodesulfurization treatment / g, after reconciling with LCN light components, the total sulfur is 42.6μg / g, olefins are reduced from 38.5v% to 31.2v%, RON is reduced from 92.5 to 90.9, and t...

Embodiment 2

[0030] Using FCC gasoline 1 in Table 2 as the raw material, first introduce the full cut FCC gasoline 1 into the selective hydrogenation reactor and the pre-desulfurization reactor to reduce the dienes in the raw material from 1.5v% to below 0.5v%, and the total sulfur content Decrease from 1250μg / g to 685μg / g, olefin saturation is less than 5%, then the pre-desulfurization product enters the separator-fractionation tower combination device, with 80°C as the fractionation point, with LCN:HCN weight ratio of 45:55, fractionated out The total sulfur of the LCN light component is 42.8μg / g, the total sulfur of the HCN heavy component is 1326.5μg / g, and the total sulfur of the HCN heavy component is reduced to 44.5μg / g after hydrodesulfurization treatment, which is reconciled with the LCN light component The final total sulfur was 43.9 μg / g, olefins decreased from 38.5v% to 31.8v%, RON decreased from 92.5 to 91.0, and the loss was 1.5 units. The detailed data of reaction operating ...

Embodiment 3

[0032] Using the FCC gasoline 2 in Table 2 as the raw material, first introduce the full fraction FCC gasoline 2 into the selective hydrogenation reactor and the pre-desulfurization reactor, and reduce the diene content in the full fraction FCC gasoline 2 from 1.2v% to 0.45 after treatment. v%, the total sulfur content decreased from 412 μg / g to 281.4 μg / g, and the olefin saturation rate was less than 3%. Then the pre-desulfurization product is introduced into the separation-fractionation combined device, the fractionation point is selected as 75°C, the mass ratio of the fractionated LCN light component is 40%, the total sulfur content is 36.5 μg / g, and the mass ratio of the fractionated HCN heavy component is 60%. , the total sulfur content is 539.4μg / g, the total sulfur is reduced to 41.8μg / g after hydrogenation of heavy oil, and then the sulfur content is 39.4μg / g after reconciliation with LCN light components, and the olefin content is reduced from 39.4v% to 34.5v%, RON wi...

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Abstract

The invention provides a method for modification by coupling hydrodesulfurization of FCC (Fluid Catalytic Cracking) gasoline and aromatization of liquefied petroleum gas. All-fraction FCC gasoline is sequentially subjected to selective hydrogenation and preliminary desulfurization treatment to obtain HCN (Hydrogen Cyanide) heavy-component gasoline by fractionation, and the obtained HCN heavy-component gasoline is then subjected to hydrodesulfurization treatment; and the HCN heavy-component gasoline obtained from the hydrodesulfurization treatment and liquefied petroleum gas are co-fed into a fixed bed multi-stage aromatization reactor to recover/improve the octane number of a gasoline product through the processes of polymerization, pyrolysis, aromatization, hydrogen transfer and the like of olefin. The method is applied to the production process of ultra-low sulfur clean gasoline meeting national IV gasoline standard, and especially the ultra-low sulfur clean gasoline meeting national V gasoline standard. As a gradual desulfurization process is adopted, the operation conditions of all the units are mild, the desulfurization process is coupled with a liquefied petroleum gas aromatization process, and therefore the method has the characteristics that the gasoline desulfurization efficiency is high, the octane number loss of a product does not lose and is even increased, the gasoline yield is increased and the reaction process is flexible.

Description

technical field [0001] The invention belongs to the technical field of clean vehicle fuel production, and in particular relates to a method for coupled upgrading of FCC gasoline hydrodesulfurization-liquefied gas aromatization. Background technique [0002] With the rapid development of my country's economy, the demand for oil resources is increasing. In 2010, my country's oil demand reached 455 million tons, of which more than 250 million tons of crude oil and refined oil were imported. The shortage of oil resources has become a bottleneck restricting the sustainable development of my country's economy and society. In the next few decades, the most in short supply of petroleum downstream products will be vehicle transportation fuels, mainly gasoline and diesel (Contemporary Petroleum and Petrochemical, Vol. 17, No. 11, 2009, Countermeasures for the sustainable development of my country's oil refining and petrochemical industries) . [0003] With the increasing attention to...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G67/02C10G70/00
Inventor 朱向学黄岳寅安杰陈福存杜林徐龙伢杨军王玉忠陈孝
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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