Selective hydrodesulfurization method for high-sulfur high-olefin catalytic gasoline

A technology for catalyzing gasoline and gasoline hydrogenation, which is applied in the treatment of hydrocarbon oil, hydrotreating process, petroleum industry, etc., can solve the problems of small loss of octane number, poor adaptability, single operation of fractionation unit, etc., and achieves loss of octane number. small effect

Inactive Publication Date: 2011-05-04
江苏佳誉信实业有限公司
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Problems solved by technology

However, due to the limited desulfurization effect of the deodorization unit, it has poor adaptability to local refineries with high sulfur content
[0010] In the prior art, the production of low-sulfur clean gasoline from FCC gasoline with high sulfur and high olefin content is difficult to solve in the following aspects: the contradiction between deep desulfurization and excessive loss ...

Method used

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  • Selective hydrodesulfurization method for high-sulfur high-olefin catalytic gasoline
  • Selective hydrodesulfurization method for high-sulfur high-olefin catalytic gasoline
  • Selective hydrodesulfurization method for high-sulfur high-olefin catalytic gasoline

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Embodiment

[0042] This example shows the desulfurization effect of a high-sulfur, high-olefin catalytic cracking gasoline, and those skilled in the art can formulate specific reaction conditions according to the properties of raw materials and product quality requirements.

[0043] The catalyst is an industrialized catalyst produced by Jiangsu Jiayuxin Company.

[0044] Table 1 Basic physicochemical properties of catalysts

[0045]

[0046] 1) Pre-hydrotreating of feedstock oil

[0047] The raw oil pre-hydrogenation section adopts JY-01 and JY-02 commercial catalysts produced by Jiangsu Jiayuxin Industrial Co., Ltd., and the two catalysts are respectively loaded in two reactors. The operating conditions are: hydrogen partial pressure of 2.0 Mpa, inlet reaction temperature 160°C, liquid hourly space velocity 9.0h -1 , the volume ratio of hydrogen to oil is 200, the operating conditions of the pre-desulfurization reaction are: 2.0Mpa, the inlet reaction temperature is 225°C, and the l...

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Abstract

The invention relates to a clean production method for high-sulfur high-olefin catalytic gasoline, which comprises the following steps of: performing selective hydrogenation on full fraction catalytically cracked gasoline in the presence of a gasoline hydrogenation pretreatment catalyst to remove active sulfide such as micro-molecular mercaptan, thioether, disulfide and the like, wherein the process conditions of the selective hydrogenation are that: hydrogen partial pressure is 1.5 to 3.0MPa, the reaction temperature is between 200 and 260 DEG C, liquid hourly space velocity is 6.0 to 12.5h<-1>, and the volume ratio of hydrogen to the gasoline is 150:1-500:1; performing fractionation segmentation on the gasoline subjected to the selective hydrogenation to form a light gasoline fraction and a heavy gasoline fraction, mixing the heavy gasoline fraction and the hydrogen, adding into a deep hydrodesulfurization unit and performing hydrofining in the presence of a gasoline hydrofining catalyst to obtain heavy fraction hydrogenated gasoline with low sulfur content, wherein the process conditions of the hydrofining are that: the hydrogen partial pressure is 1.5 to 2.5MPa, the reaction temperature is between 220 and 350 DEG C, the liquid hourly space velocity is 3.0 to 6.0h<-1>, and the volume ratio of the hydrogen to the gasoline is 200:1-500:1; and blending light fraction gasoline with the heavy fraction hydrogenated gasoline to obtain China IV clean gasoline.

Description

technical field [0001] The invention relates to a method for deep desulfurization of catalytic cracking gasoline to produce clean gasoline. Background technique [0002] In recent years, in order to protect the environment, countries around the world have put forward stricter restrictions on the composition of engine fuels in order to reduce environmental pollution caused by the emission of harmful substances. On July 1, 2007, the National III standard was officially implemented nationwide. However, until December 31, 2009, clean gasoline that meets the National III standard will be available nationwide. Although the National IV (sulfur content less than 50μg / g) standard is used in some cities, the existing gasoline production costs are too high, which is difficult for petrochemical companies and the market to accept. The backwardness of clean gasoline production technology has become a major obstacle to the upgrading of gasoline standards and market demand. Therefore, it ...

Claims

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Application Information

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IPC IPC(8): C10G67/00
Inventor 黄岳寅杜林孙祥杨军
Owner 江苏佳誉信实业有限公司
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