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Method for producing clean gasoline from catalytic cracking gasoline

A technology for catalytic cracking gasoline and catalytic cracking device, which is applied in the field of light hydrocarbon refining, can solve the problems of increasing the cooling load of the device, high energy consumption of the processing flow device, long production process route, etc., and achieves the effect of reducing the total sulfur content

Active Publication Date: 2015-04-15
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The production process route is longer, and the energy consumption of the processing equipment is higher
The heat of the catalytic cracking process is relatively rich, and is usually used to generate the steam required by the refinery, but most of the heat below 300 ° C cannot be fully utilized, and the cooling load of the device is also increased.

Method used

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  • Method for producing clean gasoline from catalytic cracking gasoline

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] according to figure 1 The process flow shown processes FCC catalytic cracking gasoline to produce ultra-low sulfur clean gasoline.

[0052] The naphtha after absorption and desorption in the FCC catalytic cracking absorption-stabilization unit is cut and separated in the stabilization tower to obtain light fractions and heavy fractions. The properties of the light and heavy fractions separated by the FCC catalytic cracking stabilization tower are shown in Table 1.

[0053] Table 1 Properties of light and heavy fractions separated by FCC catalytic cracking stabilizer

[0054] project light ends heavy fraction Density (20℃), g / cm 3 0.6875 0.7394 Sulfur content, μg / g 122 683 RON 95.2 92.6 Distillation range (ASTM D 86), °C IBP / 10% 30 / 35 79 / 110 30% / 50% 40 / 51 127 / 141 70% / 90% 59 / 63 157 / 188 95% / FBP 71 / 76 203 / 210

[0055] The light fraction enters the non-alkali deodorization unit to remove mercapta...

Embodiment 2

[0069] according to figure 1 The process flow shown is to process MIP catalytic cracking gasoline to produce ultra-low sulfur clean gasoline.

[0070] The naphtha after absorption and desorption in MIP catalytic cracking absorption-stabilization unit is cut and separated in the stabilization tower to obtain light fraction and heavy fraction. The properties of the light and heavy fractions separated by the MIP catalytic cracking stabilization tower are shown in Table 6.

[0071] Table 6 Properties of light and heavy fractions separated by MIP catalytic cracking stabilizer

[0072] project light ends heavy fraction Density (20℃), g / cm 3 0.6772 0.7375 Sulfur content, μg / g 118 680 Olefins, v% RON 95.6 92.8 Distillation range (ASTM D-86), ℃ IBP / 10% 30 / 35 80 / 109 30% / 50% 40 / 49 125 / 138 70% / 90% 57 / 62 153 / 185 95% / FBP 67 / 73 197 / 205

[0073] The light fraction enters the non-alkali deodorization uni...

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Abstract

The invention discloses a method for producing clean gasoline from catalytic cracking gasoline. The method comprises: leading a light fraction lateral line from a stabilization tower middle part of a catalytic cracking absorption-stabilization unit, and conducting light and heavy fraction cutting separation on crude gasoline to obtain light fractions and heavy fractions; subjecting light fractions to alkali-free deodorization, letting the deodorized light fractions and hydrocarbon-rich diesel oil from the absorption-stabilization unit enter a disulfide fractionating tower, thus obtaining light gasoline from the fractionating tower top and extracting medium gasoline from a fractionating tower middle lateral line, mixing the medium gasoline with the heavy fractions obtained at the stabilization tower bottom of the absorption-stabilization unit, then passing the mixture through a hydrogenation protection reactor and a hydrodesulfurization reactor in order, then subjecting the hydrogenated liquid product to gas stripping, and mixing the product with the refined light gasoline, thus obtaining a clean gasoline product or a blending component. The method provided in the invention not only can decrease the mercaptan sulfur content and the total sulfur content of catalytic cracking gasoline, produce a clean gasoline product with qualified sulfur and olefin content, but also can significantly reduce the energy consumption of production equipment and increase the economic benefits of a catalytic cracking gasoline desulfurization device.

Description

technical field [0001] The invention relates to a process for refining light hydrocarbons, more specifically a method for producing clean gasoline by catalytic cracking gasoline, especially a method for producing clean gasoline by reducing the mercaptan sulfur content of catalytic cracking gasoline. technical background [0002] With the rapid development of the automobile industry and increasingly stringent environmental protection requirements, the production of low-sulfur and ultra-low-sulfur clean gasoline has become an inevitable trend in the development of the oil refining industry. Judging from the composition of my country's current gasoline pool, catalytic cracking gasoline components account for 75% to 80%. The sulfur content of catalytic cracking gasoline is usually 100~2000μg / g, and the contribution rate to the sulfur content in the gasoline pool in my country is the highest, reaching more than 98%. Moreover, as the feedstock processed by catalytic cracking deve...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G67/00
Inventor 张龙关明华王海波齐慧敏李经伟王岩陈新刘志禹
Owner CHINA PETROLEUM & CHEM CORP