Gasoline hydrodesulfurization method

A technology for hydrodesulfurization and gasoline hydrogenation, which is applied in the field of removing sulfur impurities in gasoline and catalytically cracked gasoline, can solve the problems of reducing olefin saturation, not considering the distribution law of olefins and sulfides, and being unfavorable for further improving the desulfurization rate of products. , to achieve the effect of improving gasoline desulfurization rate and small loss of octane number

Active Publication Date: 2008-01-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the same catalyst is filled in the whole tower without considering the distribution of olefins and sulfides along the

Method used

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  • Gasoline hydrodesulfurization method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] The raw materials used, the processing capacity, and the reaction conditions are the same as those of the comparative example, except that a fractionation section is added to the feed port in the middle of the tower. The height of the fractionation section is 40 cm, and the fractionation section is filled with 25 grams of selective hydrogenation catalyst RGO-2 catalyst. The height of the bottom stripping section is 30cm. Both the rectification reaction zone and the stripping reaction zone are filled with RSDS-1 catalyst. The height of the rectification reaction zone is 220cm, and the height of the stripping reaction zone is 110cm. The properties of the products after desulfurization are shown in Table 3.

Embodiment 2

[0035] The raw materials used, processing capacity, reaction conditions, and catalyst loading position are the same as those in Example 1, except that the rectification reaction section is filled with RSDS-1 catalyst, and the stripping reaction section is loaded with high-activity hydrodesulfurization catalyst CH-18. The properties of the product after desulfurization are see table 2

[0036] Table 1

[0037] catalyst

CH-18

RGO-2

RSDS-1

WO 3 ,%

≮19.0

/

/

MoO 3 ,%

/

≮5.0

≮8.0

NiO,%

≮2.0

≮2.5

/

CoO,%

≮0.04

/

≮2.5

Specific surface, m 2 / g

≮130

≮170

≮250

Pore ​​volume, ml / g

≮0.27

≮0.50

≮0.35

[0038] * The percentages in the table are percentages by weight.

[0039] Table 2

[0040] raw material

sweetened light fraction

heavy fraction

Density, g / cm3

0.7157

0.6...

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Abstract

A method using the gasoline hydrogenation to desulfurize is provided, which is carried out in a catalytic distillation column. The catalytic distillation column is divided into a rectification process section, a fractionation section, a stripping reaction section and a stripping section from top from bottom. The preheated raw materials are led into the fractionation section and the hydrogen is led into the bottom of the stripping section; the lighter components fractionated from the fractionation section enter into the section and conduct hydrodesulfurization reaction with the hydrogen under the contact with hydrodesulfurization catalyst A; the discharge on the tower top gains the liquid after cooling and separating; one part of the discharge returns to the rectification process section as the overhead reflux and the other part works as the desulfurized products 1; the heavier components fractionated enter the stripping reaction section and conduct hydrodesulfurization reaction with the hydrogen under the contact with hydrodesulfurization catalyst B and is discharged from the reboiler on the tower bottom after the a stripping section further separates the H2S to work as the desulfurized products 2. The method provided by the invention can obviously improve the rate of the desulfurization of gasoline and have low loss of the octane number of the gasoline.

Description

technical field [0001] The invention relates to a method for hydrodesulfurization of petroleum hydrocarbons. More specifically, it is a method for removing sulfur impurities in gasoline, especially catalytically cracked gasoline, while minimizing the loss of gasoline octane number. Background technique [0002] With the rapid development of the automobile industry, the pollution of automobile exhaust to the environment is becoming more and more serious. The production of low-sulfur, low-olefin, and low-aromatic vehicle fuels has become a common goal pursued by people. Various countries have formulated new vehicle fuel standards one after another. The World Fuel Standard II and III gasoline standards require that the sulfur content in gasoline should be lower than 200ppm and 30ppm respectively. At present, 90-99% of the sulfur content of finished gasoline comes from FCC gasoline; therefore, reducing the sulfur content of FCC gasoline is the key to reducing the sulfur content...

Claims

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Application Information

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IPC IPC(8): C10G45/04
Inventor 毛俊义李明丰张占柱渠红亮夏国富黄涛褚阳
Owner CHINA PETROLEUM & CHEM CORP
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