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Method for improving selectivity of catalyst

A catalyst and selective technology, applied in chemical instruments and methods, catalyst activation/preparation, catalyst regeneration/reactivation, etc., can solve problems such as economic uneconomical, achieve easy implementation, decrease olefin hydrogenation saturation activity, and improve selectivity sexual effect

Active Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, if the sulfur content of catalytic cracking gasoline is to be further reduced to less than 50 μg / g, the operating severity of the catalytic cracking raw material hydrogenation unit must be greatly increased, which is very uneconomical economically.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] Using fresh A and B catalysts, the loading volume ratio of A and B catalysts in the reactor is A:B=85:15. The catalysts A and B in the reactor are vulcanized. After the vulcanization is over, the gas in the reaction system is adjusted to be a catalytic gas. In the catalytic gas, the volume fraction of hydrogen is 80%, H 2 The volume fraction of S is 1.5%, and the catalytic raw material is introduced into the reaction system, and the hydrogen partial pressure is 1.6MPa under the catalytic condition; the hydrogen-oil ratio is 100Nm 3 / m 3 ;Volume space velocity 4.0h -1 ; After contacting with the catalyst for 48h under the condition of reaction temperature 360°C. The distillation range of the catalytic raw material is 30-350°C, wherein the volume fraction of olefins is 30%.

[0040] Then adjust to normal reaction conditions, switch the catalytic raw material to gasoline raw material, and switch the gas in the reactor to hydrogen-rich gas. Based on the whole hydrogen-ri...

Embodiment 2

[0043] Adopt fresh A catalyst to sulfide the A catalyst in the reactor. After the sulfidation is over, adjust the gas in the reaction system to be the catalyzing gas. In the catalyzing gas, the volume fraction of hydrogen is 82%, H 2 The volume fraction of S is 1.0%, the catalytic raw material is introduced into the reaction system, and the hydrogen partial pressure is 1.6MPa under the catalytic condition; the hydrogen-oil ratio is 200Nm 3 / m 3 ;Volume space velocity 4.0h -1 ; Contact with the catalyst for 48 hours at a reaction temperature of 350°C, the distillation range of the catalytic raw material is 30-350°C, wherein the volume fraction of olefins is 25%, and the volume fraction of aromatics is 30%.

[0044] Adjust to normal reaction conditions, switch the catalyzing raw material to gasoline raw material, switch the gas in the reactor to hydrogen-rich gas, take the hydrogen-rich gas as a whole as a benchmark, the volume fraction of hydrogen is 85%, and the volume fracti...

Embodiment 3

[0047] Using fresh A and B catalysts, the loading volume ratio of A and B catalysts in the reactor is A:B=85:15. The A and B catalysts in the reactor are vulcanized. After the vulcanization is over, the gas in the reaction system is adjusted to be the activating gas. In the catalyzing gas, the volume fraction of hydrogen is 85%, H 2 The volume fraction of S is 2.0%, the catalytic raw material is introduced into the reaction system, and the hydrogen partial pressure is 1.6MPa under the catalytic condition; the hydrogen-oil ratio is 100Nm 3 / m 3 ;Volume space velocity 4.0h -1 ; Contact the catalyst for 72 hours at a reaction temperature of 350°C, and the distillation range of the catalytic raw material is 30-350°C, wherein the volume fraction of olefins is 45%, and the volume fraction of aromatics is 25%.

[0048] Adjust to normal reaction conditions, switch the catalyst raw material to gasoline raw material, switch the gas in the reactor to hydrogen-rich gas, take the hydroge...

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PUM

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Abstract

The invention relates to a method for improving selectivity of a catalyst. A catalyst selectivity regulation and control process is increased between a desulfurization process and a normal production process, and the catalyst selectivity regulation and control process is that activity catalytic raw materials are in contact with the catalyst for 24-96h in an atmosphere of activity catalytic gas under activity catalytic reaction conditions, wherein the activity catalytic gas comprises hydrogen gas and hydrogen sulfide, and based on the whole activity catalytic gas, the volume fraction of the hydrogen gas is not less than 70%, and the volume fraction of hydrogen sulfide is 0.2%-5%; and the normal production process is that gasoline raw material is in contact with the catalyst in the atmosphere which is rich in the hydrogen gas under normal reaction conditions to be in hydrogenation reaction. By adopting the method provided by the invention, the selectivity of the catalyst can be improved. Compared with the prior art, under the situation that the sulfur content in a gasoline product is the same, the olefin saturation rate is lower and the loss in octane number of a product is smaller.

Description

technical field [0001] The present invention relates to a method for improving catalyst selectivity. Background technique [0002] As we all know, air pollution is a serious environmental problem, and a large number of engine emissions are one of the important causes of air pollution. In recent years, in order to protect the environment, countries around the world have put forward stricter restrictions on the composition of engine fuel, especially the sulfur content. The standards implemented in Beijing and Shanghai require the sulfur content in gasoline to be less than 50 μg / g. [0003] The processing capacity of catalytic cracking in my country accounts for a relatively large proportion of secondary processing, and catalytic cracking gasoline is the main source of commercial gasoline, and other gasoline components are few, and the blending ability is poor. Judging from the various blending components in the gasoline pool, the sulfur in catalytic cracking gasoline is the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J37/00B01J37/20B01J38/10C10G45/08
Inventor 习远兵高晓冬张登前李明丰屈锦华聂红褚阳李大东
Owner CHINA PETROLEUM & CHEM CORP
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