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Method for purifying circulated gas regenerated continuously by reforming catalyst

A technology for reforming catalysts and circulating gases, applied in catalyst regeneration/reactivation, chemical instruments and methods, control/regulation of reforming operations, etc. Control, equipment corrosion, etc.

Inactive Publication Date: 2003-12-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

If this method is improperly operated, it will cause equipment corrosion, and even bring the alkali washing liquid into the drying tank, making the desiccant invalid, and the regeneration system is forced to shut down; and the gas treated by the alkali washing process needs to be washed with water, and the washed water The water content of the gas cannot be well controlled, resulting in an increase in the load of the drying system; there are also problems such as the pollution discharge of the alkali washing liquid, the freezing and cracking of the alkali washing tower and corresponding pipelines in winter, which affect the long-term stable operation of the regeneration system

Method used

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  • Method for purifying circulated gas regenerated continuously by reforming catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] The chlorine content of the charred regenerated gas and the dechlorinated gas was 1235 ppm. The gas is at a temperature of 400°C, a total pressure of 1.0MPa, and a volumetric space velocity of 1000h -1 Contact with the dechlorination agent in the dechlorination tank under certain conditions, and the gas after dechlorination is dried. The chlorine content of the purified gas is <1ppm.

Embodiment 2

[0029] The chlorine content of the charred regenerated gas and the dechlorinated gas was 4296ppm. The gas is at a temperature of 300°C, a total pressure of 1.0MPa, and a volumetric space velocity of 500h -1 Contact with the dechlorination agent in the dechlorination tank under certain conditions, and the gas after dechlorination is dried. The chlorine content of the purified gas is <1ppm.

Embodiment 3

[0031] The chlorine content of the gas after charring regeneration and the gas after dechlorination is 968ppm, and the water content is 5500 ppm. The gas is at a temperature of 300°C, a total pressure of 1.0MPa, and a volumetric space velocity of 500h -1 Contact with the dechlorination agent in the dechlorination tank under certain conditions, and the gas after dechlorination is dried. The chlorine content of the purified gas is <1ppm.

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Abstract

A process for purifying the circulating gas regenerated continuously by reforming catalyst includes such steps as removing Cl, cooling, drying, filtering, boosting up, heating and circulating back to coking segment. Its advantage is high effect to remove Cl to lower than 1 ppm.

Description

technical field [0001] The invention relates to a method for continuous catalytic reforming of naphtha, more specifically, a method for purifying circulating gas when the reforming catalyst is regenerated. Background technique [0002] Catalytic reforming unit is an important part of the oil refining and petrochemical industry. With the increase in the demand for gasoline for vehicles, the improvement of environmental protection requirements, the wide application of basic chemical raw materials such as light aromatics (benzene, toluene, xylene), and the refinery The increase in the demand for hydrogen for various newly-built hydrogenation units has led to greater development of catalytic reforming units at home and abroad. As of 2000, my country had 55 sets of catalytic reforming units with a total processing capacity of 16.47 million tons per year, including 14 sets of continuous reforming devices with a capacity of 8.89 million tons per year, accou...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J38/00B01J38/26B01J38/44C10G35/14C10G35/24
Inventor 赵仁殿丁冉峰张兰新张金锐田鹏程何宗付
Owner CHINA PETROLEUM & CHEM CORP
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