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Catalytic conversion catalyst regenerator and regeneration method

A catalytic conversion and regenerator technology, applied in the direction of catalyst regeneration/reactivation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of increasing the height of the device, and achieve the effect of reducing the height and improving the effect of gas-solid separation

Active Publication Date: 2017-07-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In actual production, due to the arrangement of equipment in the settler, the height of the dilute phase section is about 1.8 to 2.0 times the conveying settlement height, resulting in an increase in the height of the device

Method used

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  • Catalytic conversion catalyst regenerator and regeneration method
  • Catalytic conversion catalyst regenerator and regeneration method
  • Catalytic conversion catalyst regenerator and regeneration method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0044] figure 1 It is a schematic diagram of the basic equipment of Embodiment 1 provided by the present invention.

[0045] figure 1 The shown regenerator equipment includes the first regeneration zone 1 (fast fluidized bed), the delivery pipe 2, the subsequent regeneration zone 3 of the first regeneration zone (dense phase fluidized bed, hereinafter referred to as the second regeneration zone), the first stage gas Solid separator 4, second-stage gas-solid separator 5, third-stage gas-solid separator 6, flue gas collection chamber 7, flue gas delivery pipeline 8, heat collector 9, catalyst circulation pipeline 10, main air pipeline 11 , the waiting catalyst delivery pipeline 12, the regenerated catalyst delivery pipeline 13, the fluidizing air pipeline 14, the connector 15 between the delivery pipe and the first-stage gas-solid separator.

[0046] Such as figure 1 As shown, the catalyst to be regenerated enters the first regeneration zone 1 through the pipeline 12, and is ...

Embodiment approach 2

[0048] figure 2 It is a schematic diagram of the basic equipment of Embodiment 2 provided by the present invention.

[0049] figure 2 The shown regenerator equipment includes the first regeneration zone 1 (dense phase fluidized bed), delivery pipe 2, the subsequent regeneration zone 3 of the first regeneration zone (dense phase fluidized bed, referred to as the second regeneration zone), the first stage gas Solid separator 4, second-stage gas-solid separator 5, third-stage gas-solid separator 6, flue gas collection chamber 7, flue gas delivery pipeline 8, heat collector 9, regenerated catalyst circulation pipeline 10, main air pipeline 11. The waiting catalyst delivery pipeline 12, the regenerated catalyst delivery pipeline 13, the main air pipeline 14, and the connector 15.

[0050] Such as figure 2 As shown, the catalyst to be regenerated enters the first regeneration zone 1 through the pipeline 12, and is regenerated in contact with the regeneration gas from the main ...

Embodiment approach 3

[0052] image 3 It is a schematic diagram of the basic equipment of Embodiment 3 provided by the present invention.

[0053] image 3 The equipment includes the first regeneration zone 1 of the fast fluidized bed, the conveying pipe 2, the subsequent regeneration zone 3 of the first regeneration zone (dense phase fluidized bed, referred to as the second regeneration zone), the first-stage gas-solid separator 4, the second Stage gas-solid separator 5, flue gas collection chamber 7, flue gas delivery pipeline 8, heat collector 9, catalyst circulation pipeline 10, main air pipeline 11, standby catalyst delivery pipeline 12, regenerated catalyst delivery pipeline 13, fluidization Air pipeline 14, connector 15.

[0054] Such as image 3 As shown, the catalyst to be regenerated enters the first regeneration zone 1 through the pipeline 12, and is regenerated in contact with the regeneration gas from the main air pipeline 11. Part of the regenerated catalyst in the first regenerati...

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Abstract

Catalytic conversion catalyst regenerator, including at least two regeneration zones, delivery pipes, gas-solid separation equipment, and flue gas collection chamber, wherein one end of the delivery pipe communicates with the first regeneration zone, and the other end of the delivery pipe communicates with the gas-solid separation equipment , the gas-solid separation equipment is located in the subsequent regeneration zone of the first regeneration zone, and the gas-solid separation equipment is connected with the flue gas collection chamber. The catalyst to be regenerated enters the first regeneration zone and is burnt. The regenerated catalyst and flue gas enter the subsequent regeneration zone through the conveying pipe and gas-solid separation equipment to contact the fluidized medium, and the regenerated catalyst leaves the regenerator. The invention airtightly connects the conveying pipe with the gas-solid separator, greatly reduces the flue gas volume in the subsequent regeneration zone, reduces the height of the regenerator, and greatly improves the gas-solid separation effect after adopting the three-stage gas-solid separator.

Description

technical field [0001] The invention relates to a regenerator and a regeneration method for charcoal-containing catalysts in the catalytic cracking process. Background technique [0002] When the raw oil undergoes catalytic cracking reaction, due to the condensation reaction, in addition to generating light hydrocarbons, a part of coke is also generated, which is deposited on the catalyst, thereby reducing the activity and selectivity of the catalyst. Therefore, the high-temperature oxidation regeneration method is used to burn and remove the coke on the catalyst to restore the performance of the catalyst. This process is called catalyst regeneration. Usually, the catalyst with deposited coke is called a standby catalyst, and the catalyst after oxidation regeneration is called a catalyst. to regenerate the catalyst. The coking process is completed in the regenerator, which can be divided into turbulent bed, fast bed and conveying bed according to the different types of rege...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J38/30
Inventor 崔守业常学良马建国刘守军
Owner CHINA PETROLEUM & CHEM CORP