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Hydrogenation catalyst regenerating method

A hydrogenation catalyst and catalyst technology, applied in catalyst regeneration/reactivation, chemical instruments and methods, physical/chemical process catalysts, etc.

Active Publication Date: 2019-06-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For the deactivated catalyst caused by carbon deposition, its activity can be restored by regeneration, but for the deactivated catalyst caused by metal deposition pollution, it cannot be regenerated to restore its activity, so it can only be discarded.

Method used

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  • Hydrogenation catalyst regenerating method
  • Hydrogenation catalyst regenerating method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Take a deactivated hydrotreating catalyst with a carbon deposit of 5.8%, and its active metal components are Mo and Ni, and perform carbon burning regeneration treatment in an oxygen-containing atmosphere. At a heating rate of 3°C / min, the temperature was raised to 200°C, kept at a constant temperature for 10 hours, and then continued to rise to 310°C, kept at a constant temperature for 8 hours. The obtained sample had a carbon content of 1.8% and a sulfur content of 2.0%. The obtained sample was named C-1.

[0025] Take a deactivated hydrotreating catalyst with a carbon deposition of 7.9%, and its active metal components are Mo, Ni, Co, and use different conditions to burn carbon regeneration treatment in an oxygen-containing atmosphere. At a heating rate of 3°C / min, the temperature was raised to 200°C and kept at a constant temperature for 10 hours, and then continued to rise to 320°C and kept at a constant temperature for 10 hours. The obtained sample had a carbon con...

Embodiment 2

[0027] Take 15g of tetrakis hydroxymethylphosphorus sulfate aqueous solution (solution concentration: 75wt%), spray catalyst C-1, after aging for 3 hours, treat at 100°C for 3 hours, take 2.3ml of hydrazine hydrate, spray it, and spray it at 100°C Low temperature heat treatment for 3 hours. That is, the desired catalyst C-3 is obtained.

Embodiment 3

[0029]Take 14g of tetrahydroxyethylphosphorus sulfate, dilute it with water to form a 75ml solution, spray the catalyst C-2 with the solution, and after aging for 3 hours, heat-treat at 80°C for 3 hours. After spraying with 2.3ml of hydrazine hydrate, heat treatment at a low temperature of 100°C for 3 hours. That is, the desired catalyst C-4 is obtained.

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Abstract

The invention provides a hydrogenation catalyst regenerating method, which comprises: (1) making a to-be-regenerated hydrogenation catalyst contact an oxygen-containing gas, and carrying out charcoalburning treatment to obtain a catalyst A; (2) making the catalyst A contact an organic compound solution, and carrying out heat treatment to obtain a catalyst B; and (3) introducing hydrazine hydrateinto the catalyst B, and carrying out heat treatment to obtain a regenerated catalyst. The regeneration method of the present invention can increase the activity of the regenerated catalyst.

Description

technical field [0001] The invention relates to a catalyst regeneration method, in particular to a hydrogenation catalyst regeneration method. Background technique [0002] Hydroprocessing is a very important process for converting crude oil into high-value products, and its core is a hydroprocessing catalyst. The activity of the catalyst is provided by the sulfide state of the metal. The activity of the catalyst will gradually decrease during use, that is, the catalyst is deactivated. In summary, the reasons are generally divided into coking deactivation (causing catalyst pore blockage), poisoning deactivation (causing catalyst acid center poisoning) and sintering deactivation (causing catalyst crystal phase changes), etc. The main reasons for the deactivation of industrial hydrogenation catalysts are coke formation and metal blockage, migration or aggregation of active metal components, changes in phase composition, reduction in the number of active centers, sintering of...

Claims

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Application Information

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IPC IPC(8): B01J38/20B01J38/02B01J38/50B01J38/66
Inventor 徐黎明高玉兰葛海龙孟兆会佟佳
Owner CHINA PETROLEUM & CHEM CORP
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