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Regeneration method of hydrogenation catalyst

A hydrogenation catalyst and catalyst technology, applied in the direction of catalyst regeneration/reactivation, chemical instruments and methods, catalyst activation/preparation, etc., can solve problems such as temperature rise, metal waste, and shortened start-up time in the vulcanization process, and achieve improved initial vulcanization Effect of temperature, stool storage and transportation, and improvement of dispersion state

Active Publication Date: 2017-05-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0018] Since hydrogen sulfide is generated during the vulcanization process, hydrogen sulfide reacts with active metals, and this process will generate a lot of heat, resulting in a rapid rise in the temperature during the vulcanization process
[0019] In order to avoid excessive temperature rise, the vulcanization process heats up slowly, but this will cause the catalyst vulcanization time to be too long, which is not conducive to shortening the start-up time
[0020] Furthermore, both the existing internal presulfurization and external presulfurization will cause insufficient vulcanization of the active metal component in the hydrogenation catalyst, poor dispersion of the active metal, and the inability of the active metal component to fully play its role, resulting in metal waste

Method used

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  • Regeneration method of hydrogenation catalyst
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  • Regeneration method of hydrogenation catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0078] Example 1 Catalyst burning charcoal

[0079] Take a hydrodemetallization catalyst to be regenerated with a carbon deposit of 6.7wt% and a sulfur content of 7.1wt%, and perform charcoal burning in an oxygen-containing atmosphere. The specific process is as follows:

[0080] Take 500g of the hydrogenation catalyst to be regenerated, raise the temperature to 230°C at a heating rate of 3°C / min, directly pass air into it and keep the temperature at 230°C for 10 hours, then reduce the oxygen content of the oxygen-containing gas to 10%, and continue to heat up at 3°C / min heating rate, heated to 320 ° C constant temperature for 3 hours, the obtained sample was named A, and its carbon content was 1.5%.

Embodiment 2

[0081] Example 2 Catalyst burning charcoal

[0082] Take a hydrodemetallization catalyst to be regenerated with a carbon deposit of 7.8wt% and a sulfur content of 7.5wt%, and carry out charcoal-burning treatment under an oxygen-containing atmosphere. The specific process is as follows:

[0083] Take 500g of the hydrogenation catalyst to be regenerated, heat up to 200°C at a heating rate of 3°C / min, directly feed air at 200°C for 6 hours, and then continue at a heating rate of 3°C / min, the oxygen content of the oxygen-containing gas The temperature was reduced to 15%, and the temperature was raised to 350°C for 5 hours at a constant temperature. The obtained sample was named B, and its carbon content was 0.8%.

Embodiment 3

[0084] Embodiment 3 Preparation of regenerated catalyst C

[0085] Weigh 100g of sample A, dissolve 18g of 2,4,6-trimercaptotriazine triammonium salt in 20wt% ammonia solution, then spray sample A, dry in the shade in a ventilated place, and heat-treat at 250°C for 3 hours under the protection of nitrogen. The regenerated catalyst C was obtained, and its main physical properties are shown in Table 1.

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Abstract

The invention discloses a regeneration method of a hydrogenation catalyst. The method comprises the following steps: 1, the hydrogenation catalyst to be regenerated is in contact with an oxygen-containing gas to carry out carbon burning regeneration; and 2, an organic compound is introduced to a carbon-burnt catalyst obtained in step 1, and at least one low-temperature heat treatment is carried out, wherein no calcination is carried out. The regenerated catalyst realizes direct in-situ sulfuration of metals on the surface of the catalyst without a generation reaction of hydrogen sulfide or a sulfuration reaction of hydrogen sulfide and the active metal in the sulfuration starting process, so the initial sulfuration temperature at working starting of the catalyst is greatly improved, the problem of too fast temperature rising in the catalyst sulfuration process is solved, and the starting time is greatly shortened.

Description

technical field [0001] The invention relates to a regeneration method of a hydrogenation catalyst. Background technique [0002] With the sales of refining catalysts increasing year by year, the production of spent catalysts is also increasing year by year. [0003] If the spent catalysts are not managed scientifically, the toxic and harmful components in them will pollute the environment and endanger human health, and some of the precious metal resources will also be lost. [0004] Therefore, the regeneration and utilization of deactivated hydrogenation catalysts has drawn extensive attention from industry and academia. [0005] Improving the activity of the regenerated hydrogenation catalyst not only has high social benefits, but also brings considerable economic benefits to refineries. [0006] In the prior art, after the hydrogenation catalyst is regenerated, it is generally an oxidized catalyst, and the catalyst needs to be presulfurized before use. [0007] Hydrogen...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J38/00B01J38/02B01J38/50B01J37/20B01J37/18B01J37/02C10G45/08C10G49/04
Inventor 徐黎明高玉兰吕振辉张学辉佟佳孙海
Owner CHINA PETROLEUM & CHEM CORP
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