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Inactivated Co-Mo type hydrogenation catalyst regeneration liquid and regeneration method

A technology of hydrogenation catalyst and regeneration solution, which is applied in catalyst regeneration/reactivation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalyst, etc., to improve activity recovery rate, reduce usage, and be easy to promote Effect

Pending Publication Date: 2022-07-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method can only remove the carbon deposits in the catalyst, but the dust in the catalyst is not removed

Method used

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  • Inactivated Co-Mo type hydrogenation catalyst regeneration liquid and regeneration method
  • Inactivated Co-Mo type hydrogenation catalyst regeneration liquid and regeneration method
  • Inactivated Co-Mo type hydrogenation catalyst regeneration liquid and regeneration method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] To prepare the regeneration solution, the preparation steps and material consumption are as follows:

[0029] (a) Weigh 1.77 g of cobalt acetate into a 200 mL beaker, add 100 mL of deionized water and stir to dissolve;

[0030] (b) Weigh 0.42 g of citric acid and add it to the solution of step (a) and stir to dissolve;

[0031] (c) Weigh 0.012 g of ethylenediamine into the solution of step (b) and stir to dissolve.

[0032] Put 1000 grams of deactivated catalyst in a high temperature furnace, raise the temperature to 200°C at a heating rate of 3°C / min, and then keep the temperature constant for 80 minutes, then raise the temperature to 250°C at a heating rate of 3°C / min. The heating rate was raised to 400°C per minute, and after 80 minutes of constant temperature, it was cooled to room temperature and taken out. The number is T01, the S content of the catalyst T01 is 0.35 wt %, and the C content is 0.45 wt %.

[0033] Take 100 g of the charred catalyst T01 and put it...

Embodiment 2

[0035] To prepare the regeneration solution, the preparation steps and material consumption are as follows:

[0036] (a) Weigh 1.77 g mol of cobalt acetate into a 200 mL beaker, add 100 mL of deionized water, and stir to dissolve;

[0037] (b) Weigh 0.42 g of citric acid and add it to the solution of step (a) and stir to dissolve;

[0038] (c) Weigh 0.012 g of ethylenediamine into the solution of step (b) and stir to dissolve.

[0039] Take 100g of calcined catalyst T01, rinse with 300ml of 0.02mol / L oxalic acid aqueous solution for 30 minutes, then dry at 110°C for 4 hours, calcinate at 400°C for 3 hours, put it into a 1000mL plastic beaker, add 60mL of regeneration solution to saturate Dipping for 40 minutes, then curing and drying at 110°C for 3 hours. The dried catalyst was placed in a high-temperature furnace, the temperature rising rate was raised to 400°C at a rate of 3°C / min, and the temperature was kept constant for 4 hours to obtain a regenerated catalyst, numbered...

Embodiment 3

[0041] To prepare the regeneration solution, the preparation steps and material consumption are as follows:

[0042] (a) Weigh 3.54 grams of cobalt acetate into a 200 mL beaker, add 100 mL of deionized water, and stir to dissolve;

[0043] (b) Weigh 0.84 g of citric acid and add it to the solution of step (a) and stir to dissolve;

[0044] (c) Weigh 0.024 g of ethylenediamine into the solution of step (b) and stir to dissolve.

[0045] Take 100g of calcined catalyst T01, rinse with 300ml of 0.02mol / L oxalic acid aqueous solution for 30 minutes, then dry at 110°C for 4 hours, calcinate at 400°C for 3 hours, put it into a 1000mL plastic beaker, add 60mL of regeneration solution to saturate Dipping for 40 minutes, then curing and drying at 110°C for 3 hours. The dried catalyst was placed in a high-temperature furnace, the temperature rising rate was raised to 400°C at a rate of 3°C / min, and the temperature was kept constant for 4 hours to obtain a regenerated catalyst, numbered a...

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Abstract

The invention discloses an inactivated Co-Mo type hydrogenation catalyst regeneration liquid and a regeneration method. On the basis of the weight of the regeneration liquid, the regeneration liquid comprises 0.1 wt%-3.0 wt% of cobalt oxide, 80 wt%-96.9 wt% of water and 3 wt%-17 wt% of regeneration liquid; the regeneration liquid is organic acid and / or organic amine. The regeneration method comprises the following steps: (1) carrying out oil burning, sulfur burning and carbon burning treatment on the inactivated Co-Mo type aviation kerosene hydrogenation catalyst; (2) washing the scorched catalyst with a solution containing an organic acid, and then drying and roasting, and (3) adding the treated catalyst into a regeneration solution, carrying out saturated immersion treatment, and carrying out curing, drying and roasting to obtain the regenerated catalyst. According to the method, the specific surface area and the pore volume of the deactivated catalyst can be effectively recovered, and the hydrogenation activity of the catalyst can be recovered to the maximum extent.

Description

technical field [0001] The invention relates to a catalyst regeneration technology, in particular to a deactivated Co-Mo type hydrogenation catalyst regeneration solution and a catalyst regeneration method. Background technique [0002] The surface area of ​​the hydrorefining catalyst is inevitably carbonized during the operation. When the carbon deposition reaches a certain level, the pore volume and specific surface area of ​​the catalyst decrease, and the hydrodesulfurization activity of the catalyst decreases rapidly. At this time, the catalyst needs to be regenerated and burn off the surface of the catalyst. Carbon and sulfur can restore the pore volume and specific surface area of ​​the catalyst to the standard of the fresh agent, and the activity of the catalyst is restored. [0003] CN01121373.6 discloses a hydrogenation catalyst regeneration method. After preheating the deactivated hydrogenation catalyst, it is successively heated for 1-7 hours through a low tempera...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/882B01J23/94B01J38/02B01J38/62B01J38/48B01J35/10C10G45/08
CPCB01J23/882B01J23/002B01J23/94B01J38/02B01J38/62B01J38/485C10G45/08C10G2300/202B01J35/633B01J35/635B01J35/615Y02P20/584
Inventor 姚运海刘丽杨成敏段为宇郑步梅郭蓉李扬周勇孙进
Owner CHINA PETROLEUM & CHEM CORP