Method for regenerating and revivifying hydrogenation catalyst

A technology of hydrogenation catalysts and compounds, applied in catalyst regeneration/reactivation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as complex processes and large heat release, and achieve simple processes, weakened interactions, The effect of high active recovery degree

Active Publication Date: 2010-01-06
CHINA PETROLEUM & CHEM CORP +1
View PDF2 Cites 19 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] CN1298925A discloses hydrogenation catalyst external regeneration method, adopts vertical thin layer moving bed regenerator, and burns sulfur section and burns charcoal section and carries out separately, overcomes burning sulfur and charcoal and burns off at high temperature when exothermic big at the same time Disadvantages, but the degree of recovery of catalyst activity can be further improved
This regeneration method requires repeated washing with a large amount of anhydrous methanol or ethanol, and the process is complicated

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Preparation of deactivated catalyst.

[0019] Take Industrial CoMo / Al 2 o 3 Hydrorefining catalyst, hydrodesulfurization of diesel fuel in a trickle bed reactor until the activity is significantly lower than that of the fresh catalyst (see Table 1). Lower the temperature to room temperature, and take out the deactivated hydrotreating catalyst, numbered SA.

[0020] The following examples use the SA catalyst to carry out the regeneration test.

Embodiment 2

[0022] Take the catalyst SA and regenerate it in an air atmosphere. Calcined at a constant temperature of 300°C for 5 hours, then raised to 525°C for 5 hours, and cooled to room temperature to obtain catalyst A0.

Embodiment 3

[0024] Catalyst A0 was impregnated with 0.5% dodecylmercaptan by weight of catalyst A0 for 2 hours, and then calcined at 380° C. for 1 hour to obtain catalyst A1.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention discloses a method for regenerating and revivifying a hydrogenation catalyst, which comprises the steps of treating an inactivated hydrogenation catalyst subjected to sulfur burning and carbon burning treatment with organic sulfur compound-containing thioalcohol and/or thioether and roasting a resulting product, wherein the organic sulfur compound-containing thioalcohol and/or thioether accounts for 0.1 to 2.2 percent of the weight of the inactivated hydrogenation catalyst. The method of the invention can effectively weaken the interaction between metal and the carrier to obtain a regenerated hydrogenation catalyst with high activity restoration degree. The method is particularly suitable for vulcanized hydrofining catalysts and hydrogenation catalysts.

Description

technical field [0001] The invention relates to a regeneration and revival method of a hydrogenation catalyst, in particular to a regeneration and revival method of a sulfurized non-noble metal hydrorefining catalyst or a hydrogenation treatment catalyst. Background technique [0002] Hydrogenation catalysts are key to the production of clean fuel oils and other chemical feedstocks from crude oil. During the hydrogenation process, the catalyst will be deactivated due to various reasons, mainly including: the active metal on the catalyst changes due to long-term operation, the pore structure of the catalyst changes due to the carbon deposit on the catalyst, impurities in the raw oil (such as Catalyst irreversible deactivation caused by metal nickel, vanadium) deposition, etc. Among these phenomena, the influence of carbon deposition is the most obvious. Deactivated hydrotreating catalysts typically contain 3-15% by weight of carbon deposits which result in a reduction in ca...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): B01J39/20B01J38/10
Inventor 杨成敏郭蓉姚运海段为宇丁莉
Owner CHINA PETROLEUM & CHEM CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products

Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic.

© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap