Hydrotreating catalyst intermediate, hydrotreating catalyst, and preparation methods of hydrotreating catalyst intermediate and hydrotreating catalyst

A hydrogenation treatment and catalyst technology, which is applied in the direction of physical/chemical process catalysts, chemical instruments and methods, organic chemistry, etc., can solve the problem that the active metal component cannot fully play its role, the hydrogenation catalyst cannot be completely vulcanized, the active metal group Insufficient vulcanization and other problems can be solved to shorten the start-up time, solve the problems of airtightness and heat release, and facilitate storage and transportation

Active Publication Date: 2017-07-14
CHINA PETROLEUM & CHEM CORP +1
View PDF11 Cites 7 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

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
[0008] Furthermore, the existing external presulfurization and internal presulfurization are both presulfurized or activated under the action of hydrogen, and hydrogenolysis reactions of oxidized hydrogenation catalysts will occur, and because the binding force between the active component and the carrier is often too high Strong, so that the hydrogenation catalyst cannot be completely vulcanized, resulting in 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

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

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Hydrotreating catalyst intermediate, hydrotreating catalyst, and preparation methods of hydrotreating catalyst intermediate and hydrotreating catalyst
  • Hydrotreating catalyst intermediate, hydrotreating catalyst, and preparation methods of hydrotreating catalyst intermediate and hydrotreating catalyst
  • Hydrotreating catalyst intermediate, hydrotreating catalyst, and preparation methods of hydrotreating catalyst intermediate and hydrotreating catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0058] Example 1 Preparation of Hydrotreating Catalyst A

[0059] Weigh 40.6g of ammonium molybdate, 21.7g of nickel nitrate, and 50mL of ammonia water, and mix them with deionized water to 100mL to obtain solution I. Dissolve 41 g of 2,4,6-trimercapto-s-triazine triammonium salt in 50 mL of water to obtain solution II. Weigh 84g of macroporous pseudo-boehmite (73wt% on a dry basis) and 24mL of silica gel (containing 30wt% of silicon dioxide) into 1L of water, stir vigorously for 20min, add solutions I and II side-by-side, and then After stirring for 30 min, wash and filter with suction. The filter cake obtained by suction filtration was heat-treated at a low temperature of 80° C. for 3 hours. After the filter cake is pulverized, add 3 g of scallop powder and mix evenly, then mix 42 g of small-pore alumina with 3 g of citric acid, 10 mL of nitric acid (concentration: 30 wt%), and 120 mL of deionized water to make a slurry as a binder. After rolling for 20 min, the Extruded ...

Embodiment 2

[0060] Example 2 Preparation of Hydrotreating Catalyst B

[0061] Take 33.5g of molybdenum oxide, 9.2g of basic nickel carbonate, 2mL of phosphoric acid, and 60mL of deionized water, mix them uniformly and boil for 1 hour to obtain solution I. Weigh 58 g of 2,4-dimercapto-s-triazine diammonium salt and dissolve it in 100 mL of acetone solution to obtain solution II. Weigh macroporous pseudo-boehmite (dry basis is 73wt%) 72g, zirconium oxychloride 12g and water-soluble silicone oil 20g, put into 1L water then, after strong stirring for 20min, solution 1 is dripped into the slurry and stirred for 10min, Then the solution II was dripped into the slurry, stirred vigorously during the dripping process, then stirred for 30 minutes, washed, and suction filtered. The filter cake obtained by suction filtration was heat-treated at a low temperature of 80° C. for 3 hours. After the filter cake is pulverized, add 3 g of scallop powder and mix evenly, then mix 56 g of small-pore alumina ...

Embodiment 3

[0062] Example 3 Preparation of Hydrotreating Catalyst C

[0063] Weigh 40.6g of ammonium molybdate, 21.7g of nickel nitrate, and 50mL of ammonia water, and mix them with deionized water to 100mL to obtain solution I. 102 g of 2,4,6-trimercapto-s-triazine monoammonium salt was dissolved in 50 mL of water to obtain solution II. The other steps were the same as in Example 1 to obtain hydrogenation catalyst C. The main physical properties are shown in Table 1.

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

PropertyMeasurementUnit
specific surface areaaaaaaaaaaa
diameteraaaaaaaaaa
specific surface areaaaaaaaaaaa
Login to view more

Abstract

The present invention discloses a hydrotreating catalyst intermediate, a hydrotreating catalyst, and preparation methods of the hydrotreating catalyst intermediate and the hydrotreating catalyst. According to the present invention, the hydrotreating catalyst intermediate comprises a hydrogenation activity metal component, a carrier component and a specific organic compound, and can complete the vulcanization process without a hydrogen sulfide generation reaction and a vulcanization reaction between hydrogen sulfide and an active metal, such that the problem that the temperature increase is too rapid during the catalyst vulcanization process can be avoided; the hydrotreating catalyst is the vulcanization type hydrotreating catalyst having complete significance, and after the hydrotreating catalyst is loaded into the hydrogenation reaction device, the hydrogenation reaction temperature can be directly achieved so as to substantially shorten the startup time; and the catalyst has advantages of complete vulcanization, good metal dispersibility, and good hydrogenation property.

Description

technical field [0001] The invention relates to a hydrogenation treatment catalyst, in particular to a hydrogenation treatment catalyst intermediate, a hydrogenation treatment catalyst and a preparation method thereof. Background technique [0002] Conventional hydrogenation catalysts are in an oxidized state, but the substances that actually play an active role in actual use are in a sulfurized state, so the hydrogenation catalysts in an oxidized state need to be pre-sulfurized before use. The commonly used pre-sulfurization methods are in-vehicle pre-sulfurization and out-of-vehicle pre-sulfurization. The in-vehicle pre-sulfurization is to put the oxidized catalyst into the hydrogenation reactor, and pass hydrogen and sulfidation agent into the reactor during the heating process, so that It generates hydrogen sulfide, which converts the hydrogenation active metal from oxide to sulfide. External pre-sulfurization means that the catalyst is combined with the sulfurizing age...

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): C07D251/38B01J27/051B01J35/10C10G45/08
CPCB01J27/0515B01J35/1019B01J35/1057B01J35/1061C07D251/38C10G45/08
Inventor 徐黎明高玉兰吕振辉张学辉佟佳孙海
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