Octanol hydrorefining catalyst and preparation method thereof

A hydrogenation refining and catalyst technology, which is applied in hydrogenation preparation, chemical instruments and methods, preparation of hydroxyl compounds, etc. It can solve the problems of improving catalyst surface active sites, poor dispersion of active components, and reducing the distribution of active components, etc. problems, to achieve good industrial application prospects, high practical value, and the effect of improving catalytic performance

Inactive Publication Date: 2010-08-04
UNIV OF SCI & TECH BEIJING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, nickel-based catalysts also have some problems. They are prone to agglomeration, poor dispersion, or easy to form nickel-aluminum spinel, resulting in low nickel content on the surface and low utilization rate. Therefore, general nickel-based catalysts can only be used at higher nickel loadings better catalytic activity
The main reasons for these problems are: (1) under common preparation conditions (such as impregnation), the active component Ni is easy to enter the carrier skeleton to generate metal-carrier solid solutions or new compounds, and the generation of these components reduces the active component. Distribution on the surface of the carrier; (2) In the preparation process such as precipitation method, the precipitation reaction increases the size of nickel particles, although the content of nickel species on the surface can be increased, but the dispersion of active components is not good, which is not conducive to improving the surface active sites of the catalyst.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Add 200g of pseudo-boehmite powder, 3g of celadon powder, 6g of concentrated nitric acid, and 180g of water, fully knead, and extrude into The trilobal-shaped strip-shaped carrier is dried at 110°C for 10 hours, and then roasted at 600°C for 3 hours to obtain the required carrier A; prepare 0.02mol / L lanthanum nitrate solution B, 1.0mol / L Mixed solution C of nickel nitrate + 1.0mol / L urea; immerse 10g of carrier A in lanthanum nitrate solution B for 3 hours, dry at 110°C and then roast at 50°C for 3 hours; then immerse in 20ml of C solution, put it in an autoclave, Place at 110°C for 24h, after the experiment is completed, dry at 110°C and bake at 500°C for 3h to prepare the catalyst precursor.

Embodiment 2

[0030] Add 200g of pseudo-boehmite powder, 3g of celadon powder, 6g of concentrated nitric acid, and 180g of water, fully knead, and extrude into The three-leaf-shaped strip-shaped carrier is dried at 110°C for 10 hours, and then roasted at 600°C for 3 hours to obtain the required carrier A; configure 0.02mol / L lanthanum nitrate solution B, 1.5mol / L Nickel nitrate + 1.5mol / L urea mixed solution C; firstly impregnate 10g of carrier A in lanthanum nitrate solution B for 3h, dry at 110°C and then roast at 500°C for 3h; then impregnate in 20ml of C solution and put it in an autoclave , placed at 110°C for 24h, after the experiment was completed, dried at 110°C and calcined at 500°C for 3h to obtain a catalyst precursor.

Embodiment 3

[0032] Add 200g of pseudo-boehmite powder, 5g of scallop powder, 8g of concentrated nitric acid, and 160g of water, fully knead, and extrude into The trilobal-shaped strip carrier, the formed carrier is dried at 110°C for 10h, and then roasted at 600°C for 3h to obtain the required carrier A; configure 0.05mol / L lanthanum nitrate solution B, 1.0mol / L Nickel nitrate + 1.0mol / L urea mixed solution C; firstly impregnate 10g of carrier A in lanthanum nitrate solution B for 3h, dry at 110°C and then roast at 500°C for 3h; then impregnate in 20ml of C solution and put it in an autoclave , placed at 120°C for 24h, after the experiment was completed, dried at 110°C and calcined at 500°C for 3h to obtain a catalyst precursor.

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PUM

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Abstract

The invention discloses an octanol hydrorefining catalyst, which belongs to the field of hydrorefining catalytic materials. The prepared catalyst is used for modifying a carrier by using a rare earth element, reducing the amount of an active component of a nickel ion entering a carrier framework and improving the content of surface nickel species; the active component is loaded by adopting a hydrothermal deposition method, the dispersion of nickel salts on the surface of a carrier pore canal by using hydrothermal high-temperature and high-pressure conditions and forming nickel precipitation with proper size at the loading initial period of the active component by using a deposition reaction, so the invention can effectively control the amount of the nickel ions entering the carrier, improve the content of the surface nickel species and simultaneously can avoid the growth of nickel oxide particles; and the catalyst greatly increases the surface nickel active site, effectively improves the utilization rate of the active component of nickel and has higher catalytic reaction activity during hydrorefining the octanol at higher airspeed. The result shows that the hydrogenation rate of an unsaturated substance in crude octanol reaches over 90 percent when the temperature is 120DEG c, the pressure is 2.5MPa, the ratio of hydrogen to liquid for feeding is 8:1 and the airspeed is 30<-1>hour.

Description

technical field [0001] The invention belongs to the technical field of hydrogenation refining catalytic materials, in particular to a hydrothermal deposition synthesis of rare earth elements modified Ni / Al 2 o 3 Catalyst preparation and application. Background technique [0002] Octanol is an important chemical raw material, widely used in plasticizing, medicine, dyestuff, pesticide and so on. In industry, octanol is mainly produced by hydrogenation of octenal, but the synthesized products often contain a small amount of reactants (octenal) and unsaturated by-products (isooctanal and octenol), which greatly affect the purity of octanol. . Due to the continuous improvement of the quality requirements of fine chemicals, it is of special significance to improve the purity of octanol and remove the unsaturated components. So far, neither imported nor domestic catalysts can achieve 100% hydrogenation rate of octenal. [0003] At present, the main method adopted in this field...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83C07C31/125C07C29/90C07C29/17C07C29/141
Inventor 李晓刚杨仁春吴俊升
Owner UNIV OF SCI & TECH BEIJING
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