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High-fluorine-containing C9 resin hydrogenation catalyst and preparation method and application thereof

A hydrogenation catalyst and catalyst technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve the problems of low defluorination accuracy and complicated process flow

Active Publication Date: 2021-04-06
WUHAN KELIN FINE CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] In summary, it can be seen that the current pretreatment of resin hydrogenation is generally the removal of sulfur, nitrogen, and chlorine. 3 The pretreatment of catalytically polymerized resins with high fluorine content is less studied, and the current defluorination research is the process of washing with surfactants, the defluorination accuracy is not high, and the process is complicated

Method used

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  • High-fluorine-containing C9 resin hydrogenation catalyst and preparation method and application thereof
  • High-fluorine-containing C9 resin hydrogenation catalyst and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026]86.1 g of nickel nitrate, 3.8 g of copper chloride and 23.5 g of aluminum sulfate were added to water into solution I, then 0.5 mol / L of sodium hydroxide solution droplets were added to the solution I, and the reaction temperature was 65 ° C, and the system pH was 9 After the precipitation was completed, the constant temperature was stirred for 4 h, and the obtained slurry was treated. A 6.9 g of lymolybdate was dissolved in water, and 2 g of sodium dodecyl sulfonate was added to a solution II, stirred to 80 ° C, and then the above-mentioned slurry was added to the solution II, and the reaction was refluxed at 120 ° C for 4h. The resulting product was filtered, washed, dried to give a component M1Pretty precursor.

[0027]24 g of sodium bleed sodium, 100 g sodium silicate (25% SiO2The content), 33.5 g of aluminum sulfate each formulated into a solution, and the reaction temperature was added to the reaction vessel, the reaction temperature was 35 ° C, the pH was 6.5, and the re...

Embodiment 2

[0030]37.3 g of nickel chloride, 6.7 g of copper and 111.8 g of aluminum nitrate were added to water into a solution I, then 0.6 mol / L of ammonia solution droplets were added to the solution I, and the reaction temperature was 50 ° C, the system pH was 10, precipitation After completion, the constant temperature was stirred for 3 h, and the obtained slurry was treated. Ammonium 7.3 g of ketan-molybdate was dissolved in water, and a solution of 2.5 g of cencetal trimethyl bromide was added to a solution II, stirred to 50 ° C, and then the above obtained slurry was added to the solution II, at 80 ° C at 80 ° C The reflux reaction was 3 h, and the resulting product was filtered, washed, dried to give a component M1Pretty precursor.

[0031]32.2 g of aluminate, 40 g sodium silicate (25% SiO2The content), 67 g of aluminum sulfate each substrate into a solution, and the reaction temperature was added to the reaction vessel, the reaction temperature was 20 ° C, the pH was 9.5, and the react...

Embodiment 3

[0034]151 g of nickel nickel nickel nickel nickel nitrate, 31.6 g of aluminum nitrate was added to water into a solution I, then 0.5 mol / L of sodium hydroxide solution droplets were added to the solution I, control the reaction temperature of 80 ° C, and the system pH is 9, precipitation After completion, the constant temperature was stirred for 5 h, and the obtained slurry was treated. 6.8 g of four molybdate is dissolved in water, and 2 g of sodium dodecyl sulfonate is added to solution II, stirred to 65 ° C, and then adding the slurry to the solution II, reflux reaction at 100 ° C for 5 h, The resulting product was filtered, washed, dried to give a component M1Pretty precursor.

[0035]Put 16 g of aluminate, 40 g sodium silicate (25% SiO2The content), 47 g of aluminum aluminum sulfate each formulated into a solution, and the reaction temperature was added to the reaction vessel, and the reaction temperature was 50 ° C, the pH was 8, and the reaction was 2.5 h, then heated to 90 ° ...

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Abstract

The invention relates to a high-fluorine-containing C9 resin hydrogenation catalyst, which is composed of an active component M1, an auxiliary agent component M2 and a carrier component M3. Based on 100% of the total weight of the catalyst, the content of the M1 component is 37%-54%, the content of the M2 component is 4%-6%, and the balance is the M3 component. The component M1 contains Ni, Mo, Cu and Al, the component M2 contains Sm and Na, and the component M3 is amorphous silicon-aluminum MgAl2O4 composite oxide. The invention also discloses a preparation method and application of the catalyst. The catalyst provided by the invention is used for hydrogenation removal of fluorine and sulfur in C9 resin, and can effectively delay fluorine and sulfur poisoning of a rear-stage hydrogenation catalyst.

Description

Technical field[0001]The present invention relates to a high fluorine C9 resin hydrogenation catalyst, and further involves the preparation method of the catalyst, and its application in hydrogenation of hydrogen-containing C9 resin.Background technique[0002]The C9 resin is a thermoplastic resin obtained by the C9 fraction of the by-product in industrial ethiically e.flusion, which is heated or catalyzed by a thermoplastic resin obtained by the polymerization. Since its tackiness is strong, it is better to compatibility with other oils and resins. , Widely used in binder, road lacquer, ink and rubber and other industries. The C9 fraction typically contains impurities such as sulfur, nitrogen, olefins, and BF is used in C9 resin catalytic polymerization3The catalyst such that the C9 resin contains higher fluorine, and the above impurities cause a high resin chromaticity and poor photothermal stability, so that the application is limited. At present, Hydrogenation modification of C9 r...

Claims

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Application Information

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IPC IPC(8): B01J23/887C08F8/04C08F240/00
CPCB01J23/8871C08F8/04C08F240/00
Inventor 张先茂吴阳春王泽王瑜王国兴夏大寒周正赵志杰彭渺
Owner WUHAN KELIN FINE CHEM
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