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Nickel-based catalyst used for preparation of hydrogenated petroleum resin as well as preparation method and application of catalyst

A technology for hydrogenating petroleum resins and nickel-based catalysts, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the influence of catalyst life and reduce catalyst hydrogenation activity , irreversible deactivation and other problems, to achieve the effect of inhibiting the reduction of softening point, high industrial application value, and excellent hydrogenation performance

Active Publication Date: 2019-07-12
FUZHOU UNIVERSITY
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] Although palladium-based catalysts have high catalytic hydrogenation activity for petroleum resins and can effectively inhibit the hydrogenation degradation of petroleum resins, they are sensitive to sulfur-containing compounds in petroleum resins and are easily poisoned, resulting in irreversible deactivation. higher
Patent CN 103386302A discloses a petroleum resin hydrogenation catalyst, which uses γ-Al 2 o 3 As a carrier, supporting noble metal Pd and oxide promoters, the metal Pd crystallites with a particle size of less than 3 nm in the obtained catalyst account for more than 90%, but its disadvantage is that the catalytically active metal Pd has a great influence on the impurity S 2- / Cl - Poor tolerance, easy poisoning and deactivation, catalyst life is affected
[0008] The nickel-diatomite supported catalyst prepared by the impregnation method reported in the patent US 3040009 is used in the hydrogenation reaction of C5 petroleum resin. After reacting for 5-7 h, the bromine value of the obtained hydrogenated petroleum resin is 1-3 gBr 2 / 100g, its disadvantage is that the preparation of high-loaded active metals by traditional impregnation method is easy to cause the aggregation of active components, and it is easy to sinter at high temperature, which reduces the hydrogenation activity of the catalyst

Method used

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  • Nickel-based catalyst used for preparation of hydrogenated petroleum resin as well as preparation method and application of catalyst
  • Nickel-based catalyst used for preparation of hydrogenated petroleum resin as well as preparation method and application of catalyst
  • Nickel-based catalyst used for preparation of hydrogenated petroleum resin as well as preparation method and application of catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] 0.01 mol Ni(NO 3 ) 2 •6H 2 O (molecular weight 290.81), 0.05 mol Mg(NO 3 ) 2 •6H 2 O (molecular weight 256.41), 0.05mol Al(NO 3 ) 3 •9H 2 O (molecular weight 375.13), 0.001 mol La(NO 3 ) 3 •9H 2 O (molecular weight 487.05) and 0.405 mol urea (molecular weight 60.06) were added to 100 g of deionized water, stirred evenly, transferred to a stainless steel reactor with a polytetrafluoroethylene liner, and then placed in a rotary oven at 95 °C for dynamic crystallization. 6 h, after static aging for 6 h, cool to room temperature, vacuum filter, wash the precipitate, and dry the precipitate in an oven at 70 °C to constant weight to obtain the quaternary nickel-magnesium-aluminum-lanthanum hydrotalcite NiMgLaAl-LDH, and then the obtained quaternary The nickel-magnesium-aluminum hydrotalcite was placed in a muffle furnace, raised from room temperature to 500 °C at a rate of 5 °C / min, and calcined for 6 h to obtain a composite metal oxide precursor, which was placed i...

Embodiment 2

[0044] 0.025 mol Ni(NO 3 ) 2 •6H 2 O, 0.05 mol Mg(NO 3 ) 2 •6H 2 O, 0.05mol Al(NO 3 ) 3 •9H 2 O , 0.002 mol Cu(NO 3 ) 2 •3H 2 O (molecular weight 235.56) and 0.45mol urea were added to 120g deionized water, stirred evenly, transferred to a stainless steel reactor with a polytetrafluoroethylene liner, and then placed in a rotary oven for dynamic crystallization at 105 °C for 12 h. After static aging for 6 h, cool to room temperature, vacuum filter, wash the precipitate, and dry the precipitate in an oven at 70 °C to constant weight to obtain light green quaternary hydrotalcite NiMgAlCu-LDH, and then place the obtained quaternary hydrotalcite in a horse In a Furnace, the temperature was increased from room temperature to 400 °C at a rate of 5 °C / min, and roasted for 6 h to obtain a composite metal oxide precursor, which was placed in a tube furnace under a hydrogen atmosphere at 750 °C (flow rate kept Reduction at 50-100 ml / min) for 6 h, then cooled to room temperatur...

Embodiment 3

[0047] 0.01 mol Ni(NO 3 ) 2 •6H 2 O, 0.05 mol Mg(NO 3 ) 2 •6H 2 O, 0.05mol Al(NO 3 ) 3 •9H 2 O , 0.002mol Cu(NO 3 ) 2 •3H 2 O and 0.405 mol urea were added to 100 g of deionized water, stirred evenly, transferred to a stainless steel reactor with a polytetrafluoroethylene liner, and then placed in a rotary oven for dynamic crystallization at 115 °C for 18 h, and after static aging for 6 h , cooled to room temperature, vacuum filtered, washed the precipitate, and dried the precipitate in an oven at 70 °C to constant weight to obtain light green quaternary hydrotalcite NiMgAlCu-LDH, and then place the obtained quaternary hydrotalcite in a muffle furnace to The rate of 5 ℃ / min was increased from room temperature to 600 ℃, and calcined for 6 h to obtain a composite metal oxide precursor, which was placed in a tube furnace under a hydrogen atmosphere of 850 ℃ (the flow rate was kept at 50-100 ml / min) reduction for 6 h, then cooled to room temperature, formed by mechanic...

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Abstract

The invention discloses a nickel-based catalyst used for preparation of hydrogenated petroleum resin as well as a preparation method and application of the catalyst. The method comprises the followingsteps: preparing carbonate radical intercalated NiMgAl-M-LDH (M=La or Cu) quaternary hydrotalcite by adopting a urea hydrolysis method, performing high-temperature calcination, and performing reduction in a reducing atmosphere to obtain the nickel-based catalyst having a high specific surface area and a highly-dispersed active center. According to the catalyst synthesized by the method, auxiliaryagent metal element La or Cu is doped, so that the acidity of the surface of the catalyst can be effectively neutralized, inhibition of hydrodegradation of petroleum resin is facilitated, the softening point of the hydrogenated product is improved, dispersity of the active center Ni can be effectively increased, and deep hydrogenation of unsaturated hydrocarbon bonds in the petroleum resin can bepromoted; and the catalyst has a simple and easy synthetic method, low preparation costs, a simple hydrogenation process and easy industrialization, and when the obtained catalyst is used for hydrogenation of the petroleum resin, the hydrogenated petroleum resin having a water white color and a high softening point can be prepared.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, and in particular relates to a nickel-based catalyst used for the preparation of hydrogenated petroleum resin, a preparation method and application thereof. Background technique [0002] Petroleum resin is a kind of thermoplastic resin produced by polymerizing the by-product distillate oil in the cracking ethylene production process. It is widely used in coatings, rubber additives, printing and other industries, but at the same time, petroleum resin contains A large number of impurities such as unsaturated hydrocarbon bonds and halogen elements make petroleum resins have disadvantages such as dark hue, pungent smell, poor adhesion, light and thermal stability, and poor oxidation stability, which limits its application in high-precision fields. [0003] Hydrogenated petroleum resin is a special material with excellent performance obtained by catalytic hydrogenation of unsaturated C=C ...

Claims

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Application Information

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IPC IPC(8): B01J23/83B01J23/755B01J35/10C08F8/04C08F240/00
CPCB01J23/83B01J23/755B01J23/002C08F8/04B01J2523/00B01J35/647B01J35/615C08F240/00B01J2523/22B01J2523/31B01J2523/3706
Inventor 袁珮杨江涛鲍晓军朱海波王廷海岳源源崔勍焱白正帅
Owner FUZHOU UNIVERSITY
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