Reduction state hydrogenation catalyst and preparation method thereof

A technology of hydrogenation catalyst and hydrogenation activity, which is applied in the direction of catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalyst, etc. gender issues

Active Publication Date: 2020-07-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Precious metal catalysts have strong olefins and aromatics saturation capabilities, and achieve ideal results in the hydrogenation and decolorization of petroleum resins. However, precious metal catalysts have the following disadvantages: first, the preparation cost of precious metal catalysts is much higher than that of non-precious metal catalysts; secondly, precious metal catalysts Catalysts have very strict requirements on the impurity content in the raw material, especially the sulfur content in the raw material.
[0006] CN103386302A discloses a kind of petroleum resin hydrogenation catalyst, with Al 2 o 3 As a carrier, loaded with precious metal Pd and oxide additives, metal palladium microcrystals with a particle size of less than 3nm accounted for more than 90%. 2- Poor tolerance and easy poisoning deactivation, catalyst life is affected
However, the above-mentioned catalysts are catalysts in an oxidized state, and need to be reduced before the reaction in order to exert their hydrogenation activity, and the use steps are cumbersome.

Method used

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  • Reduction state hydrogenation catalyst and preparation method thereof
  • Reduction state hydrogenation catalyst and preparation method thereof
  • Reduction state hydrogenation catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0055] (1) Catalyst preparation

[0056] Weigh 120g of ammonium phosphate, dissolve it in 400mL of deionized water to obtain solution A; grind 200g of petroleum coke into powder, then add it to solution A, let it stand for 1.5h, then filter, and put the obtained solid sample in an oven at 110°C Dry for 5h. At 200°C, pretreat the dried solid sample with water vapor for 3 hours (the volumetric space velocity of the water vapor gas is 1200 hours -1 ), then raise the temperature to 400°C, continue pretreatment for 3h, and then cool to 60°C under nitrogen protection to obtain pretreated petroleum coke.

[0057] Mix 189.1g of nickel nitrate and 33.0g of ferric nitrate, 200g of the above-mentioned pretreated petroleum coke and 400g of potassium hydroxide, and place them in a microwave heating furnace with a microwave frequency of 2450MHz. Then, the temperature was raised to 500°C and kept constant for 40 minutes, then nitrogen gas was introduced to normal pressure, and the temperat...

Embodiment 2

[0062] (1) Catalyst preparation

[0063] Weigh 100g of diammonium hydrogen phosphate, dissolve it in 400mL of deionized water to obtain solution A; grind 200g of petroleum coke to powder, then add it to solution A, leave it for 1.5h, then filter, and put the obtained solid sample in an oven at 110 Dry at ℃ for 5h. At 200°C, use water vapor to pretreat the dried solid sample for 3 hours (the volumetric space velocity of the water vapor gas is 1000h -1 ), then raise the temperature to 400°C, continue pretreatment for 3h, and then cool to 60°C under nitrogen protection to obtain pretreated petroleum coke.

[0064] Mix 247.5g of nickel nitrate, 48.0g of ferric nitrate, 200g of the above-mentioned pretreated petroleum coke and 600g of potassium hydroxide evenly, place it in a microwave heating furnace with a microwave frequency of 2450MHz, and vacuum it under the condition that the microwave power is 0.3kw Then, the temperature was raised to 600°C and kept constant for 20 minutes...

Embodiment 3

[0069] (1) Catalyst preparation

[0070] Weigh 80g of ammonium dihydrogen phosphate, dissolve it in 400mL of deionized water to obtain solution A; grind 200g of petroleum coke to powder, then add it to solution A, leave it for 1.5h, then filter, and put the obtained solid sample in an oven at 110 Dry at ℃ for 5h. At 200°C, pretreat the dried solid sample with water vapor for 3 hours (the volumetric space velocity of the water vapor gas is 800 hours -1 ), then raise the temperature to 400°C, continue pretreatment for 3h, and then cool to 60°C under nitrogen protection to obtain pretreated petroleum coke.

[0071] Mix 317.7g of nickel nitrate, 65.9g of ferric nitrate, 200g of the pretreated petroleum coke obtained above and 800g of potassium hydroxide evenly, place in a microwave heating furnace with a microwave frequency of 2450MHz, and vacuumize it under the condition that the microwave power is 0.3kw Then, the temperature was raised to 400°C and kept constant for 60 minutes...

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Abstract

The invention discloses a reduction state hydrogenation catalyst and a preparation method thereof. The reduction state hydrogenation catalyst comprises a hydrogenation active metal component, an auxiliary agent and a carrier, wherein the hydrogenation active metal component is nickel oxide, the auxiliary agent is one or more of IIA group alkaline earth metal, IB group transition metal, IIB group transition metal, VIII group transition metal and lanthanide series metal, and the carrier is petroleum coke-based activated carbon. The preparation method comprises the following steps: uniformly mixing petroleum coke, metal soluble salt containing hydrogenation activity, metal soluble salt containing auxiliaries and an activating agent, and activating same; carrying out steam treatment on the obtained sample; cooling, introducing oxygen-containing gas for treatment, and finally washing and drying to obtain the reduction-state hydrogenation catalyst. According to the catalyst, petroleum coke-based activated carbon is used as a carrier, so that dispersion of active metal components is facilitated, more high-hydrogenation activity centers are easy to form, and the catalyst has higher hydrogenation activity.

Description

technical field [0001] The invention belongs to the technical field of oil refining and chemical industry, and relates to a catalytic material and a preparation method thereof, in particular to a reduced state hydrogenation catalyst and a preparation method thereof. Background technique [0002] Petroleum resin is a functional resin with a relatively low molecular weight, which has the characteristics of thickening, cohesiveness and compatibility with other resins. Widely used in coatings, adhesives, printing inks, rubber additives, paper additives and other fields. Petroleum resin can be divided into C and C according to different raw materials and properties. 5 Petroleum resin, C 9 Petroleum resin, C 5 -C 9 Copolymerized petroleum resin, etc. At present, the main source of preparing petroleum resin is the by-product of petroleum cracking ethylene. Due to the difference of cracking raw material and cracking depth, the output of this by-product is generally 10% to 20% o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J23/78B01J35/10B01J37/02B01J37/10B01J37/28B01J37/34C08F8/04C08F240/00
CPCB01J23/755B01J23/78B01J37/343B01J37/0201B01J35/1023B01J35/1047B01J37/10B01J37/28C08F8/04C08F240/00Y02P20/52
Inventor 刘璐金浩朱慧红杨光孙素华杨涛
Owner CHINA PETROLEUM & CHEM CORP
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