Nickel-based high dispersion emulsion catalyst, preparation method and application thereof

A catalyst and high-dispersion technology, applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, physical/chemical process catalysts, etc., can solve the problems of unsuitability for large-scale industrial production, large amount of acid catalyst addition, poor catalyst dispersion performance, etc. problem, to achieve the effect of simplifying the multi-stage emulsification and dispersion process, good coke suppression effect and low use cost

Pending Publication Date: 2019-02-01
CHINA UNIV OF PETROLEUM (EAST CHINA)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Supported catalysts and solid particle catalysts have poor dispersion performance; acidic catalysts are added in a large amount and are corrosive, which is not suitable for large-scale industrial production; oil-soluble catalysts have good dispersion effec

Method used

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  • Nickel-based high dispersion emulsion catalyst, preparation method and application thereof
  • Nickel-based high dispersion emulsion catalyst, preparation method and application thereof
  • Nickel-based high dispersion emulsion catalyst, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] A nickel-based high-dispersion emulsion catalyst, the catalyst active component is nickel, the weight content of nickel in the catalyst is 5.01%, and its preparation method is as follows:

[0029] (1) Take 13.84g Ni(NO 3 ) 2 ·6H 2 O, 0.40g sodium lauryl sulfonate, add 4.27g deionized water;

[0030] (2) Take another 0.80g Span-80, add 30g 400N base oil, heat to 70°C and stir at a shear speed of 2000r / min; 150N base oil, 400N base oil, clay refined wax oil

[0031] (3) Slowly add the water phase into the container containing the oil phase, shear and disperse at 70°C for 10 minutes, the dispersion speed is 2000r / min, cool to room temperature after the dispersion is completed, and it is a nickel-based high-dispersion emulsion catalyst.

Embodiment 2

[0033] A nickel-based high-dispersion emulsion catalyst, the catalyst active component is nickel, the weight content of nickel in the catalyst is 5.01%, and its preparation method is as follows:

[0034] (1) Get 13.84g nickel carbonate, 0.60g sodium dodecylbenzenesulfonate, add 43.3g deionized water;

[0035] (2) Take another 0.60g of Span-85, add 30g of 150N base oil, heat to 50°C and stir at a shear speed of 4000r / min;

[0036] (3) Slowly add the water phase into the container containing the oil phase, shear and disperse at 50°C for 15 minutes, and disperse at a speed of 1000r / min. After the dispersion is completed, cool to room temperature, which is a nickel-based high-dispersion emulsion catalyst.

Embodiment 3

[0038] A nickel-based highly dispersed emulsion catalyst, the catalyst active component is nickel, and the weight content of nickel in the catalyst is 6.04%. Its preparation method is as follows:

[0039] (1) Get 17.63g nickel chloride, 0.24g cetyltrimethylammonium bromide and 0.24g Tween-80, add 10g deionized water;

[0040] (2) Take another 0.72g of oleic acid, add 30g of clay refined wax oil, heat to 80°C and stir at a shear speed of 1000r / min;

[0041] (3) Slowly add the water phase into the container containing the oil phase, shear and disperse at 80°C for 5 minutes at a dispersing speed of 4000r / min, cool to room temperature after dispersing, and it becomes a nickel-based high-dispersion emulsion catalyst.

[0042] The stability parameters of the prepared catalysts are shown in Table 1.

[0043] Table 1 catalyst stability data

[0044] Catalyst name

Stable parameter / % after standing for 5 days

Stable parameter / % after standing for 15 days

Exampl...

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Abstract

The invention discloses a nickel-based high dispersion emulsion catalyst, a preparation method and application thereof. The preparation method comprises the steps of: (1) heating and dissolving a hydrophilic surfactant and a nickel salt in a 0.3-3 times mass of deionized water; (2) putting an oleophylic surfactant and wax oil into a condenser, performing heating to 50-80DEG C, and conducting stirring under a rotating speed of 1000-4000r/min; and (3) when the oil phase reaches a required temperature, adding the water phase slowly into the container, performing shearing dispersion under a constant temperature condition for 5~15min, and then conducting cooling to room temperature, thus obtaining the nickel-based high dispersion emulsion catalyst. The deionized water introduced into the catalyst prepared by the invention has no need for removal, the problem of large water removal energy consumption in a slurry bed hydrogenation process of the previous water-soluble catalysts can be avoided, the operation efficiency is improved, and the catalyst also has the advantages of good dispersion effect in raw materials, high hydrogenation activity, good coke suppression effect and high coal conversion rate.

Description

technical field [0001] The invention relates to the technical field of catalysts, in particular to a nickel-based highly dispersed emulsion catalyst and a preparation method and application thereof, which are suitable for hydrogenation co-refining of different coal types and heavy oil. Background technique [0002] my country's energy resource structure is characterized by poor oil, little gas, and rich coal. 70% of these primary energy sources are coal, and nearly 80% of them are converted into secondary energy sources such as electric energy and heat energy through direct combustion. The conversion efficiency is low, and there are serious ecological and environmental problems. In recent years, the world's petroleum resources tend to be heavy and inferior, and the proportion of heavy crude oil continues to increase. The petroleum industry and chemical industry increasingly need to develop heavy oil processing technology. Coal / heavy oil hydroprocessing co-smelting technology...

Claims

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Application Information

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IPC IPC(8): B01J31/28C10G1/06C10G1/08C10G47/02C10G49/04
CPCB01J31/28C10G1/06C10G1/086C10G47/02C10G49/04C10G2300/10
Inventor 李传符欣怡邓文安王兴兆杜峰刘超李庶峰任志祥
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)
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