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Nickel-molybdenum bimetallic oxide catalyst, preparation method and application thereof

A bimetallic oxide and catalyst technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., to achieve the effects of low cost, simple operation method and short cycle

Active Publication Date: 2018-07-13
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The successful synthesis of ordered mesoporous nickel-molybdenum bimetallic oxides has not been reported so far

Method used

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  • Nickel-molybdenum bimetallic oxide catalyst, preparation method and application thereof
  • Nickel-molybdenum bimetallic oxide catalyst, preparation method and application thereof
  • Nickel-molybdenum bimetallic oxide catalyst, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] Ordered mesoporous bimetallic nickel-molybdenum oxides were prepared according to the following steps:

[0044] Weigh 8g of P123 into a 500ml beaker, then add 60ml of deionized water, 240ml of 2mol / L hydrochloric acid, and stir at 40°C for 4h. 17gTEOS was slowly added dropwise and continued to stir vigorously at 40°C for 24h. The obtained white turbid liquid was transferred into a high-pressure reaction kettle with a polytetrafluoroethylene inner sleeve, and after being refined at 100°C for 48 hours, it was cooled, washed, and dried. The obtained white solid was calcined at 550° C. for 6 hours with a heating rate of 2° C. / min, and the obtained solid was SBA-15 mesoporous molecular sieve. Small-angle X-ray (SAXRD) and N 2 Adsorption-desorption isotherm characterization, the spectrum is as follows figure 1 and figure 2 shown by figure 1 and figure 2 It can be seen that the prepared SBA-15 has a regular two-dimensional hexagonal mesoporous channel structure, and it...

Embodiment 2

[0049] The synthesis steps of the hard template SBA-15 are the same as in Example 1.

[0050] The synthesis steps of the ordered mesoporous nickel oxide are the same as in Example 1.

[0051] Weigh a certain amount of molybdenum pentachloride and dissolve it in ethanol, stir to obtain a homogeneous solution, then add the prepared mesoporous nickel oxide into the above solution (Ni:Mo molar ratio is 3:2), dry at 40°C and place The ordered mesoporous nickel-molybdenum oxide was obtained by raising the temperature to 400° C. at a rate of 1° C. / min in a muffle furnace and keeping the temperature at this temperature for 2 hours. Its specific surface area is 61m 2 / g. The prepared ordered mesoporous nickel-molybdenum oxide was characterized by TEM and SAXRD, and its TEM photo and SAXRD spectrum are as follows Figure 7 and Figure 8 shown.

[0052] The evaluation of the propane oxidative dehydrogenation performance of the ordered mesoporous nickel-molybdenum oxide is the same a...

Embodiment 3

[0054] The synthesis steps of the hard template SBA-15 are the same as in Example 1.

[0055] The synthesis steps of the ordered mesoporous nickel oxide are the same as in Example 1.

[0056] Weigh a certain amount of molybdenum pentachloride and dissolve it in ethanol, stir to obtain a homogeneous solution, then add the prepared mesoporous nickel oxide into the above solution (Ni:Mo molar ratio is 1:0.5), dry at 40°C and place The ordered mesoporous nickel-molybdenum oxide was obtained by raising the temperature to 400° C. at a rate of 1° C. / min in a muffle furnace and keeping the temperature at this temperature for 2 hours. Its specific surface area is 70m 2 / g. The prepared ordered mesoporous nickel molybdenum oxide 2 Adsorption-desorption and XRD characterization, its N 2 The adsorption-desorption diagram and XRD spectrum are as follows Figure 9 and Figure 10 shown.

[0057] The evaluation of the propane oxidative dehydrogenation performance of the ordered mesopor...

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Abstract

The invention discloses an ordered mesoporous nickel-molybdenum composite oxide catalyst and a preparation method thereof. The material is expected to be used in the reduction of catalytic cracking regenerated flue gas nitrogen oxides or propane oxidative dehydrogenation reaction, and belongs to the field of petrochemical industry. Ordered mesoporous nickel-molybdenum oxide uses mesoporous silicon as a hard template, first prepares ordered mesoporous nickel oxide with nickel nitrate as a precursor, and then prepares ordered mesoporous nickel-molybdenum oxide with ordered mesoporous nickel oxide as a substrate catalyst. The ordered mesoporous nickel-molybdenum oxide catalyst synthesized by this method is suitable for propane oxidative dehydrogenation reaction. The mesoporous metal oxide prepared by the present invention has ordered pores, high specific surface area, and better propane oxidative dehydrogenation performance than bulk nickel molybdenum oxide; meanwhile, the ordered mesoporous nickel oxide substrate prepared by the present invention is a solvent-free It is carried out under certain conditions, the preparation method is simple, the time is short, the yield is high, there is no consumption of solvent such as ethanol, and the cost is low.

Description

technical field [0001] The invention relates to a mesoporous composite metal oxide catalyst and a preparation method thereof, in particular to a preparation method of an ordered mesoporous nickel-molybdenum double metal oxide catalyst. Background technique [0002] Propylene is an important organic raw material second only to ethylene, and is mainly used in the production of chemical products such as polypropylene, acrylonitrile, propylene oxide, acrylic acid, acrolein, phenol and octyl alcohol. In recent years, with the rapid development of my country's petrochemical industry, the demand for propylene has risen linearly. Although my country's propylene production has grown at an average annual rate of 27.1%, it still cannot meet the domestic market demand, and a large amount of propylene still needs to be imported every year. At present, the world's propylene mainly comes from the by-products of fluidized catalytic cracking and steam cracking of hydrocarbons in refineries. ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/889B01J35/04C07C11/06C07C5/333
CPCY02P20/52
Inventor 李玉龙刘坚王斯晗赵震褚洪岭范晓强杜龙弟韦岳长邓旭亮徐显明王薇张志翔苑慧敏张忠涛王凤荣
Owner PETROCHINA CO LTD