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Preparation and application of liquid-phase dehydrogenation catalyst

A dehydrogenation catalyst and catalyst technology are applied in the field of preparation of liquid-phase dehydrogenation catalysts, and can solve the problems of high operating cost, fast catalyst deactivation and high reaction temperature

Active Publication Date: 2020-04-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] The technical problems to be solved by the present invention are problems such as high reaction temperature, fast catalyst deactivation, high operating cost caused by membrane reaction, large equipment investment and difficult maintenance in traditional gas phase dehydrogenation technology. Phase dehydrogenation catalyst and preparation method thereof, when the method is used in the dehydrogenation reaction of organic liquid hydrogen storage materials, the carbon-hydrogen bond can be activated under liquid phase conditions, and the migration and aggregation of noble metals can be prevented, and the stability of the catalyst can be greatly improved

Method used

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  • Preparation and application of liquid-phase dehydrogenation catalyst
  • Preparation and application of liquid-phase dehydrogenation catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] 2g of single-walled carbon nanotubes were placed in a tubular reactor and treated with nitrogen containing 10% HCl. The gas flow rate was 300mL / min, the treatment temperature was 450°C, and the treatment time was 12h. After cooling, it was used as a catalyst carrier.

[0037]Take 0.1244mL of chloroplatinic acid solution with a concentration of 16.14mL / L, add 0.378mL of water to prepare a solution, add 2g of the above-mentioned carrier to this solution, stir, leave at room temperature for 2h, then dry at 120°C for 4h, and finally put it The catalyst was calcined at 500°C for 4 h in a muffle furnace under N2 atmosphere. The catalyst composition is shown in Table 1.

[0038] The obtained catalyst was pressed into tablets, ground into a particle size of 12-20 mesh, and 1 gram was taken for evaluation in an isothermal fixed-bed reactor. Before the evaluation, it was reduced with hydrogen. The reduction conditions were as follows: normal pressure, temperature 450°C, hydrogen ...

Embodiment 2

[0040] 2g of single-walled carbon nanotubes were placed in a tubular reactor and treated with nitrogen containing 10% HCl. The gas flow rate was 300mL / min, the treatment temperature was 450°C, and the treatment time was 12h. After cooling, it was used as a catalyst carrier.

[0041] Take 0.622mL of chloroplatinic acid solution with a concentration of 16.14mL / L, add 0.378mL of water to prepare a solution, add 2g of the above-mentioned carrier to the solution, stir, and place at room temperature for 2h, then dry at 120°C for 4h, and finally put it The catalyst was calcined at 500° C. for 4 h in a muffle furnace with N2 atmosphere. The catalyst composition is shown in Table 1.

[0042] Take 1 g of the catalyst for evaluation in an isothermal fixed-bed reactor, and reduce it with hydrogen before the evaluation. The reduction conditions and evaluation conditions are the same as in Example 1. The preparation method and test results of the catalyst are shown in Table 2.

Embodiment 3

[0044] 2g of single-walled carbon nanotubes were placed in a tubular reactor and treated with nitrogen containing 10% HCl. The gas flow rate was 300mL / min, the treatment temperature was 450°C, and the treatment time was 12h. After cooling, it was used as a catalyst carrier.

[0045] Take 0.622mL of chloroplatinic acid solution with a concentration of 32.28mL / L, add 0.378mL of water to prepare a solution, add 2g of the above-mentioned carrier to this solution, stir, and place it at room temperature for 2h, then dry it at 120°C for 4h, and finally put it The catalyst was calcined at 500° C. for 4 h in a muffle furnace with N2 atmosphere. The catalyst composition is shown in Table 1.

[0046] Take 1g of the catalyst for evaluation in an isothermal fixed-bed reactor, and reduce it with hydrogen before the evaluation. The reduction conditions and evaluation conditions are the same as in Example 1. The preparation method and test results of the catalyst are shown in Table 2.

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Abstract

The invention discloses preparation and application of a liquid-phase dehydrogenation catalyst, which comprises the following components: (a) 0.01-5 parts of at least one metal or alloy thereof selected from group VIII noble metal elements in the periodic table of elements, wherein the metal or alloy is used as an active metal; and (b) 70-95 parts of a compound formed by a halogen element and a carbon nano tube, wherein the compound is used as a carrier. The dehydrogenation catalyst is prepared by the following steps: (1) carrying out a halogen element treatment on a carbon material to obtaina carrier, and (2) dissolving a salt of a VIII group noble metal element in water, and loading the salt on the carrier by adopting a saturated impregnation method to obtain the catalyst. When the dehydrogenation catalyst is applied to liquid-phase dehydrogenation of hydrogen storage compounds, the catalyst has higher stability.

Description

technical field [0001] The invention discloses the preparation and application of a liquid-phase dehydrogenation catalyst, in particular a liquid-phase dehydrogenation catalyst for organic liquid hydrogen storage materials and a preparation method thereof. Background technique [0002] In recent years, the rapid consumption of fossil resources has not only threatened the energy security of human society, but also caused irreversible harm to the environment. These have forced human beings to establish a new sustainable new energy system to solve the problems of fossil energy. . Among many new energy sources, hydrogen energy is clean, efficient, and has high energy density, and is considered to be the ultimate goal of replacing fossil energy. From the development to the application of hydrogen energy, it is necessary to establish a perfect hydrogen storage and transportation method. However, so far, hydrogen, as a promising new energy source, has not been commercially applied...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/42B01J23/44C07C11/09C07C11/08C07C13/20C07C15/24C07C5/333C07C5/32
CPCB01J23/42B01J23/44C07C5/3337C07C5/325C07C2523/42C07C2523/44C07C2601/16C07C2602/10C07C11/09C07C11/08C07C13/20C07C15/24Y02E60/32
Inventor 童凤丫孙清邵一凡缪长喜
Owner CHINA PETROLEUM & CHEM CORP