Method for immediately eliminating carbon monoxide poisoning of metal catalyst in heterogeneous catalytic hydrogenation and application

A metal catalyst, carbon monoxide technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, catalyst regeneration/reactivation, physical/chemical process catalyst, etc., can solve the deactivation of hydrogenation metal catalyst, poisoning deactivation, etc. problems, to achieve the effect of increased conversion and selectivity, improved activity and selectivity, and simple operation

Pending Publication Date: 2021-11-26
XIAMEN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In some catalytic hydrogenation industrial processes, although the use of crude hydrogen as a hydrogen source has the characteristics of simple industrial equipment and higher economic efficiency, a small amount of carbon monoxide (from tens to thousands of ppm) will cause the hydrogenation metal catalyst to deactivate, because there is a strong interaction between carbon monoxide and the metal active center, which quickly occupies the catalytic active site during the catalytic reaction, so that the reactant molecules cannot be adsorbed on the surface of the catalyst. Inactivation by poisoning (B.Campo, C.Petit, A.María, Hydrogenation of crotonaldehyde on different Au / CeO 2 catalysts.[J].J.Catal.,2008,254(1):71-78; A.Waghray,D.G.Blackmond,Infraredspectros carbon monoxide pic studies of the absorption and reaction of 3-methyl-2-butenal over alkali-promoted Ru / SiO 2 catalysts.[J].J.Phys.Chem.,1993,97(22):6002-6006.)

Method used

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  • Method for immediately eliminating carbon monoxide poisoning of metal catalyst in heterogeneous catalytic hydrogenation and application
  • Method for immediately eliminating carbon monoxide poisoning of metal catalyst in heterogeneous catalytic hydrogenation and application
  • Method for immediately eliminating carbon monoxide poisoning of metal catalyst in heterogeneous catalytic hydrogenation and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] The preparation steps of catalyst are as follows:

[0023] 1.0g iridium acetylacetonate Ir (acac) 3 Dissolved in acetylacetone to obtain 3.9264mg / mL Ir(acac) 3 The precursor solution; 0.190g of SiO 2 Carrier was added to 2.547mL Ir(acac) 3 Precursor solution, the resulting mixture was stirred and ultrasonicated for 20 minutes, transferred to a dark place for 24 hours, then placed in an oven and dried at 383K for 3 hours, and finally the obtained solid was calcined in a muffle furnace, heated to 773K at a rate of 2K / min and Keep it for 3h, and after cooling down, you can get 0.2g 5%Ir / SiO 2 catalyst.

[0024] The specific reaction steps of catalytic gas-phase selective hydrogenation of crotonaldehyde to produce crotyl alcohol are as follows: Catalyst activity evaluation is carried out on a fixed-bed device at normal pressure, and 25 mg of 5% Ir / SiO 2 The catalyst was loaded into a quartz reaction tube, and the high-purity H at 10 mL / min 2 Under the air flow, the te...

Embodiment 2

[0026] The preparation steps of the catalyst are the same as in Example 1, and the reaction conditions for the gas-phase selective hydrogenation of catalyzed crotonaldehyde to produce crotyl alcohol refer to Example 1, the difference is that high-purity H 2 into H containing traces of carbon monoxide 2 Mixed gas (concentration of carbon monoxide is 100ppm), all the other conditions are with embodiment 1. The evaluation results are shown in Table 1. When hydrogen gas similar to crude hydrogen (containing low-concentration carbon monoxide) is used as the hydrogen source, the conversion rate of crotonaldehyde is only 1.2%, and the selectivity of the product crotyl alcohol is 72.5%.

Embodiment 3

[0028] The catalyst deactivated by carbon monoxide poisoning in Example 2 is activated, and the activation gas contains O 2 and H 2 Mixed gas (O 2 The concentration of crotonaldehyde is 0.02%), the activation temperature is 423K, and the activation time is 2h; after the activation finishes, the reaction conditions of catalytic crotonaldehyde gas-phase selective hydrogenation to produce crotyl alcohol are the same as in Example 1, and the reaction results are shown in Table 1. The conversion rate of crotonaldehyde is 48.1%, the selectivity of product crotyl alcohol is 91.5%.

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Abstract

The invention discloses a method for immediately eliminating carbon monoxide poisoning of a metal catalyst in heterogeneous catalytic hydrogenation, which comprises the following steps: when a heterogeneous hydrogenation reaction is catalyzed by using the metal catalyst in a gas or liquid flow dynamic environment, carbon monoxide poisoning of the metal catalyst can be eliminated or prevented by introducing a small amount of oxidizing gas into a reaction system. According to the method provided by the invention, after a trace amount of oxygen or oxidizing gas is doped into a reaction atmosphere, carbon monoxide adsorbed on the surface of the catalyst can be preferentially oxidized to generate carbon dioxide and is quickly desorbed, and poisoned active sites are released, so that the catalytic hydrogenation capacity of the catalyst is recovered. The method provided by the invention is applied to unsaturated aldehyde or ketone selective hydrogenation reaction, ester catalytic selective hydrogenation reaction and lignin oxygen-containing compound hydrogenolysis reaction. The method not only improves the catalytic activity and selectivity, but also improves the stability and service life of the catalyst. In addition, the method also has the advantages of simple operation and good repeatability.

Description

technical field [0001] The invention belongs to the technical field of catalyst application, and in particular relates to a method and application for instantly eliminating carbon monoxide poisoning of metal catalysts in situ in heterogeneous catalytic hydrogenation. Background technique [0002] Catalytic reaction processes are important processes in modern industry and are key steps in the production of clean fuels and advanced chemicals. In some catalytic hydrogenation industrial processes, although the use of crude hydrogen as a hydrogen source has the characteristics of simple industrial equipment and higher economic efficiency, a small amount of carbon monoxide (from tens to thousands of ppm) will cause the hydrogenation metal catalyst to deactivate, because there is a strong interaction between carbon monoxide and the metal active center, which quickly occupies the catalytic active site during the catalytic reaction, so that the reactant molecules cannot be adsorbed o...

Claims

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Application Information

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IPC IPC(8): C07C29/141C07C29/149C07C29/20C07C1/22B01J23/755B01J23/72B01J23/46B01J38/04B01J38/14C07C33/03C07C31/20C07C13/18C07C35/08C07B35/02C07B41/02
CPCC07C29/141C07C29/149C07C1/22C07C29/20B01J23/468B01J23/72B01J23/755B01J38/14B01J38/04C07B35/02C07B41/02C07C2601/14C07C33/03C07C31/202C07C13/18C07C35/08Y02P20/584
Inventor 林海强陈建许康段新平袁友珠
Owner XIAMEN UNIV
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