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Preparation method and application of Pd/HY molecular sieve and method for selectively loading metal on hierarchical pore molecular sieve

A molecular sieve and selective technology, applied in the direction of molecular sieve catalysts, catalyst activation/preparation, chemical instruments and methods, etc., can solve the problem of low utilization of metal active sites and carrier acid sites, weakening the adsorption of reactants and intermediates, metal - Problems such as poor carrier interaction, to achieve the effect of increased activity, increased accessibility, and small size

Pending Publication Date: 2022-01-28
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0010] Using traditional ion exchange and impregnation methods to prepare zeolite-supported noble metal catalysts will lead to random entry of metals into mesopores and micropores or agglomeration on the surface, resulting in low utilization of metal active sites and acidic sites of the carrier, and low metal-carrier interaction. Poor effect
In addition, the narrow channels of molecular sieves will cause considerable diffusion resistance to macromolecular reactants and hydrogenation products, and will also weaken the adsorption of reactants and intermediates on acidic sites, reducing the yield of target products

Method used

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  • Preparation method and application of Pd/HY molecular sieve and method for selectively loading metal on hierarchical pore molecular sieve
  • Preparation method and application of Pd/HY molecular sieve and method for selectively loading metal on hierarchical pore molecular sieve
  • Preparation method and application of Pd/HY molecular sieve and method for selectively loading metal on hierarchical pore molecular sieve

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] Embodiment 1: (water content 15wt%)

[0048] 10mL Pd(OAc) 2 / CH 2 Cl 2 solution (containing 10.6mg Pd(OAc) 2 ) into a round bottom flask as a hydrophobic solution. Take 450 mg of micro-mesoporous HY molecular sieves calcined in a muffle furnace at 550°C for 4h (the heating rate is 2.5°C / min). Then add 80 μL of ultrapure water and stir to make the water fully contact with the zeolite carrier. The resulting mixture was added to the palladium precursor solution and stirred continuously at room temperature for 24 h. After standing still, the metal precursor solution turns orange to colorless and transparent, and the zeolite precipitate turns yellow or brown. This phenomenon shows that Pd(OAc) 2 Transfer from DCM to HY molecular sieve surface. Then, the dichloromethane was removed by rotary evaporation. The resulting solid was washed with 100 mL CH 2 Cl 2 Wash, filter dry at room temperature, and then dry at 110°C for 12h. The sample powder changed from white to ...

Embodiment 2

[0049] Embodiment 2: (water content 20wt%)

[0050] The specific implementation conditions are similar to Example 1, but the amount of ultrapure water added is 115 μL (the volume of water is equal to the micropore volume of HY). The results of low-temperature nitrogen physical adsorption test show that the specific surface area and micropore volume of Pd / HY(20) are basically similar to those of unsupported HY (Table 1), indicating that palladium metal particles basically do not occupy the micropore channels of the carrier, and more Dispersed in the mesopores and on the outer surface. HAADF-STEM images such as figure 1 As shown in C, the palladium particles are uniformly dispersed on the carrier, and the particle size is 1.53±0.24nm.

Embodiment 3

[0051] Embodiment 3: (water content 30wt%)

[0052] The specific implementation conditions are similar to Example 1, but the amount of ultrapure water added is 200 μL (the volume of water is equal to the total pore volume of HY). The results of low-temperature nitrogen physical adsorption test show that the specific surface area of ​​Pd / HY(30) is larger than that of the original HY zeolite, while the micropore volume remains unchanged (Table 1), indicating that the palladium metal particles do not occupy the micropore channels of the carrier, and all rivets are in the mesopores. and on the outer surface and form a certain degree of accumulation. HAADF-STEM images such as figure 1 As shown in C, the palladium particles are uniformly dispersed on the carrier, and the particle size is 1.74±0.37nm.

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Abstract

The invention discloses a preparation method and application of a Pd / HY molecular sieve and a method for selectively loading metal on a hierarchical pore molecular sieve. The preparation method comprises the following steps: (1) adding a Pd source into a first organic solvent to obtain an organic solution of Pd; (2) pretreating a micro-mesoporous HY molecular sieve; (3) adding water into the pretreated micro-mesoporous HY molecular sieve, and stirring to obtain an HY molecular sieve mixture; (4) mixing the HY molecular sieve mixture with the organic solution of Pd, stirring, and standing to obtain a first mixture; (5) performing rotary evaporation on the first mixture to obtain a first solid; (6) washing the first solid with a second organic solvent, filtering, and drying to obtain a second solid; and (7) roasting the second solid to obtain the Pd / HY molecular sieve. According to the invention, a Pd / HY catalyst is prepared by adopting a double-solvent method, the falling position of metal particles is regulated and controlled by changing the content of water, and the particle size and dispersity of the metal particles are controlled; and the prepared Pd / HY catalyst shows high activity and high decahydronaphthalene selectivity in a naphthalene hydrogenation saturation reaction, and the decahydronaphthalene yield can reach 98% or above.

Description

technical field [0001] The invention relates to the technical field of catalyst preparation, in particular to a preparation method and application of a Pd / HY molecular sieve and a method for selectively loading metals on a multi-stage molecular sieve. Background technique [0002] Zeolite-supported noble metal catalysts have the advantages of high activity, low cost, and good stability, and have been widely used in industry. The tunable acidity and hierarchical channel structure of zeolite have a great influence on the hydrogenation efficiency of aromatic hydrocarbons. The position and distribution of metal nanoparticles in the hierarchical zeolite channel have great influence on particle size, dispersibility, stability, activity, accessibility and Selectivity also plays a key role, which in turn determines the catalytic performance. [0003] Ion exchange and impregnation methods are often used in the preparation of zeolite-supported noble metal catalysts. But during the l...

Claims

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Application Information

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IPC IPC(8): B01J29/12B01J29/44B01J29/74B01J35/00B01J37/00C07C5/10C07C13/48C07C5/11C07C13/50
CPCB01J37/0018B01J29/126B01J29/7415B01J29/44C07C5/10C07C5/11C07C2602/10C07C2602/28B01J2229/186B01J35/393C07C13/48C07C13/50
Inventor 李国柱张香文张明惠王涖王庆法
Owner TIANJIN UNIV