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A kind of preparation method of noble metal @zsm core-shell structure catalyst

A core-shell structure and catalyst technology, which is applied in the field of preparation of noble metal@ZSM core-shell structure catalysts, can solve the problems of inability to achieve fine desulfurization, limited adsorption performance, and lack of noble metal active sites, so as to improve desulfurization efficiency and service life. Implementation, high success rate effect

Active Publication Date: 2021-08-27
HENAN SHENMA CATALYTIC TECH CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this type of catalyst is not suitable for adsorption and desulfurization of sulfur-containing benzene liquid, because the active components of noble metals are exposed to the outer surface during use, and the adsorbed sulfide is very easy to desorb, so that fine desulfurization cannot be achieved. However, if the molecular sieve adsorbent is simply used, the adsorption performance is very limited due to the lack of active sites of noble metals.

Method used

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  • A kind of preparation method of noble metal @zsm core-shell structure catalyst
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  • A kind of preparation method of noble metal @zsm core-shell structure catalyst

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preparation example Construction

[0027] A preparation method of a noble metal@ZSM core-shell structure catalyst, comprising the following steps:

[0028] Step 1: Add the first base compound to the first part of water and stir, after dissolving, add CO-520 and cyclohexane with a volume ratio of 1: (2~3) and continue to stir evenly to form microemulsion A;

[0029] Step 2: Add an appropriate amount of hydrochloric acid and the second part of water to the noble metal salt and stir. After dissolving, add CO-520 and cyclohexane with a volume ratio of 1: (2~3) and continue stirring to form a microemulsion B;

[0030] Step 3: Mix microemulsion A with microemulsion B, add an appropriate amount of the second alkali compound after stirring for a period of time, continue stirring for a period of time, slowly add an organic amine template and stir evenly to obtain microemulsion C;

[0031] Step 4: Add a certain amount of aluminum source compound to microemulsion C under stirring, after the aluminum source is evenly dispe...

Embodiment 1

[0046] Add 2.9 g of NaOH to 650 ml of water and stir. After dissolving, add 850 ml of CO-520 and 2550 ml of cyclohexane and continue to stir evenly to form a microemulsion A; Add 0.5ml of hydrochloric acid and 450ml of water to copper nitrate and stir. After dissolving, add 850ml of CO-520 and 2550ml of cyclohexane and continue to stir evenly to form microemulsion B; mix microemulsion A with microemulsion B, and then add 19 ml concentrated ammonia water, continue to stir for a period of time, slowly add 25.0g TPAOH and stir evenly to obtain microemulsion C; add 6.3 g aluminum isopropoxide to microemulsion C under stirring, after the aluminum isopropoxide is uniformly dispersed, slowly Add 320 g TEOS, continue to stir until it becomes white emulsion, then transfer it to a hydrothermal synthesis kettle, and crystallize at 150°C for 72 hours; the crystallized material is separated from solid and liquid, washed, and put into an oven for 5 The temperature was raised to 100°C for 2 ...

Embodiment 2

[0048] Add 2.7 g of NaOH to 400 ml of water and stir. After dissolving, add 800 ml of CO-520 and 1600 ml of cyclohexane and continue stirring to form a microemulsion A; add 1.0 g of ruthenium chloride, 5.4 g of cerium nitrate hexahydrate and 2.1 g of silver nitrate Add 300ml of water and stir. After dissolving, add 1200ml of CO-520 and 2400ml of cyclohexane and continue to stir evenly to form microemulsion B; mix microemulsion A with microemulsion B, add 12 ml of concentrated ammonia after stirring for a while, continue After stirring for a period of time, slowly add 15.7g of TPAOH and stir evenly to obtain microemulsion C; add 7.9 g of aluminum isopropoxide to microemulsion C under the action of stirring, after the aluminum isopropoxide is uniformly dispersed, slowly add 320 g of TEOS, continue Stir until it becomes a white emulsion, then transfer it to a hydrothermal synthesis kettle, and crystallize at 150°C for 72 hours; the crystallized material is separated from solid and...

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Abstract

The invention discloses a preparation method of a noble metal@ZSM core-shell structure catalyst. The noble metal is used as an active component, and an auxiliary metal salt can be selectively added, and CO-520 and cyclohexane are added to the precursor, so that the noble metal salt and The auxiliary metal salt can form a microemulsion, and then add the raw materials prepared by ZSM-5 molecular sieve, so that the groups in the metal salt microemulsion can combine with the hydroxyl groups of the molecular sieve, and finally through hydrothermal crystallization, filtration washing, drying, and roasting After obtaining the core-shell structure, the catalyst can play a catalytic role by further reducing the noble metal. The preparation method of the present invention is used to form a specific catalyst core-shell structure, and the molecular sieve is used to protect the noble metal active component inside, and the molecular sieve and the active component form a cascade catalytic effect, thereby improving the catalytic performance, especially suitable for trace sulfide in benzene removal.

Description

technical field [0001] The invention belongs to the technical field of chemical industry, and in particular relates to a preparation method of a noble metal@ZSM core-shell structure catalyst. Background technique [0002] Noble metals have excellent catalytic effects on various reactions including hydrogenation and adsorption, and are widely used in chemical industry. In order to improve the catalytic effect of noble metals, the noble metals are usually loaded on the carrier. On the one hand, the carrier forms a support for it, and on the other hand, it is beneficial to the dispersion of the noble metals. However, this type of catalyst is not suitable for adsorption and desulfurization of sulfur-containing benzene liquid, because the active components of noble metals are exposed to the outer surface during use, and the adsorbed sulfide is very easy to desorb, so that fine desulfurization cannot be achieved. However, if molecular sieve adsorbents are simply used, the adsorpt...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/44B01J29/46C07C7/163C07C15/04
CPCB01J29/46B01J29/44C07C7/163B01J2229/186B01J35/391B01J35/398C07C15/04Y02P20/52
Inventor 靳鹏梁巍李世强王跃辉张红卫郑晓广王子昊王东江何聪聪
Owner HENAN SHENMA CATALYTIC TECH CO LTD