Catalyst with active component nano particles embedded in molecular sieve to crystallize, method and application

A technology of nanoparticles and active components, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of high n-aldehyde selectivity, large particle size, low catalytic activity, etc., to prevent active components The effects of separation loss, good mechanical stability and long catalyst life

Inactive Publication Date: 2013-05-15
BEIJING UNIV OF CHEM TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this type of supported catalyst has the following defects: 1) most of the active metals are located on the outer surface of the molecular sieve; 2) the particle size is large; 3) the metal active center and the acid center cannot be effectively matched, and the heavy component product cannot be effectively cracked; 4) due to the metal Strong interaction with molecular sieves, resulting in low catalytic activity, poor metal reduction, and high methane selectivity
However, such molecular sieve membrane catalysts have the following defects: 1) Generally, they are directly constructed on the surface of millimeter-scale nuclear catalysts, and the presence of molecular sieve membranes will increase CO and H 2 2) The preparation process of molecular sieve membranes is complex and often requires various pretreatment processes. The formation of molecular sieve membranes requires good compatibility between c

Method used

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  • Catalyst with active component nano particles embedded in molecular sieve to crystallize, method and application
  • Catalyst with active component nano particles embedded in molecular sieve to crystallize, method and application
  • Catalyst with active component nano particles embedded in molecular sieve to crystallize, method and application

Examples

Experimental program
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Embodiment 1

[0047] A method for preparing a catalyst in which active component nanoparticles are embedded in molecular sieve crystals, comprising the following steps:

[0048] 1) Co / SiO2 2 Existing Equal Volume Impregnation Preparation of Precursor Catalysts:

[0049] SiO 2 Treated in air at 200°C for 2h, then treated with Co(NO 3 ) 2 ·6H 2 O is the impregnation of the same volume as the Co source, the active metal Co loading is 20wt%, vacuum treatment for 1h, drying at 120°C for 12h, and roasting at 400°C for 2h to obtain the precursor particle catalyst; crush and screen the precursor particle catalyst to pass 80 mesh powder;

[0050] 2) TPAOH was used as template, and Al(NO 3 ) 3 9H 2 O is the source of Al, with Co / SiO 2 The Si dissolved out during the synthesis is used as the Si source;

[0051] Al(NO 3 ) 3 9H 2 O is dissolved in deionized water and ethanol (abbreviation: EtOH), and after stirring evenly, add the precursor catalyst powder obtained in step 1), add the templ...

Embodiment 2

[0059]A method for preparing a catalyst in which active component nanoparticles are embedded in molecular sieve crystals, comprising the following steps:

[0060] 1) Co / Al 2 o 3 Existing Equal Volume Impregnation Method Preparation of Precursor Catalysts

[0061] γ-Al 2 o 3 Treated in air at 200°C for 2h, then treated with Co(NO 3 ) 2 ·6H 2 O is impregnated with an equal volume of Co source, the active metal Co loading is 20wt%, vacuum treatment for 1h, drying at 120°C for 12h, and calcination at 400°C for 2h to obtain a precursor catalyst; crush and sieve the obtained precursor catalyst into a 20-mesh powder ;

[0062] 2) TPAOH was used as template, TEOS was used as Si source, and Co / Al 2 o 3 The Al dissolved during the synthesis process is used as the Al source;

[0063] Mix TEOS with deionized water and ethanol, stir evenly, add the precursor catalyst powder obtained in step 1), and then add template agent drop by drop, stir and mix evenly to obtain a synthetic so...

Embodiment 3

[0072] A method for preparing a catalyst in which active component nanoparticles are embedded in molecular sieve crystals, comprising the following steps:

[0073] Preparation of Co-Zr / SiO by Traditional Equal Volume Impregnation Method 2 catalyst:

[0074] SiO 2 Treated in air at 200°C for 2h, then treated with Co(NO 3 ) 2 ·6H 2 O and Zr(NO 3 ) 4 ·5H 2 O aqueous solution impregnated the equal volume, the active metal Co loading was 20wt%, the additive Zr loading was 6wt%, vacuum treatment for 1h, drying at 120°C for 12h, calcination at 400°C for 2h, to obtain Co-Zr / SiO 2 Precursor catalyst; Gained precursor catalyst is crushed and sieved into 60-mesh powder;

[0075] The rest of the operation steps are the same as in Example 1, and a novel structure Co-Zr·HZSM-5 molecular sieve catalyst is prepared. The Co-Zr·HZSM-5 catalyst includes Co active component nanoparticles, Zr additive particles and HZSM-5 molecular sieve, the Co active component nanoparticles are embedded...

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Abstract

The invention discloses a catalyst with active component nano particles embedded in a molecular sieve to crystallize. The catalyst comprises metal active component nano particles and a molecular sieve, the catalyst comprises metal active component nano particles are embedded and dispersed in the molecular sieve, the content of the active component nano particles in the catalyst is 2-70wt%, the particle size of the active component nano particles is 4-200nm, the crystal grain size of the molecular sieve is 1-10mu m; and the invention further discloses a preparation method and an application of the catalyst. The active metal in the catalyst disclosed by the invention is embedded and dispersed in the molecular sieve, the particle size is small; the metal active centre is effectively matched with an acid centre, the heavy constituent product can be effectively cracked; the catalytic activity is high, the metal reducibility is high, and the methane selectivity is low; the Fischer-Tropsch reaction activity cannot be reduced; the preparation process is simple, the cost is recued, and the catalyst is suitable for large industrial application; and the molecular sieve cannot break due to the difference of thermal coefficients of expansion, and the mechanical strength is high.

Description

technical field [0001] The invention relates to a catalyst, a preparation method and its application; in particular, it relates to a catalyst, a method and an application in which active component nanoparticles are embedded in molecular sieve crystals. Background technique [0002] Under the background of the gradual scarcity of world oil resources and the increasingly prominent energy crisis, carbon-chemical (C 1 Chemistry) has been extensively researched and developed rapidly. The carbon chain growth process of synthesizing and preparing organic compounds containing two or more carbon atoms from compounds with only one carbon atom (such as CO, methane, methanol, hydrocyanic acid, etc.) is called carbon-one chemistry. Carbon-chemical raw materials have a wide range of sources, which can reduce the excessive dependence on petroleum resources. It is the most important and promising way to replace petroleum synthesis routes to prepare basic organic chemical raw materials, fue...

Claims

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Application Information

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IPC IPC(8): B01J29/46B01J29/48B01J29/76B01J29/44B01J29/03B01J29/89B01J29/85C10G2/00C07C1/04C07C43/04C07C41/01
Inventor 张燚刘江永陈建峰
Owner BEIJING UNIV OF CHEM TECH
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