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Core-shell-structured carrier for paraffin isomerization catalyst and preparation method of core-shell-structured carrier

A technology of catalyst carrier and core-shell structure, which is applied in the direction of catalyst carrier, catalyst activation/preparation, physical/chemical process catalyst, etc., can solve problems such as poor stability, reduce residence time, improve anti-carbon performance, and improve The effect of stability

Inactive Publication Date: 2017-12-01
NORTHEAST GASOLINEEUM UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The introduction of other non-noble metals such as Ni, Zn, Mn, etc. can improve the activity of the catalyst, but the stability is not good

Method used

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  • Core-shell-structured carrier for paraffin isomerization catalyst and preparation method of core-shell-structured carrier
  • Core-shell-structured carrier for paraffin isomerization catalyst and preparation method of core-shell-structured carrier
  • Core-shell-structured carrier for paraffin isomerization catalyst and preparation method of core-shell-structured carrier

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Embodiment one: with Al 2 o 3 Preparation of catalyst support with core-shell structure prepared for the core

[0029] This embodiment provides a method for preparing a core-shell structure catalyst carrier, comprising the following steps:

[0030] S1: Using ammonia water with a mole fraction of 6% as the activator and deionized water as the medium, the catalyst carrier Al 2 o 3 The surface is pre-activated for 48 hours, and then dried in an oven at 100°C for 12 hours;

[0031] S2: Add the catalyst carrier Al dried in step S1 to n-butanol solution 2 o 3 , then add a small amount of deionized water and stir for 12 hours to ensure that Al 2 o 3 Completely disperse and make water molecules fully adsorb on Al 2 o 3 Molecular surface, to get Al 2 o 3 suspension;

[0032] S3: Al obtained in step S2 2 o 3 Add zirconium n-butoxide to the suspension, then stir for 5 minutes, then transfer to a high-pressure reactor, and hydrothermally synthesize at 100°C for 48 hou...

Embodiment 2

[0045] Embodiment two: different Al 2 o 3 Preparation of Core-Shell Structured Solid Supercatalyst with Content

[0046] In this example, four different Al 2 o 3 The core-shell structure catalyst carrier of content, specifically comprises the following steps:

[0047] S1: Using ammonia water with a mole fraction of 6% as the activator and deionized water as the medium, the catalyst carrier Al 2 o 3 The surface is pre-activated for 48 hours, and then dried in an oven at 100°C for 12 hours;

[0048] S2: Add the catalyst carrier Al dried in step S1 to n-butanol solution 2 o 3 , then add a small amount of deionized water and stir for 12 hours to ensure that Al 2 o 3 Completely disperse and make water molecules fully adsorb on Al 2 o 3 Molecular surface, to get Al 2 o 3 suspension;

[0049] S3: Al obtained in step S2 2 o 3 Add zirconium n-butoxide to the suspension, then stir for 5 minutes, then transfer to a high-pressure reactor, and hydrothermally synthesize at 1...

Embodiment 3

[0057] Example 3: Preparation of core-shell structure solid super catalysts prepared with different materials as the core

[0058] In this example, HZSM-5, Al 2 o 3 and SiO 2 For catalyst carrier, prepare different core-shell structure catalyst carrier, specifically comprise the following steps:

[0059] S1: Using ammonia water with a mole fraction of 6% as the activator and deionized water as the medium, the catalyst supports HZSM-5, Al 2 o 3 and SiO 2 The surface is pre-activated for 48 hours, and then dried in an oven at 100°C for 12 hours;

[0060] S2: In the n-butanol solution, add the catalyst carrier HZSM-5 and the catalyst carrier Al after drying in step S1 respectively 2 o 3 and catalyst support SiO 2 , then add a small amount of deionized water and stir for 12 hours to ensure that HZSM-5, Al 2 o 3 and SiO 2 Completely disperse and make water molecules fully adsorb on HZSM-5, Al 2 o 3 and SiO 2 Molecular surface, get HZSM-5, Al 2 o 3 and SiO 2 suspens...

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Abstract

The invention relates to a core-shell-structured catalyst carrier and a preparation method thereof. The preparation method comprises the following steps: by taking ammonium hydroxide as an activator and deionized water as a medium, pre-activating the surface of a catalyst carrier X, and then performing drying, wherein the catalyst carrier X is selected from one of HZSM-5, Al2O3 and SiO2; adding the dried catalyst carrier X into a n-butyl alcohol solution, adding deionized water, and performing stirring to obtain a suspension; after that, adding zirconium n-butoxide 80% in n-butanol, performing stirring, and transferring the obtained product into a high-pressure reaction kettle for hydro-thermal synthesis; and performing centrifugal separation after cooling, and drying the collected solid to obtain the core-shell-structured ZrO2@X catalyst carrier. A zirconia-coated aluminium oxide composite is prepared by the hydro-thermal method to synthesize the core-shell- structured catalyst carrier with a continuous membrane layer, and owing to the hydrophobicity of n-butyl alcohol, the loading stability of ZrO2 particles on the surface of the carrier is enhanced, and accordingly, the stability of the core-shell-structured catalyst carrier is improved.

Description

technical field [0001] The invention relates to the technical field of isomerization catalysts used in petrochemical industry, in particular to a core-shell structure carrier for alkane isomerization catalysts and a preparation method thereof. Background technique [0002] In the past ten years, China's automobile production, sales and growth rate have leapt to the forefront of the world and will continue to maintain a high growth trend. At the same time, automobile exhaust emissions have become one of the important sources of pollution to the environment. People pay more and more attention to the use of clean fuel. Europe has successively launched Euro II, Euro III, Euro IV, and Euro-V standards, and higher standards are in the pipeline; the United States, Japan, and South Korea are currently implementing standards similar to Euro-V. China has implemented the China-IV standard which is close to Euro-IV nationwide in 2015, and fully implemented the China-V standard which i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J32/00B01J21/06B01J27/043B01J29/40B01J29/46B01J35/00B01J35/10B01J37/00B01J37/02B01J37/08B01J37/10C10G45/64C10G45/60
CPCC10G45/60C10G45/64B01J21/066B01J27/043B01J29/40B01J29/46B01J37/00B01J37/0201B01J37/0207B01J37/082B01J37/10C10G2300/1081C10G2300/70B01J2229/18B01J35/397B01J35/613B01J35/615B01J35/633B01J35/647
Inventor 宋华李盛楠姜楠胡云峰陈彦广牛瑞霞
Owner NORTHEAST GASOLINEEUM UNIV