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Catalyst carrier with temperature adjustment function and preparation method of catalyst carrier

A technology of catalyst carrier and temperature adjustment, which is applied in the direction of catalyst carrier, chemical instruments and methods, physical/chemical process catalysts, etc., which can solve the problems of limited use occasions and limited use, and achieve the effect of reducing costs and reducing environmental pollution

Active Publication Date: 2019-12-20
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, since the reaction temperature of most catalytic reactions is lower than 450 °C, and there are few catalyst systems that use Ni, Fe or Cu oxides as the carrier to support active components, the above-mentioned "high temperature phase change heat storage composite catalyst carrier" Use cases are very limited
In addition, the preparation method provided by the above-mentioned patent requires the use of thermite reaction, which can only be adapted to the preparation of a carrier whose core is Al, which limits the use of this method

Method used

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  • Catalyst carrier with temperature adjustment function and preparation method of catalyst carrier
  • Catalyst carrier with temperature adjustment function and preparation method of catalyst carrier
  • Catalyst carrier with temperature adjustment function and preparation method of catalyst carrier

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Example 1 SiO 2 Coated Sn 0.99 Cu 0.01 Preparation of Alloy Powder as Catalyst Carrier with Temperature Regulating Function

[0029] 1) Weigh 30g of pre-prepared LiNO 3 -NaNO 3 -KNO 3 eutectic mixture (melting point about 120 °C) and 6 g of Sn prepared by high-temperature melting 0.99 Cu 0.01 alloy;

[0030] 2) LiNO 3 -NaNO 3 -KNO 3 The eutectic mixture is placed in a container and heated to melt it to obtain LiNO 3 -NaNO 3 -KNO 3 molten liquid, and heated up to 290 ° C, while passing nitrogen to drive out the air in the container, the Sn 0.99 Cu 0.01 The alloy is carefully added to the above molten liquid, and after the metal emulsion is formed under the action of ultrasonic waves, it is rapidly cooled to room temperature to obtain a solid;

[0031] 3) The obtained solid was washed with water to remove nitrate, and dried under vacuum at 40°C for 12 h to obtain micron-sized Sn 0.99 Cu 0.01 powder, its scanning electron image is as figure 1 shown;

[0...

Embodiment 2

[0033] Example 2TiO 2 Coated Bi 0.98 Cu 0.02 Preparation of Alloy Powder as Catalyst Carrier with Temperature Regulating Function

[0034] 1) Weigh 20 g of the pre-prepared LiCl–KCl–CsCl eutectic mixture (melting point about 270°C) and 5 g of Bi prepared by high-temperature melting 0.98 Cu 0.02 alloy;

[0035] 2) Put the LiCl–KCl–CsCl eutectic mixture in a container, heat it to melt to obtain a molten liquid, and raise the temperature to 350°C, and at the same time, blow in argon to drive out the air in the container. Put Bi 0.98 Cu 0.02 The alloy is carefully added to the above molten liquid, and after the metal emulsion is formed under the action of ultrasonic waves, it is rapidly cooled to room temperature to obtain a solid;

[0036] 3) The obtained solid was washed with water to remove chloride, and dried under vacuum at 40°C for 12 h to obtain micron-sized Bi 0.98 Cu 0.02 Powder;

[0037] 4) Weigh 4.5 g of the above Bi 0.98 Cu 0.02 Powder, put it in a containe...

Embodiment 3

[0038] Example 3Al 2 o 3 Coated Zn 0.92 Cu 0.08 Preparation of Alloy Powder as Catalyst Carrier with Temperature Regulating Function

[0039] 1) Weigh 15 g of the pre-prepared LiCl–KCl–CsCl eutectic mixture (melting point is about 270°C) and 5 g of Zn prepared by high-temperature melting 0.92 Cu 0.08 alloy;

[0040] 2) Put the LiCl–KCl–CsCl eutectic mixture in a container, heat it to melt to obtain a molten liquid, and raise the temperature to 480°C, and at the same time pass argon to drive out the air in the container, and Zn 0.92 Cu 0.08 The alloy is carefully added to the above molten liquid, and after the metal emulsion is formed under the action of ultrasonic waves, it is rapidly cooled to room temperature to obtain a solid;

[0041] 3) The obtained solid was washed with water to remove chloride, and dried under vacuum at 40°C for 12 h to obtain micron-sized Zn 0.92 Cu 0.08 Powder;

[0042] 4) Weigh 4.5 g of the above Zn 0.92 Cu 0.08 For powder, put it in a co...

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Abstract

The invention discloses a catalyst carrier with a temperature adjustment function and a preparation method of the catalyst carrier. The catalyst carrier with the temperature adjustment function has amicrocapsule structure, and a core is a micron-sized Sn, Bi, or Zn-based metal eutectic alloy, and is used for energy storage and energy release through a melting and solidification phase transition process, thereby realizing adjustment of the internal temperature of a catalyst; and a shell is an oxide that can be widely used as a catalyst carrier, namely SiO2, Al2O3 and TiO2, and is used to act as the true carrier of the catalyst. The preparation method of the catalyst carrier includes the following steps: preparing the micron-sized Sn, Bi or Zn-based eutectic alloy powder by using a metal emulsion process, and coating the metal eutectic alloy powder with the SiO2, the Al2O3 or the TiO2 by using a heterogeneous nucleation growth process. According to the method, the components of the metal eutectic alloy are changed, so that the prepared carrier can load the metal active component; and the carrier is applied to an exothermic catalytic reaction at the reaction temperature of 200-420 DEG C.

Description

technical field [0001] The invention belongs to the technical field of catalyst carrier preparation, in particular to a catalyst carrier with a temperature regulating function and a preparation method thereof. Background technique [0002] For a strongly exothermic catalytic reaction on a solid catalyst, even under optimized operating conditions, it is difficult for the heat generated by the reaction to be transferred from the inside of the catalyst particle to the outer surface of the particle in time, and then taken away by the fluid, and these cannot be timely The heat taken away not only causes a temperature gradient between the inside and outside of the catalyst, but also between the catalyst and the fluid. The end result is that the temperature inside the catalyst is often much higher than the temperature of the fluid. Since the active components of supported metal catalysts are often in a highly dispersed state (such as nanoscale), these thermodynamically unstable nan...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/06B01J23/14B01J23/18B01J23/80B01J23/835B01J23/843B01J32/00
CPCB01J23/835B01J23/8437B01J23/80B01J23/14B01J23/18B01J23/06B01J35/396
Inventor 刘宗健刘凌浩罗伟张歌珊唐浩东
Owner ZHEJIANG UNIV OF TECH