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Pd/CeBaSi catalyst and preparation method thereof

A technology of catalyst and preparation steps, which is applied in the field of Pd/CeBaSi catalyst and its preparation, and can solve the problems of incomplete low-temperature deep oxidation of methanol, poor purification effect of intermediate products, and great influence of air-fuel ratio.

Active Publication Date: 2019-04-05
CHENGDU UNIV OF INFORMATION TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The existing three-way catalyst can only purify the conventional pollutants in the exhaust gas, but has poor purification effect on methanol and methanol intermediate products, and cannot fully realize the low-temperature deep oxidation of methanol. Easy to deactivate and other issues

Method used

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  • Pd/CeBaSi catalyst and preparation method thereof
  • Pd/CeBaSi catalyst and preparation method thereof
  • Pd/CeBaSi catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] The present embodiment adopts co-precipitation method to prepare modified Pd / BaCe catalyst, as follows:

[0032] The preparation of carrier, according to mass ratio 13:87:100 respectively weigh Ba(NO 3 ) 2 , Ce(NO 3 ) 3 ·6H 2 O, Na 2 SiO 3 9H 2 O was added to water and stirred until completely dissolved to obtain a brine, followed by NH 3 ·H 2 O as the lye, take the salt solution and the lye at the same time with a flow rate ratio of 1: (1.5 ~ 2) and drop them into the reaction container to stir and react, age for 24h, and suction filter the obtained reaction solution. After drying, the obtained powder Calcined at 550-650°C for 3 hours to obtain a carrier composite oxide.

[0033] Catalyst preparation, adding support composite oxide to PdCl 2 In the aqueous solution, stir and disperse for 0.5h, then dry and bake at 550-650°C for 3h to obtain the catalyst Pd / CeBaSi-1.

Embodiment 2

[0035] The present embodiment adopts hydrothermal synthesis method to prepare modified Pd / BaCe catalyst, as follows:

[0036] The preparation of carrier, according to mass ratio 13:87:100 respectively weigh Ba(NO 3 ) 2 , Ce(NO 3 ) 3 ·6H 2 O, Na 2 SiO 3 9H 2 O was added to water and stirred until completely dissolved to obtain a brine, followed by NH 3 ·H 2O as lye, take salt solution and lye at the flow rate ratio of 1: (1.5 ~ 2) and drop them into the reaction vessel at the same time to stir the reaction, then transfer to the high-pressure reactor, and crystallize at 140°C for 72h to obtain the reaction liquid, and the reaction liquid was suction-filtered and dried, and the obtained powder was calcined at 550-650°C for 3 hours to obtain a carrier composite oxide.

[0037] Catalyst preparation, adding support composite oxide to PdCl 2 In the solution, stir and disperse for 0.5h, then dry and bake at 550-650°C for 3h to obtain the catalyst Pd / CeBaSi-2.

Embodiment 3

[0039] The present embodiment adopts salt drop alkali method to prepare modified Pd / BaCe catalyst, as follows:

[0040] The preparation of carrier, according to mass ratio 13:87:100 respectively weigh Ba(NO 3 ) 2 , Ce(NO 3 ) 3 ·6H 2 O, Na 2 SiO 3 9H 2 O was added to water and stirred until completely dissolved to obtain a brine, followed by NH 3 ·H 2 O as lye, add the salt solution dropwise into the lye and stir for reaction, then age for 24 hours, filter the obtained reaction solution, dry, and roast the obtained powder at 550-650°C for 3 hours to obtain a carrier composite oxide .

[0041] Catalyst preparation, adding support composite oxide to PdCl 2 In the solution, stir and disperse for 0.5h, then dry and bake at 550-650°C for 3h to obtain the catalyst Pd / CeBaSi-3.

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Abstract

The invention relates to the technical field of catalysts, in particular to a Pd / CeBaSi catalyst and a preparation method thereof. The Pd / CeBaSi catalyst is prepared from SiO2-modified Pd / CeBa and hasPd content of 0.5%. The Pd / CeBaSi catalyst is prepared through co-precipitating process, hydrothermal process, salt alkali-dripping process or alkali salt-dripping process, wherein the catalyst prepared via the co-precipitating process has the maximum specific surface area, pore capacity and pore size, adsorption of reaction molecules to the surface of the catalyst is benefited, the high pore capacity is good for dispersion of reaction molecules, and catalytic reaction is facilitated accordingly; the prepared Pd / CeBaSi catalyst has surface mid-strong basic sites and strong basic sites, whichare good for the catalytic conversion and deep oxidation of methanol; the catalyst herein is applicable to front purification of methanol fuel exhaust; methanol not combusted completely and intermediate products generated by incomplete combustion of methanol are converted into CO2 and H2O, so that the service life of an automotive rear-end three-way catalyst can be extended, and clean emission ofthe exhaust is facilitated.

Description

technical field [0001] The invention relates to the technical field of catalysts, in particular to a Pd / CeBaSi catalyst and a preparation method thereof. Background technique [0002] As a modern means of transportation, automobiles have brought a lot of convenience to people. However, a large amount of exhaust gas from automobiles has caused serious pollution to the atmospheric environment, especially causing great harm to people's health. Methanol is an oxygenated fuel and has many advantages in combustion performance, so it can be used as an alternative fuel for automobiles. However, due to the low temperature in the cylinder and insufficient oxygen concentration in methanol gasoline vehicles during cold start or idling, it is easy to cause incomplete combustion of methanol and produce oxygen-containing intermediate products such as aldehydes and esters. Into the vehicle exhaust and discharged, the discharge of these substances will accelerate air pollution. Therefore, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/63F01N3/28
CPCF01N3/2803B01J23/002B01J23/63B01J2523/00B01J2523/25B01J2523/3712B01J2523/41B01J2523/824
Inventor 张雪乔詹江波陈星仡
Owner CHENGDU UNIV OF INFORMATION TECH