Device and method for synthesizing catalyst by using novel redox coprecipitation method

A co-precipitation method and catalyst technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problem of destroying the kinetic balance of precipitation and uneven distribution of catalyst components , Reduce catalyst activity and other issues, achieve the effects of reducing catalyst agglomeration, uniform catalyst synthesis, and stable pH of the reaction solution

Inactive Publication Date: 2020-02-07
HUAZHONG UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, hydrothermal synthesis, co-precipitation, sol-gel method and impregnation method are four commonly used synthesis methods. Compared with other preparation methods, co-precipitation method has lower requirements on the production environment because of its simple process. Therefore, it has a wide range of applications in industry, but the addition of precipitating agents will cause the local pH value to be too high, which will destroy the kinetic balance of precipitation, resulting in agglomeration and uneven distribution of catalyst components, thereby reducing the distribution of active sites of the catalyst on the surface of the catalyst. Reduce catalyst activity

Method used

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  • Device and method for synthesizing catalyst by using novel redox coprecipitation method
  • Device and method for synthesizing catalyst by using novel redox coprecipitation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] Configure acidic (nitric acid) deionized aqueous solution A (pH=1.0), weigh 9.31g Mn(NO 3 ) 2 50wt%H 2 O is dissolved in solution A to obtain solution B, which is sucked into the reducing solution injection pump 3;

[0053] Configure acidic (nitric acid) deionized aqueous solution C (pH=1.0), weigh 2.78g KMnO 4 Solid and 2.69g (NH 4 ) 2 Ce(NO 3 ) 6 , adding it to solution C, stirring to dissolve it to obtain solution D, and sucking solution D into the oxidizing solution syringe pump 2;

[0054] Configure 0.4M KOH solution E (pH=13.6), and suck the solution E into the alkaline solution syringe pump 4;

[0055] Start the magnetic stirrer 8 with heating function, heat the deionized water in the reaction tank to 70°C, and start the magnetic stirrer;

[0056] Set the pH value (1.0) required for this catalyst synthesis on the host computer 7, the syringe pump starts to work, and injects the reaction chemical solution into the reaction tank;

[0057] After the end, c...

Embodiment 2

[0059] Configure acidic (nitric acid) deionized aqueous solution A (pH=1.0), weigh 9.31g Mn(NO 3 ) 2 50wt%H 2 O is dissolved in solution A to obtain solution B, which is sucked into the reducing solution injection pump 3;

[0060] Configure acidic (nitric acid) deionized aqueous solution C (pH=1.0), weigh 2.78g KMnO 4 Solid and 2.69g (NH 4 ) 2 Ce(NO 3 ) 6 , adding it to solution C, stirring to dissolve it to obtain solution D, and sucking solution D into the oxidizing solution syringe pump 2;

[0061] Configure 0.4M KOH solution E (pH=13.6), and suck the solution E into the alkaline solution syringe pump 4;

[0062] Start the magnetic stirrer 8 with heating function, heat the deionized water in the reaction tank to 70°C, and start the magnetic stirrer;

[0063] The pH value (3.0) required for this catalyst synthesis is set on the upper computer 7, the syringe pump starts to work, and the reaction chemical solution is injected into the reaction tank;

[0064] After th...

Embodiment 3

[0066] Configure acidic (nitric acid) deionized aqueous solution A (pH=1.0), weigh 9.31g Mn(NO 3 ) 2 50wt%H 2 O is dissolved in solution A to obtain solution B, which is sucked into the reducing solution injection pump 3;

[0067] Configure acidic (nitric acid) deionized aqueous solution C (pH=1.0), weigh 2.78g KMnO 4 Solid and 2.69g (NH 4 ) 2 Ce(NO 3 ) 6 , adding it to solution C, stirring to dissolve it to obtain solution D, and sucking solution D into the oxidizing solution syringe pump 2;

[0068] Configure 0.4M KOH solution E (pH=13.6), and suck the solution E into the alkaline solution syringe pump 4;

[0069] Start the magnetic stirrer 8 with heating function, heat the deionized water in the reaction tank to 70°C, and start the magnetic stirrer;

[0070] Set the pH value (5.0) required for this catalyst synthesis on the host computer 7, the syringe pump starts to work, and injects the reaction chemical solution into the reaction tank;

[0071] After the end, c...

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Abstract

The invention discloses a device for synthesizing a catalyst by using a novel redox coprecipitation method. The device is characterized by comprising a reaction tank (1), an oxidant solution injectionpump (2), a reducing agent solution injection pump (3), an alkaline solution injection pump (4), a pH probe (5), a temperature probe (6), an upper computer (7) and a magnetic stirrer (8) with a heating function, wherein the upper computer (7) is used for controlling the ion concentration and the redox reaction speed in the reaction tank (1) through control on the propelling speed of the oxidant solution injection pump (2) and the propelling speed of the reducing agent solution injection pump (3), is used for measuring the pH value of a solution accurately through the pH probe (5) in the reaction tank (1), and is used for controlling the propelling speed of the alkaline solution injection pump (4) so that the pH value of the prepared solution is stabilized within a preset range of the setpH value. Through the device, the pH value in the reaction tank can be controlled with high precision, so that the synthesis reaction speed is controlled, the degree of automation is high, and manualerrors are reduced.

Description

technical field [0001] The invention belongs to the technical field of catalyst synthesis equipment, and in particular relates to a device and method for synthesizing catalysts by a novel oxidation-reduction co-precipitation method. Background technique [0002] With the rapid development of social economy, catalysts have been widely used in industrial production. Synthesizing catalysts with special morphology and functions has become a widespread consensus. At present, hydrothermal synthesis, co-precipitation, sol-gel method and impregnation method are four commonly used synthesis methods. Compared with other preparation methods, co-precipitation method has lower requirements on the production environment because of its simple process. Therefore, it has a wide range of applications in industry, but the addition of precipitating agents will cause the local pH value to be too high, which will destroy the kinetic balance of precipitation, resulting in agglomeration and uneven...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J4/00B01J19/18B01J23/34
CPCB01J4/001B01J4/008B01J19/0006B01J19/18B01J23/002B01J23/34B01J2204/002B01J2219/00063B01J2219/00177
Inventor 仲柳方庆艳李权张成陈刚
Owner HUAZHONG UNIV OF SCI & TECH
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