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Activated carbon carrier treatment method, and preparation method and application of palladium-carbon catalyst

The technology of a palladium-carbon catalyst and a treatment method, applied in the field of catalysis, can solve problems such as uninvolved influence, and achieve the effects of good anti-poisoning ability, easy popularization and application, and high reaction performance

Inactive Publication Date: 2020-01-21
XIAN CATALYST NEW MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, none of the above technical solutions involves the influence of the intrinsic pH on the surface of activated carbon on the performance of the catalyst.

Method used

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  • Activated carbon carrier treatment method, and preparation method and application of palladium-carbon catalyst
  • Activated carbon carrier treatment method, and preparation method and application of palladium-carbon catalyst
  • Activated carbon carrier treatment method, and preparation method and application of palladium-carbon catalyst

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Embodiment 1-1

[0032] The processing method of the activated carbon carrier of the present embodiment may further comprise the steps:

[0033] Step 1. Under normal temperature conditions, the particle size of 100g is 200 mesh, and the specific surface area is 1500m 2 The gac / g is placed in 1000g pretreatment solution and soaked for 24h, filters, washes the retentate with deionized water, filters, and obtains pretreatment gac; described pretreatment solution is the nitric acid solution that mass concentration is 10%;

[0034] Step 2, adding the pretreated activated carbon described in step 1 into 1500g of buffer solution, stirring at room temperature for 12h, filtering, and washing the filtered activated carbon to obtain an activated carbon carrier; the buffer solution is acetic acid with a pH of 4±0.1 - sodium acetate buffer solution;

[0035] It was determined that the pH value of the activated carbon carrier was 4.

Embodiment 1-2

[0042] The processing method of the activated carbon carrier of the present embodiment may further comprise the steps:

[0043] Step 1. Under normal temperature conditions, 100g of particles with a particle size of 400 mesh and a specific surface area of ​​950m 2 The gac / g is placed in 2000g pretreatment solution and soaked for 24h, filters, washes the retentate with deionized water, and filters to obtain pretreatment gac; the pretreatment solution is hydrogen peroxide with a mass concentration of 10%, which can also be 10% nitric acid solution;

[0044] Step 2. Add the pretreated activated carbon described in step 1 into 1000g of buffer solution, stir for 12 hours at room temperature, filter, and do not wash the filtered activated carbon to obtain an activated carbon carrier; the buffer solution is carbonic acid with a pH of 10±0.2 Sodium-sodium bicarbonate buffer solution.

[0045] It was determined that the pH value of the activated carbon carrier was 10.

Embodiment 1-3

[0047] The processing method of the activated carbon carrier of the present embodiment may further comprise the steps:

[0048] Step 1. Under normal temperature conditions, 100g of particles with a particle size of 300 mesh and a specific surface area of ​​1200m 2 The gac / g is placed in 1500g pretreatment solution and soaked for 24h, filters, washes the retentate with deionized water, filters, and obtains pretreatment gac; described pretreatment solution is the sodium hydroxide solution that mass concentration is 10%, also can Be the potassium hydroxide solution that mass concentration is 10%;

[0049] Step 2. Add the pretreated activated carbon described in step 1 into 2000g of buffer solution, stir for 12 hours at room temperature, filter, and filter the activated carbon without washing to obtain the activated carbon carrier; the buffer solution is acetic acid with a pH of 4 ± 0.1 - Sodium acetate buffer solution.

[0050] It was determined that the pH value of the activat...

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Abstract

The invention discloses a treatment method of an activated carbon carrier, which comprises the following steps: 1, soaking activated carbon in a pretreatment solution at normal temperature for 20-30 hours, washing the activated carbon, and filtering the liquid to obtain pretreated activated carbon, wherein the pretreatment solution is a nitric acid solution, a potassium hydroxide solution, a sodium hydroxide solution or hydrogen peroxide; 2, adding the pretreated activated carbon obtained in the step 1 into a buffer solution, stirring the solution for 1-48 h at normal temperature, and filtering the solution to obtain an activated carbon carrier. In addition, the invention also provides a method for preparing a palladium-carbon catalyst by adopting the activated carbon carrier obtained by the method and application. In the invention, the activated carbon is treated through a pretreatment solution, the pretreated activated carbon is subjected to secondary treatment through a buffer solution, a carrier with the surface intrinsic pH value strictly controlled is directly obtained to be used for preparing the palladium-carbon catalyst without water washing, and the catalyst has high reaction activity in the catalytic synthesis reaction of N,N-dimethylcyclohexylamine.

Description

technical field [0001] The invention belongs to the technical field of catalysis, and in particular relates to an activated carbon carrier treatment method, a preparation method and an application of a palladium carbon catalyst. Background technique [0002] Pd / C catalysts are widely used to catalyze liquid-phase hydrogenation, oxidation, coupling and other reactions, and play an irreplaceable role in realizing the green production of fine chemical products such as medicines, dyes, and pesticides, and realize the controllable preparation of Pd / C catalysts is the key technology. The controllable preparation of Pd / C is often realized by the adjustment of the surface properties of activated carbon, and then the precise control of the particle morphology of the noble metal active center is achieved. [0003] According to C.F.Baes [C.F.Baes and R.S.Mesmer, Ber.Bunsen-Ges., 1977, 811245-246.] and S.Y.Troitskii [S.Y.Troitskii, A.L.Chuvilin and V.A.Likholobov, Russ. 1826], due to ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J32/00B01J21/18B01J23/44B01J35/10C01B32/354C07C209/26C07C211/35
CPCB01J21/18B01J23/44C01B32/354C07C209/26C07C2601/14B01J35/60B01J35/617B01J35/618C07C211/35
Inventor 张磊翟康王昭文李岳锋万克柔曾永康张之翔
Owner XIAN CATALYST NEW MATERIALS CO LTD