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Method for preparing small-size Pd<KBr>@HSC by in-situ bromine addition

A small-sized, in-situ addition technology, applied in chemical instruments and methods, catalyst activation/preparation, chemical/physical processes, etc., can solve the problems of low catalyst recycling rate, low selectivity, active component shedding, etc., to achieve Effects of improving reuse efficiency, improving catalyst activity, and improving selectivity

Inactive Publication Date: 2019-07-09
GUIZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the research on catalysts for the direct synthesis of hydrogen peroxide from hydrogen and oxygen mainly focuses on supported Pd-based catalysts, which have the problems of low selectivity and low recycling rate, mainly because the active component Pd is not evenly dispersed on the carrier. , the agglomeration of some active components Pd cannot be fully utilized; at the same time, a part of Pd is too small in size, resulting in more unsaturated sites, which make the reaction proceed in the direction of side reactions and reduce the selectivity of the catalyst
In addition, during the use of the catalyst, the active components will fall off from the carrier, resulting in a low recycling rate of the catalyst

Method used

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  • Method for preparing small-size Pd&lt;KBr&gt;@HSC by in-situ bromine addition
  • Method for preparing small-size Pd&lt;KBr&gt;@HSC by in-situ bromine addition
  • Method for preparing small-size Pd&lt;KBr&gt;@HSC by in-situ bromine addition

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] (1) Preparation of Pd KBr @SiO 2 : Take cyclohexane (40mL), n-octanol (10mL) as the oil phase, polyethylene glycol monohexadecyl ether (Brij56) (6.521g) as the surfactant, mix and dissolve at 35°C; 0.03gKBr as the functional The molecule was added to 1 mL of chloropalladium acid solution with a concentration of 0.075M, dissolved and added dropwise to the above oil phase solution as the water phase to form reverse micelles. Because the water phase is incompatible with the oil phase, a rigid film with strong rigidity will be formed at the interface of the two phases, so the water phase will form an independent nanoscale microreactor ( figure 1 -I). After the above solution was stirred for 2 h, 300 μL of NaBH was added 4 (10wt%) solution, palladium ion (Pd 2+ ) by NaBH 4 rapidly reduced to palladium nanoparticles ( figure 1 -II). After reacting for 10min, add 3ml NH dropwise 3 ·H 2 O, provide an alkaline environment for the hydrolysis of TEOS, and then add TEOS dr...

Embodiment 2

[0045] (1) Take a mixture of 35ml of n-heptane and 5ml of propanol as the oil phase, and 6g of nonylphenol polyoxyethylene ether as the surfactant, mix them and dissolve them at 30°C to obtain product A;

[0046] (2) Add 0.02gNH 3 Add Br as a functional molecule to 1ml of chloropalladium acid solution with a concentration of 0.07M, dissolve it and add it to product A as the water phase to form reverse micelles to obtain product B;

[0047] (3) After stirring product B for 1 h, add 250 μL of 10 wt% NaBH 4 solution, continue to add 2ml NH after reacting for 5min 3 ·H 2 O, to be NH 3 ·H 2 After O was fully dispersed around the palladium nanoparticles, TEOS was added dropwise to react for 5 hours, then 40ml of ethanol was added, and finally washed by centrifugation with ethanol to obtain Pd KBr @SiO 2 catalyst;

[0048] (4) Pd obtained with step (3) KBr @SiO 2 The catalyst is used as a template agent, dispersed into a mixture of 60ml of deionized water and 30ml of ethanol...

Embodiment 3

[0052] (1) Take the mixture of 45ml of isooctane and 15ml of n-heptanol as the oil phase, and 7g of sodium lauryl sulfate as the surfactant, mix it and dissolve it at 40°C to obtain product A;

[0053] (2) Adding 0.04g NaBr as a functional molecule into 1ml of chloropalladium acid solution with a concentration of 0.08M, after dissolving, add it to product A as the water phase to form reverse micelles to obtain product B;

[0054] (3) After stirring product B for 3 hours, add 350 μL of NaBH with a concentration of 10 wt%. 4 solution, continue to add 4ml NH after reacting for 15min 3 ·H 2 O, to be NH 3 ·H 2 After O was fully dispersed around the palladium nanoparticles, TEOS was added dropwise to react for 7 hours, then 60ml of ethanol was added, and finally washed by ethanol centrifugation to obtain PdKBr@SiO 2 catalyst;

[0055] (4) Pd obtained with step (3) KBr @SiO 2 The catalyst is used as a template agent, dispersed into a mixture of 80ml deionized water and 40ml et...

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Abstract

The invention discloses a method for preparing small-size Pd<KBr>@HSC by in-situ bromine addition, which comprises the following steps: (1) with a mixture of alkane and an alcohol reagent as an oil phase and polyethylene glycol monohexadecyl ether and the like as surfactants, and mixing and dissolving the surfactants to obtain a product A; (2) adding KBr into a chloropalladic acid solution to obtain a product B; (3) adding a NaBH4 solution, adding NH3.H2O, adding TEOS (tetraethyl orthosilicate), adding ethanol, and finally centrifuging and washing with ethanol to obtain a Pd<KBr>@SiO2 catalyst; (4) dispersing Pd<KBr>@SiO2 into a mixed solution of deionized water and ethanol, and adding CTAB (cetyltrimethyl ammonium bromide) to obtain a product C; (5) adding resorcinol and formaldehyde intothe product C to obtain Pd<KBr>@SiO2@RF / CTAB; and (6) carbonizing, etching and reducing the Pd<KBr>@SiO2@RF / CTAB to obtain the final product Pd<KBr>@HSC. The Pd<KBr>@HSC catalyst disclosed by the invention has the characteristics of small active component size, uniformity and difficulty in falling off.

Description

technical field [0001] The present invention relates to a kind of preparation method of hydrogen peroxide catalyst, especially a kind of preparation method of small size Pd by adding bromine in situ KBr @HSC's approach. Background technique [0002] Hydrogen-oxygen direct synthesis of hydrogen peroxide method has the advantages of simple process, low operating cost, clean product and strong atom economy in the production method of hydrogen peroxide, but H 2 o 2 The selectivity and productive rate are very low, far below the requirements of industrial production. The catalytic activity of the catalyst and its response to H 2 o 2 The selectivity is the key factor that affects the direct synthesis of hydrogen peroxide from hydrogen and oxygen. At present, the research on catalysts for the direct synthesis of hydrogen peroxide from hydrogen and oxygen mainly focuses on supported Pd-based catalysts, which have the problems of low selectivity and low recycling rate, mainly be...

Claims

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Application Information

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IPC IPC(8): B01J27/13B01J35/00B01J37/00B01J37/08C01B15/029
CPCB01J37/0018B01J37/084B01J27/13C01B15/029B01J35/398B01J35/393
Inventor 潘红艳林倩曹建新赵静昀陈政
Owner GUIZHOU UNIV