Metal carrier load gold catalyst and application thereof in preparing aldehyde or ketone by selectively oxidizing catalytic alcohol

A gold catalyst and metal carrier technology, applied in the field of catalysis, can solve the problems of high cost, many by-products, harsh reaction temperature, etc., and achieve the effects of low production cost, high activity at low temperature and high selectivity

Inactive Publication Date: 2010-02-17
EAST CHINA NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The electrolytic silver catalyst commonly used in industry has high cost, harsh reaction temperature, low catalytic activity when it is lower than 550°C, and more by-products will be produced when it is higher than 550°C, and silver crystallites are easy to quickly agglomerate under high temperature conditions, resulting in catalytic activity. And the decrease of selectivity and the increase of reaction bed resistance
However, for multi-carbon alcohols (such as benzyl alcohol, etc.), electrolytic silver catalysts are not suitable because high-temperature reactions will obviously lead to pyrolysis and excessive oxidation of reactants and products.
[0004] Oxidation-supported silver catalysts catalyze the oxidative dehydrogenation of alcohols to generate corresponding aldehydes and ketones. The supported silver catalysts reported in U.S. Patent (US 1,067,665) are simple to prepare and have high silver loadings, but the specific area of ​​the catalyst is small, Uneven distribution, less th

Method used

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  • Metal carrier load gold catalyst and application thereof in preparing aldehyde or ketone by selectively oxidizing catalytic alcohol
  • Metal carrier load gold catalyst and application thereof in preparing aldehyde or ketone by selectively oxidizing catalytic alcohol
  • Metal carrier load gold catalyst and application thereof in preparing aldehyde or ketone by selectively oxidizing catalytic alcohol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] According to the literature (Applied Catalysis A 2007, 328: 77-82), a papermaking / post-sintering technique was adopted to prepare a sintered metal fiber carrier.

[0021] The metal fibers are: Ni fiber with a diameter of 4 microns, Ni fiber with a diameter of 8 microns, copper fiber with a diameter of 8 microns, copper fiber with a diameter of 80 microns, copper fiber with a diameter of 120 microns, brass fiber with a diameter of 120 microns, and a diameter of 8 microns Stainless steel (316L) fibers, titanium fibers with a diameter of 16 microns; the length of the fibers is 2 to 5 mm.

[0022] The prepared sintered metal fiber supports are represented as S-X-Ni-4, S-X-Ni-8, S-X-Cu-Z-8, S-X-Cu-Z-80, S-X-Cu-Z-120, S-X-Cu- H-120, S-X-SS and S-X-Ti.

Embodiment 2

[0024] This example provides a preparation of a gold catalyst supported by a sintered metal fiber carrier.

[0025] Using S-X-Ni-8 as the carrier, impregnate S-X-Ni-8 with equal volumes of chloroauric acid aqueous solution containing 2 g / L, 4 g / L, 6 g / L, 8 g / L and 10 g / L of gold respectively Carrier, 400 ℃ of calcining in air after drying 2 hours, makes the gold catalyst of sintering Ni fiber support, and Au content is respectively 1% (weight), 2% (weight), 3% (weight), 4% (weight ) and 5% (weight), the catalyst product is recorded as Au-1 / S-X-Ni-8, Au-2 / S-X-Ni-8, Au-3 / S-X-Ni-8, Au-4 / S-X-Ni- 8, Au-5 / S-X-Ni-8.

[0026] Optical photo of Au-3 / S-X-Ni-8 for reference figure 1 , scanning electron microscope (SEM) photos and energy spectrum (EDX) photos refer to figure 2 with image 3 .

Embodiment 3

[0028] This example provides the preparation of a gold catalyst supported on a sintered metal fiber carrier.

[0029] Using X-Ni-8 as the carrier, the X-Ni-8 carrier is impregnated with an equal volume of chloroauric acid aqueous solution containing 6 g / L of gold, and then baked in the air at 250°C, 350°C, 400°C, and 450°C after drying. The gold catalysts supported by sintered Ni fibers were obtained, respectively denoted as Au-3-250 / X-Ni-8, Au-3-350 / X-Ni-8, Au-3-400 / X-Ni-8, Au -3-450 / X-Ni-8.

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Abstract

The invention discloses a metal carrier load gold catalyst and application thereof in preparing aldehyde or ketone by selectively oxidizing catalytic alcohol, wherein the catalyst is prepared by isopyknically impregnating a metal fiber or metal particle carriers with chloroauric acid or sodium chloraurate solution and baking for 2 hours at a temperature between 250 DEG C and 400 DEG C, and containing 0.5-6.0 percent of gold and 94.0-99.5 percent of carrier; in the process of preparing the aldehyde or the ketone by vapor phase selective oxydehydrogenation of the catalytic alcohol, the catalystadopts a fixed bed reaction device, takes oxygen or air as an oxidant and selectively oxidizes the alcohol to generate aldehyde or ketone under the conditions that the reaction temperature is 250-350DEG C, the weight hourly space velocity of the alcohol is 10-60<-1> hours and the mole ratio of O2 to hydroxyl group is 0.4-1.2. The catalyst has favorable heat conductivity, high low-temperature activity, good stability, low cost, high efficiency for the catalytic alcohol to prepare the aldehyde or the ketone by selective oxydehydrogenation, and environment friendliness.

Description

technical field [0001] The invention belongs to the technical field of catalysis, and in particular relates to a metal-supported gold catalyst and the application of the catalyst in the preparation of aldehydes or ketones by catalyzing alcohol gas-phase selective oxidation dehydrogenation. technical background [0002] Gold has always been considered as a chemically inert metal. Compared with other noble metals such as platinum and palladium, the catalytic potential of gold has not attracted enough attention. In the 1980s, Japanese scientist Haruta and British scientist Hutchings and others discovered that gold nanoparticles [Nature, 2005, 437, 1098] have extraordinary catalytic effects. At present, Au catalysts are used in low-temperature oxidation of CO, selective hydrogenation, NO x Revert to generate N 2 It exhibits excellent catalytic performance in reactions such as selective oxidative dehydrogenation of alcohols. It not only has mild reaction conditions, high activi...

Claims

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Application Information

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IPC IPC(8): B01J23/89B01J23/52B01J23/66B01J35/06B01J35/02C07C45/37
Inventor 路勇赵国锋邓苗苗薛青松刘晔何鸣元
Owner EAST CHINA NORMAL UNIV
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