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A kind of titanium/palladium composite catalyst, preparation method and its application in acetone hydrogenation reaction

A composite catalyst, titanium dioxide technology, applied in the direction of physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, carbon-based compound preparation, etc., can solve the problem that the activity and selectivity cannot meet the requirements of industrialization

Active Publication Date: 2019-02-01
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because the activity and selectivity of this kind of catalyst are not up to the requirements of industrialization, there are no reports of practical application.

Method used

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  • A kind of titanium/palladium composite catalyst, preparation method and its application in acetone hydrogenation reaction
  • A kind of titanium/palladium composite catalyst, preparation method and its application in acetone hydrogenation reaction

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0056] Step (1): Fluorine modification of mesoporous silica

[0057] Immerse 5.0 g of 40-60 mesh commercial mesoporous silica in 224 mL of 0.5 mol / L hydrofluoric acid aqueous solution, sonicate for 0.5 h, and dry overnight at 110°C to obtain fluorine-modified mesoporous silica. Elemental analysis indicated 1.6 wt% fluorine doping; labeled as SiO 2 (B-F1.6).

[0058] Step (2):

[0059] Step (2-a): supporting titanium dioxide on fluorine-modified mesoporous silica (preparation of supported titanium dioxide component)

[0060] At room temperature, mix 10mL of tetra-n-butyl titanate and 35mL of absolute ethanol in a closed flat-bottomed three-neck flask, stir vigorously for 30min, then take 20mL of glacial acetic acid, 1mL of absolute ethanol, and 0.2mL of distilled water to mix evenly, and add to the above mixture solution, stirred vigorously for 1 h. At this point, a clear transparent golden yellow solution was obtained, and 5 g of fluorine-modified mesoporous silica (SiO 2...

Embodiment 2

[0082] Step (1): Fluorine modification of mesoporous silica

[0083] Immerse 5.0 g of 40-60 mesh commercial mesoporous silica in 224 mL of 0.25 mol / L hydrofluoric acid aqueous solution, sonicate for 0.5 h, and dry at 110°C overnight. Fluorine-modified silica was obtained, elemental analysis showed that the fluorine doping amount was 0.65wt%, marked as SiO 2 (B-F-0.65).

[0084] Step (2):

[0085] Step (2-a): supporting titanium dioxide on fluorine-modified mesoporous silica (preparation of supported titanium dioxide component)

[0086] At room temperature, mix 10mL of tetra-n-butyl titanate and 35mL of absolute ethanol in a closed flat-bottomed three-neck flask, stir vigorously for 30min, then take 20mL of glacial acetic acid, 1mL of absolute ethanol, and 0.2mL of distilled water, mix well, and add to the above mixture solution, stirred vigorously for 1 h. At this point, a clear transparent golden yellow solution was obtained, and 5 g of fluorine-modified mesoporous silica...

Embodiment 3

[0093] Compared with Example 2, the difference is that in step (1), the concentration of the hydrofluoric acid aqueous solution used is 1.5mol / L, and the fluorine doping amount of the fluorine-modified silica after the step (1) is completed 2.2wt%, marked as SiO 2 (B-F-2.2).

[0094] The TiO obtained by fluorine-modified silica through step (2-a) 2 product, labeled TiO 2 / SiO 2 (B-F2.2); TiO 2 The loading was 2.24 wt%. After the step (3), the mixed catalyst of supported titanium dioxide and supported palladium is marked as TiO 2 / SiO 2 (B-F2.2) & Pd / Cor, TiO 2 The mass ratio to Pd is 36. TiO 2 / SiO 2 (B-F2.2) & Pd / Cor acetone catalytic activity results are shown in Table 2.

[0095] Embodiment 1, embodiment 2, embodiment 3 and comparative example 4 probed into the fluorine doping amount, palladium particle size on the influence of catalyst in acetone hydrogenation synthesis MIBK catalytic performance, the catalytic acetone hydrogenation of each embodiment and compar...

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Abstract

The invention discloses a titanium / palladium composite catalyst, which contains a supported titanium dioxide component and a supported palladium component, which are physically mixed. The carrier of the supported titanium dioxide component is fluorine-modified silica. In addition, the present invention also discloses a preparation method of the titanium / palladium composite catalyst and the application of the catalyst in acetone hydrogenation reaction to prepare MIBK. The catalyst of the invention is used in the normal-pressure gas phase reaction of hydrogenating acetone to synthesize methyl isobutyl ketone. The acetone conversion rate can reach 77.2%, the MIBK selectivity can reach 78.9%, and the corresponding MIBK yield can reach 60.9%. Compared with similar catalysts, this catalyst has the characteristics of high activity, high selectivity and simple preparation method.

Description

technical field [0001] The invention relates to a titanium / palladium composite catalyst, a preparation method and its application in acetone hydrogenation reaction. Background technique [0002] Acetone is a by-product of the phenol production industry as well as the propylene oxide production industry and is currently in surplus worldwide. At the same time, acetone is also an important platform compound for the production of chemical raw materials from biomass. How to convert acetone into chemical products with high added value has important economic value. [0003] At present, acetone and hydrogen are mainly mixed at home and abroad, and polycondensation (acid or base catalysis), dehydration (acid catalysis) and hydrogenation (metal catalysis) are completed under the action of a multifunctional catalyst to prepare methyl isobutyl ketone (MIBK for short). , which is the so-called one-pot process in the literature. MIBK is an excellent medium-boiling organic solvent with ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/135C07C45/73C07C49/04
CPCC07C45/73B01J23/44B01J27/135B01J35/19C07C49/04
Inventor 周永华杨乐群钟宏叶红齐王晖
Owner CENT SOUTH UNIV