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A kind of supported trimetallic catalyst and its preparation method and catalytic glycerol hydrogenolysis reaction method

A catalyst and supported technology, applied in the direction of metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., to achieve high catalytic activity and selectivity for glycerol hydrogenolysis

Active Publication Date: 2020-08-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although there are many reports in the literature, there is still a lot of room for improvement and improvement in the activity and selectivity of the catalyst for hydrogenolysis of glycerol.

Method used

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  • A kind of supported trimetallic catalyst and its preparation method and catalytic glycerol hydrogenolysis reaction method
  • A kind of supported trimetallic catalyst and its preparation method and catalytic glycerol hydrogenolysis reaction method
  • A kind of supported trimetallic catalyst and its preparation method and catalytic glycerol hydrogenolysis reaction method

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preparation example Construction

[0029] According to another aspect of the present invention, the present invention also provides a preparation method of supported trimetallic catalyst, the method comprising the steps of:

[0030] (1) impregnating the support with a solution containing the first metal component compound, or a mixed solution containing the first metal component compound and a platinum-containing compound, and then performing the first reduction activation;

[0031](2) impregnating the reductively activated product obtained in step (1) with a solution containing a platinum compound in a reducing or inert atmosphere, and then performing a second reductive activation to obtain a catalyst precursor;

[0032] (3) impregnating the catalyst precursor obtained in step (2) with a solution containing the second metal component compound in a reducing or inert atmosphere, and then drying and optionally calcining to obtain the supported trimetallic catalyst.

[0033] The platinum-containing compound is at ...

Embodiment 1

[0057] This example is used to illustrate the catalyst provided by the present invention and its preparation method.

[0058] 1) According to the required metal salt content of equal volume impregnation method, be prepared with the impregnation solution of 30.6 milliliters of nickel nitrate containing 219 grams per liter of nickel. Decant the impregnation solution to 36 g γ-Al 2 o 3 The carrier (product of Changling Catalyst Factory, particle size 20-40 mesh, the same below) was stirred evenly at 20°C, left to stand for 4 hours, and then dried at 120°C.

[0059] 2) Roasting at 400°C for 4 hours, hydrogen reduction at 400°C for 4 hours, and hydrogen pressure at 0.1 MPa.

[0060] 3) After reduction, it was lowered to room temperature, and 55.1 ml of platinum dichlorotetraammine platinum aqueous solution containing 8.12 g / L of platinum was added under a hydrogen atmosphere, allowed to stand for 2 hours, and then dried with hydrogen. After drying, the temperature was raised to ...

Embodiment 2

[0076] This example is used to illustrate the catalyst provided by the present invention and its preparation method.

[0077] 1) According to the required metal salt content of equal volume impregnation method, be prepared with the impregnation solution of 30.6 milliliters of nickel nitrate containing 219 grams per liter of nickel. Decant the impregnation solution to 36 g SiO 2 Carrier (Qingdao Ocean Chemical Factory), stirred at 15°C, allowed to stand for 6 hours, and then dried at 100°C.

[0078] 2) Roasting at 450°C for 2 hours, hydrogen reduction at 450°C for 2 hours, and hydrogen pressure at 1 MPa.

[0079] 3) After reduction, it was lowered to room temperature, and 55.1 ml of platinum dichlorotetraammine platinum aqueous solution containing 8.12 g / L of platinum was added under a hydrogen atmosphere, allowed to stand for 2 hours, and then dried with hydrogen. After drying, the temperature was raised to 450° C. and reduced for 4 hours under a hydrogen atmosphere, and the...

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Abstract

The invention discloses a supported trimetallic catalyst and a preparation method and application thereof, and a method for catalyzing the hydrogenolysis of glycerol. The catalyst comprises a carrierand metal active components loaded on the carrier, wherein the metal components with hydrogenation activity are composed of platinum, a first metal component M<1> selected from the group-VIII non-noble metals and a second metal component M<2> selected from the group-VIB and / or group-VIIB metals. The catalyst satisfies the equation that (M<2> / M<1>)<XPS> / (M<2> / M<1>)<XRF> = 2.0 to 20.0, wherein (M<2> / M<1>)<XPS> is a weight ratio, in terms of element, of the second metal component to the first metal component in the catalyst characterized by X-ray photoelectron spectroscopy, and (M<2> / M<1>)<XRF> is a weight ratio, in terms of element, of the second metal component to the first metal component in the catalyst characterized by X-ray fluorescence spectroscopy. Compared with catalysts with same metal contents in the prior art, the supported trimetallic catalyst of the invention has significantly higher activity in catalyzing the hydrogenolysis of glycerin and higher 1,3-propanediol selectivity.

Description

technical field [0001] The invention relates to a supported three-metal component catalyst, a preparation method thereof and a glycerol hydrogenolysis reaction method. Background technique [0002] 1,3-propanediol is an important raw material for the production of degradable polyester propylene terephthalate (PTT), etc., and its demand is constantly increasing; moreover, as an important chemical raw material, it can also be used in solvents, emulsifiers, medicines, In cosmetics and organic synthesis. At present, the industrial production of 1,3-propanediol mainly adopts ethylene oxide carbonylation method and acrolein hydration hydrogenation method, and the raw materials of these two processes are from petroleum. With the continuous depletion of petroleum resources, it is of great significance to find non-petroleum routes for the production of 1,3-propanediol. Glycerol is a stoichiometric by-product (about 10%) in the biodiesel production process. With the large demand and...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89B01J23/652C07C29/60C07C31/20
CPCB01J23/6527B01J23/8993C07C29/60C07C31/205
Inventor 郑仁垟李明丰李会峰夏国富吴玉徐润
Owner CHINA PETROLEUM & CHEM CORP