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Load type carbonized nickel indium alloy catalyst and its preparation method and application

A nickel-based catalyst and a catalyst technology, applied in the field of catalysis, can solve the problems of low methanol selectivity and yield, hot spots generated in the catalyst bed, low carbon dioxide conversion rate, etc., and achieve strong practical value, high conversion rate and selectivity. , Structure controllable effect

Active Publication Date: 2018-02-02
EAST CHINA NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among the copper-based catalysts, Cu-Zn-Al is the most typical copper-based catalyst with high catalytic activity but poor selectivity to methanol; LaCr 1-x Cu x o 3 Catalyst (CN101690894A), at 250°C, 2.0MPa, 9000L h -1 kg -1 、H 2 / CO 2 = CO under 2 reaction conditions 2 The conversion rate is 3-12%, and the methanol yield is only 0.06-0.38g g cat -1 h -1 ; current relatively good CO 2 Hydrogenation methanol synthesis catalyst CuZnAlGa (CN103263926A), at 200°C, 3500L h -1 kg -1 、H 2 / CO 2 =2 Under reaction conditions, although a higher CO 2 The conversion rate is 30%, but the reaction pressure is as high as 11.0MPa, and the selectivity of methanol is only 69.3%. Obviously, the main problems of Cu-based catalysts are the low conversion rate of carbon dioxide, and the selectivity and yield of methanol are not high.
Although the above copper-based catalysts have good hydrogenation performance, the two main problems facing the industrialization of these catalysts are the easy sintering of the catalyst, unsatisfactory stability and poor thermal conductivity, which lead to hot spots or even overheating in the catalyst bed.

Method used

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  • Load type carbonized nickel indium alloy catalyst and its preparation method and application
  • Load type carbonized nickel indium alloy catalyst and its preparation method and application
  • Load type carbonized nickel indium alloy catalyst and its preparation method and application

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Experimental program
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Effect test

Embodiment 1

[0046] 1. Take by weighing 3.91 grams of indium nitrate trihydrate (indium salt) and 4.95 grams of nickel nitrate hexahydrate (nickel salt), and ultrasonically dissolve them in 25 milliliters of distilled water to obtain a mixed aqueous solution containing nickel ions and indium ions; The silicon oxide carrier (carrier ZT) is impregnated with the prepared mixed aqueous solution containing nickel ions and indium ions, left at room temperature for 2 hours, then cleaned and dried, and then placed in an air atmosphere at 300 ° C for 2 hours to obtain Catalyst precursor, denoted as: In 2 o 3 -NiO / SiO 2 ;

[0047] ②The In prepared in step ① 2 o 3 -NiO / SiO 2 Place in a mixed atmosphere formed by hydrogen and carbon dioxide, and conduct reduction carbonization treatment at 400° C. for 2 hours to obtain the supported nickel-indium carbide alloy catalyst.

[0048] It is determined by plasma inductively coupled atomic emission spectrometry (ICP) that: in the catalyst prepared in th...

Embodiment 2

[0058] ① Weigh 10 grams of aluminum fiber felt (fiber diameter 50 microns; carrier ZT, expressed as Al-fiber) and immerse it in 100 ml of 0.1% sodium hydroxide aqueous solution, soak it at room temperature for 0.5 hours, Washed with distilled water, dried, and then calcined at 500 °C for 2 hours in an air atmosphere to prepare the monolithic carrier Al 2 o 3 / Al-fiber; Then, weigh 0.98 grams of indium nitrate trihydrate and 1.24 grams of nickel nitrate hexahydrate, ultrasonically dissolve them in 80 milliliters of distilled water to obtain a mixed aqueous solution containing nickel ions and indium ions; The monolithic support Al prepared by impregnating the mixed aqueous solution containing nickel ions and indium ions 2 o 3 / Al-fiber, after ultrasonication at room temperature for 0.5 hours and standing for 2 hours, after drying, and then roasting at 300°C in air atmosphere for 2 hours, the catalyst precursor was obtained, which was recorded as: In 2 o 3 -NiO / Al 2 o 3 / Al...

Embodiment 3

[0063] 1. At room temperature, dissolve ammonium chloride (15 mmol) and oxalic acid (100 mmol) in 50 milliliters of water, move the resulting solution into a hydrothermal reaction kettle, weigh 5 grams of foamed nickel (opening 100 PPI, expressed as Ni-foam) immersed in it, kept at 100 ° C for 24 hours, cooled naturally, dried after washing, and obtained a supported nickel-based catalyst precursor with nickel oxalate grown in situ on the foamed nickel carrier, abbreviated as: NiC 2 o 4 / Ni-foam;

[0064] ② Use an aqueous solution containing 1.79 grams of indium nitrate trihydrate to impregnate 5 grams of NiC prepared in step ① at room temperature. 2 o 4 / Ni-foam, after drying, bake in air at 450°C for 2 hours to obtain the catalyst precursor, denoted as: In 2 o 3 -NiO / Ni-foam;

[0065] ③The In prepared in step ② 2 o 3 -NiO / Ni-foam is placed in a mixed atmosphere formed by hydrogen, carbon monoxide and carbon dioxide, and subjected to reduction carbonization treatment a...

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Abstract

The invention discloses a load type carbonized nickel indium alloy catalyst and its preparation method and application. The load type carbonized nickel indium alloy catalyst is composed of a carrier and a carbonized nickel indium alloy loaded thereon; the catalyst has the general formula which is shown as InNixCy / ZT, wherein x is not more than 5 and not less than 1, y is not more than 1 and not less than 0.1; the mass percent of InNixCy / ZT in the load type carbonized nickel indium alloy catalyst is 1-40%, and the allowance is carrier. The load type carbonized nickel indium alloy catalyst is featured by stable structure, good thermal conductivity, high permeability, high conversion rate and selectivity, high activity, high mechanical strength, easy shaping, and easiness in filling, high flux and low pressure drop, and others; the catalyst can meet requirements of strong suction / exothermic reaction in chemical industrial process on fast thermal / mass transfer, and good catalytic performance; the catalyst is excellent catalyst for reversed water gas shift reaction, dimethyl oxalate hydrogenated glycol reaction, and carbon dioxide hydrogenated methanol reaction.

Description

technical field [0001] The present invention relates to a kind of catalyst and its preparation method and application, specifically, relate to a kind of supported nickel indium carbide catalyst and its preparation method and its inverse water gas shift reaction, dimethyl oxalate hydrogenation ethylene glycol The application in the reaction and the reaction of hydrogenation of carbon dioxide to methanol belongs to the technical field of catalysis. Background technique [0002] Carbon dioxide is the most important greenhouse gas, and the thermal energy utilization of fossil energy produces a large amount of CO 2 , has destroyed the carbon balance of the earth's ecosystem and seriously threatened the sustainable development of human beings. Therefore, CO 2 Translational and applied research in China is becoming more and more active. will CO 2 As a cheap and abundant C1 resource, it can be efficiently converted with hydrogen produced by renewable energy to produce useful chem...

Claims

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Application Information

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IPC IPC(8): B01J27/22C01B3/16C07C29/149C07C31/20
CPCB01J27/22C01B3/16C07C29/149C07C31/202Y02P20/00Y02P20/52
Inventor 路勇陈鹏静朱坚赵国锋刘晔
Owner EAST CHINA NORMAL UNIV
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