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Catalyst for production of C2H4 through CO2 oxidized C2H6 dehydrogenation and preparation method of catalyst

A carbon dioxide and ethane oxidation technology, applied in carbon compound catalysts, physical/chemical process catalysts, catalysts, etc., can solve problems such as weak carbon dioxide adsorption capacity and poor hydrothermal stability

Active Publication Date: 2019-03-08
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In order to solve the technical problems of poor hydrothermal stability and weak carbon dioxide adsorption capacity of the existing supported Cr catalyst carrier, the present invention provides a catalyst for producing ethylene and synthesis gas by oxidizing ethane and dehydrogenating carbon dioxide and a preparation method thereof

Method used

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  • Catalyst for production of C2H4 through CO2 oxidized C2H6 dehydrogenation and preparation method of catalyst
  • Catalyst for production of C2H4 through CO2 oxidized C2H6 dehydrogenation and preparation method of catalyst
  • Catalyst for production of C2H4 through CO2 oxidized C2H6 dehydrogenation and preparation method of catalyst

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Experimental program
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Effect test

Embodiment 1

[0025] 0.93g of Cr(NO 3 ) 3 9H 2 O was dissolved in 24g of deionized water, and after stirring evenly, 10g of SSZ-13 microporous molecular sieve carrier was added, and then soaked in a constant temperature water bath at 80°C for 2h, and then the obtained mixture was centrifuged, and the separated solid was dried at 110°C for 10h, and then 540 ℃ calcination for 3 hours to obtain CO 2 Oxygen C 2 h 6 Dehydrogenation to C 2 h 4 The catalyst, the mass fraction of chromium in the catalyst is 0.3%, denoted as Cr 0.3 / SSZ-13.

Embodiment 2

[0027] 1.56g, 2.21g and 4.94g of Cr(NO 3 ) 3 9H 2 O was dissolved in 24g of deionized water to prepare solutions with different Cr content. After stirring evenly, 10g of SSZ-13 microporous molecular sieve carrier was added, and then soaked in a constant temperature water bath at 80°C for 2h, and then the obtained mixture was centrifuged to separate the obtained The solid was dried at 110°C for 10h, and then calcined at 540°C for 3h to obtain CO 2 Oxygen C 2 h 6 Dehydrogenation to C 2 h 4 The catalyst, the mass fraction of chromium element in the catalyst is 0.5%, 0.7% and 1.5%, respectively denoted as Cr 0.5 / SSZ-13,Cr 0.7 / SSZ-13 and Cr 1.5 / SSZ-13.

Embodiment 3

[0029] 62.18g of Cr(NO 3 ) 3 9H 2 O was dissolved in 24g of deionized water, and after stirring evenly, 10g of SSZ-13 microporous molecular sieve carrier was added, and then soaked in a constant temperature water bath at 80°C for 2h, and then the obtained mixture was centrifuged, and the separated solid was dried at 110°C for 10h, and then 540 ℃ calcination for 3 hours to obtain CO 2 Oxygen C 2 h 6 Dehydrogenation to C 2 h 4 The catalyst, the mass fraction of chromium in the catalyst is 10%, denoted as Cr 10 / SSZ-13.

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Abstract

The invention discloses a supported catalyst for production of C2H4 through CO2 oxidized C2H6 dehydrogenation. The catalyst comprises a molecular sieve carrier and an active component, wherein the molecular sieve carrier is a SSZ-13 microporous molecular sieve with the pore diameter size range being 0.2-0.4 nm; the active component is oxide of chromium, and the mass fraction of chromium in the catalyst is 0.3%-10%. The SSZ-13 microporous molecular sieve has the advantages of small holes, high hydrothermal stability and high specific surface area, has more surface protonic acid centers and exchangeable cations and has better affinity to CO2, more CO2 molecules can participate in activation of C2H6 and following conversion reactions, the catalyst with high C2H6 content and CO2 co-conversioncapacity is obtained by introducing chromium elements in the carrier, and the problems of weak CO2 adsorption capacity and poor carrier hydrothermal stability of catalysts in the prior art can be effectively solved.

Description

technical field [0001] The invention belongs to the technical field of preparing ethylene, and in particular relates to a catalyst for oxidizing ethane with dehydrogenation of carbon dioxide to prepare ethylene and a preparation method thereof. Background technique [0002] Carbon dioxide is the final oxide of carbon and carbon-containing compounds, and it is also the most abundant carbon source in nature. Among the "greenhouse gases" that cause global warming, carbon dioxide contributes 55% to the greenhouse effect. Therefore, it is very important to carry out research on the resource utilization of carbon dioxide. Carbon dioxide molecules are very stable, and a large number of studies have shown that hydrogen can effectively activate the carbon-oxygen bonds of carbon dioxide molecules, which is a hot research direction for resource utilization of carbon dioxide. However, the high cost of industrial hydrogen production technology leads to high cost of raw materials, which ...

Claims

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Application Information

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IPC IPC(8): B01J29/78C07C5/42C07C11/04
CPCC07C5/42B01J29/783C07C2529/78B01J2229/20C07C11/04Y02P20/52
Inventor 谢宏彬杨金鹏刘家旭贺宁郭洪臣
Owner DALIAN UNIV OF TECH
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