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Composite oxide as well as preparation method and application thereof

A composite oxide, oxide technology, applied in chemical instruments and methods, catalyst activation/preparation, iron compounds, etc., can solve the problems of unbearable, high reaction temperature, low hydrogen production rate, etc.

Pending Publication Date: 2022-05-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Relatively speaking, oxygen carriers in the prior art generally have shortcomings such as limited oxygen carrying capacity, low cycle reactivity, inability to withstand high reaction temperature, and low hydrogen production rate.

Method used

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  • Composite oxide as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] Weigh a certain amount of ferric nitrate, cerium nitrate and titanium sulfate and dissolve them in deionized water, heat to 70°C, then slowly add concentrated ammonia water to the solution under stirring conditions to ensure that the pH value of the slurry is at 7.5, and after complete precipitation , left to age for 3 hours, filtered, and repeatedly washed with deionized water to neutrality, the obtained sample was dried and calcined at a drying temperature of 100°C for 24 hours. The calcination temperature is 580° C., and the calcination time is 8 hours. Obtain the composition formula of the final composite oxide as CeFe 18 Ti 5 o 39 Denoted as C1.

Embodiment 2

[0059]Weigh a certain amount of ferric nitrate, cerium nitrate and titanium sulfate and dissolve them in deionized water, heat to 80°C, then slowly add concentrated ammonia water to the solution under stirring conditions to ensure that the pH value of the slurry is at 9, and after complete precipitation , left to age for 10 hours, filtered, washed repeatedly with deionized water until neutral, then dried and calcined, the drying temperature was 150°C, and the drying time was 8 hours. The calcination temperature is 680° C., and the calcination time is 4 hours. Obtain the final composite oxide composition with the formula CeFe 24 Ti 15 o 68 Denoted as C2.

Embodiment 3

[0061] Weigh a certain amount of ferric nitrate, cerium nitrate and titanium sulfate and dissolve them in deionized water, heat to 75°C, then slowly add concentrated ammonia water to the solution under stirring conditions to ensure that the pH value of the slurry is at 8.3, and after complete precipitation , left to age for 6 hours, filtered, washed with deionized water repeatedly until neutral, then dried and calcined, the drying temperature was 120°C, and the drying time was 12 hours. The calcination temperature is 600° C., and the calcination time is 6 hours. Obtain the final composite oxide composition with the formula CeFe 20 Ti 10 o 52 Denote it as C3.

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Abstract

The invention discloses a composite oxide and a preparation method and application thereof. The composition of the composite oxide is represented by a formula CeFexTiyO delta-alpha, x is equal to 5-35, y is equal to 1-25, delta is a positive number and represents a value when oxygen in the composite oxide reaches valence equilibrium, and alpha is equal to 0-delta / 2. The method for producing a composite oxide includes a step in which a Ce source, an Fe source, and a Ti source are brought into contact and reacted to obtain a composite oxide. The composite oxide used as an oxygen carrier for chemical looping hydrogen production has the advantages of high activity, good stability, high hydrogen yield and the like.

Description

technical field [0001] The invention relates to a composite oxide, its preparation method and application, in particular to a composite oxide, its preparation method and its application in chemical looping combustion. Background technique [0002] At present, the methods of large-scale hydrogen production in industry are mainly hydrogen production by steam reforming of natural gas and hydrogen production by coal gasification. Hydrogen production by steam reforming of natural gas is a strong endothermic reaction, which needs to burn part of the fuel to provide the heat energy required for the reaction. It is generally carried out in a tubular reactor (or reformer tube), and the hydrogen production efficiency per unit volume is low, requiring the construction of a large-scale device , High equipment investment; Coal gasification hydrogen production is the crude synthesis gas obtained after partial oxidation and gasification of coal undergoes a shift reaction to obtain a shift ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G49/00C01B3/40B01J23/83B01J37/03B01J37/08
CPCC01G49/009C01B3/40C01B3/36B01J23/83B01J23/002B01J37/031B01J37/082B01J2523/00C01B2203/1041C01B2203/1082C01B2203/1241B01J2523/3712B01J2523/47B01J2523/842B01J2523/41B01J2523/22B01J2523/31Y02P20/52
Inventor 李杰张信伟刘全杰李红营王海洋郭志芳
Owner CHINA PETROLEUM & CHEM CORP