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Application and preparation of perovskite structure composite oxide in chemical looping circulation hydrogen production

A technology of perovskite structure and composite oxide, applied in the field of chemical chain hydrogen production, can solve the problems of high reaction temperature, limited oxygen carrying rate, low cyclic reactivity, etc. simple method effect

Inactive Publication Date: 2013-01-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Relatively speaking, the oxygen carrier NiO / NiAl 2 o 4 (CHO P etc. Fuel, 2004, 83(9)), Fe 2 o 3 / Al 2 o 3 (MATTISSON T etc. Fuel, 2001, 80 (13)) and CoO-NiO / YSZ (JIN H G etc. Energy Fuels, 1998, 12 (6)) have better overall performance, but there are limited oxygen loading rates and cyclic reactions low resistance, inability to withstand high reaction temperature, low dispersion of metal oxides in oxygen carriers, etc.

Method used

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  • Application and preparation of perovskite structure composite oxide in chemical looping circulation hydrogen production
  • Application and preparation of perovskite structure composite oxide in chemical looping circulation hydrogen production

Examples

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Effect test

Embodiment 1

[0018] Take 23g Ni(NO 3 ) 2 ·6H 2 O, put it into a 500mL beaker, add 100mL of distilled water, and then place the beaker in a water bath at 80°C with a stirring speed of 400rpm. Take 34.3g La(NO 3 ) 3 ·6H 2 O, put it in a beaker with 100mL distilled water, stir until it is completely dissolved. Then add the lanthanum nitrate solution dropwise into the nickel nitrate solution, and stir while adding dropwise. Take 40g of citric acid, the molar ratio of citric acid to the total amount of metal ions is 1.2:1, put it into a 100mL beaker and stir until it is completely dissolved. After the above mixed solution is stirred for 30 minutes, slowly add the citric acid solution, while adding While stirring. After stirring for 5 hours, the solution had been dehydrated and turned into a viscous gel. The gel was taken out and placed in a drying oven at 110° C. to dry overnight. Then take out the dried perovskite precursor, place it in a muffle furnace, raise the temperature from room...

Embodiment 2

[0020] Take 23g Ni(NO 3 ) 2 ·6H 2 O, put it into a 500mL beaker, add 100mL of distilled water, and then place the beaker in a water bath at 80°C with a stirring speed of 400rpm. Take 34.3g La(NO 3 ) 3 ·6H 2 O, put it in a beaker with 100mL distilled water, stir until it is completely dissolved. Then add the lanthanum nitrate solution dropwise into the nickel nitrate solution, and stir while adding dropwise. Take 67g of citric acid, the molar ratio of citric acid to the total amount of metal ions is 2:1, put it into a 100mL beaker and stir until it is completely dissolved. After the above mixed solution is stirred for 30 minutes, slowly add the citric acid solution, while adding While stirring. After stirring for 5 hours, the solution had been dehydrated and turned into a viscous gel. The gel was taken out and placed in a drying oven at 110° C. to dry overnight. Then take out the dried perovskite precursor, place it in a muffle furnace, raise the temperature from room t...

Embodiment 3

[0022] Take 23g Ni(NO 3 ) 2 ·6H 2O, put it into a 500mL beaker, add 100mL of distilled water, and then place the beaker in a water bath at 80°C with a stirring speed of 400rpm. Take 34.3g La(NO 3 ) 3 ·6H 2 O, put it in a beaker with 100mL distilled water, stir until it is completely dissolved. Then add the lanthanum nitrate solution dropwise into the nickel nitrate solution, and stir while adding dropwise. Take 100g of citric acid, the molar ratio of citric acid to the total amount of metal ions is 3:1, put it into a 100mL beaker and stir until completely dissolved, after stirring the above mixed solution for 30 minutes, slowly add the citric acid solution, dropwise While stirring. After stirring for 5 hours, the solution had been dehydrated and turned into a viscous gel. The gel was taken out and placed in a drying oven at 110° C. to dry overnight. Then take out the dried perovskite precursor, place it in a muffle furnace, raise the temperature from room temperature t...

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Abstract

The invention discloses application and preparation of perovskite structure composite oxide in chemical looping circulation hydrogen production. The perovskite structure composite oxide is composite metallic oxide with a perovskite ABO3 structure, A bit is rare earth metal lanthanum, and B bit is transition metallic nickel. The reaction temperature of the oxygen carrier in fuel is 600-1200 DEG C, and the reaction temperature of the oxygen carrier in steam is 600-1200 DEG C. The preparation process comprises the following steps: taking nickel nitrate and lanthanum nitrate as a precursor, and taking citric acid as a complexing agent to prepare into a solution, evenly mixing and stirring; carrying out water evaporation, so that the solution is changed from transparent sol to thick gel; and drying, and finally roasting, so that the roasted sample is the perovskite structure composite metal oxide. The oxygen carrier is high in oxygen carrying rate, high in activity and good in stability.

Description

technical field [0001] The invention relates to the application and preparation method of a perovskite structure composite oxide in chemical chain cycle hydrogen production technology, belonging to the field of chemical chain hydrogen production. Background technique [0002] To control CO during coal-fired electricity generation 2 CO2 emissions related to improving power generation efficiency and using other fuels with lower C / H and renewable resources 2 control route compared to coal and other fossil fuels during electricity production for CO 2 Recovery and storage (CCS) is the only effective way to achieve effective CO emission reductions in the short term 2 target, but the three COs to which CCS belongs 2 Emission reduction methods (including pre-combustion, oxy-combustion and post-combustion) and related technologies can achieve CO 2 recovery target, but would result in lower system efficiency and CO 2 The increase in recovery cost makes the CO 2 The popularizatio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/02B01J23/83
Inventor 梁皓倪向前张舒冬张喜文
Owner CHINA PETROLEUM & CHEM CORP