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A high-temperature catalytic combustion catalyst for washing tail gas with liquid nitrogen, its preparation method and application

A combustion catalyst and high-temperature catalysis technology, applied in combustion methods, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problem of catalyst deactivation, low catalyst thermal stability, and difficulty in realizing high-temperature catalytic combustion of liquid nitrogen washing tail gas, etc. problems, to achieve the effect of improving catalytic activity, promoting oxygen transport capacity, and efficient and rapid catalytic oxidation

Active Publication Date: 2020-09-22
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the calorific value of liquid nitrogen scrubbing tail gas can reach 1200-2100kJ / m 3 , during direct catalytic combustion, the temperature of the reaction catalyst is continuously around 800°C, up to 950°C, and the high temperature of the catalyst center can easily lead to the deactivation of the catalyst due to sintering
At present, the thermal stability of existing catalysts is low, and it is difficult to realize high-temperature catalytic combustion of liquid nitrogen scrubbing tail gas

Method used

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  • A high-temperature catalytic combustion catalyst for washing tail gas with liquid nitrogen, its preparation method and application

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preparation example Construction

[0031] The present invention provides a method for preparing a high-temperature catalytic combustion catalyst for washing tail gas with liquid nitrogen described in the above technical solution, comprising the following steps:

[0032] 1) mixing lanthanum nitrate, manganese nitrate, a first metal nitrate compound, citric acid and water, and complexing the obtained first mixture to obtain a gel;

[0033] 2) performing a first calcination on the gel to obtain a first carrier product;

[0034] 3) mixing the first carrier product, aluminum nitrate, the second metal nitrate compound and water, and performing a precipitation reaction on the obtained second mixture under the action of a buffer to obtain a precipitate;

[0035] 4) Carrying out the second roasting of the precipitate to obtain the second carrier product;

[0036] 5) immersing the second carrier product in a palladium nitrate solution for impregnation, and then drying the obtained mixture in sequence and third roasting ...

Embodiment 1

[0054] Weigh 86.21g of lanthanum nitrate, 35.10g of manganese nitrate and 3.39g of yttrium nitrate in a beaker of 1000mL deionized water, stir at 1500rpm for 30min to form a homogeneous solution, then add 84.29g of citric acid, wherein citric acid and total metal atoms The molar ratio is 1:1. After stirring evenly, transfer to a water bath for heating, stir in a constant temperature water bath at 80°C for 4 to 6 hours to form a wet gel, and then dry at 80°C for 2 days to obtain a xerogel. After grinding the glue to 100 mesh, carry out the first roasting at 500°C for 3 hours to obtain the first carrier product; weigh 353.06g aluminum nitrate, 1.70g barium nitrate, and 2.70g lanthanum nitrate in a beaker of 1000mL deionized water, stir well , add 50g of the first carrier product, continue to stir to form a uniform turbid liquid, and carry out precipitation reaction with a buffer prepared with a molar ratio of sodium carbonate and ammonia water of 1:1. After the precipitation reac...

Embodiment 2

[0056] Take by weighing 86.21g lanthanum nitrate, 35.10g manganese nitrate and 3.39g yttrium nitrate in the beaker that 1000mL deionized water is housed, stir under 1300rpm rotating speed and form homogeneous solution, then add 84.29g citric acid in described solution, wherein The molar ratio of citric acid to total metal atoms is 1:1. After stirring evenly, transfer to a water bath for heating, and stir at 80°C for 4h to form a wet gel. Dry the wet gel at 80°C for 2d to obtain dry coagulation After grinding the xerogel to 80 mesh, the first calcination was carried out at 500°C for 3 hours to obtain the first carrier product; weigh 353.06g of aluminum nitrate, 1.70g of barium nitrate, and 2.75g of zirconium nitrate in 1000mL of deionized water In the beaker, after stirring evenly, add 50g of the first carrier product, continue to stir to form a uniform turbid liquid, carry out the precipitation reaction with a buffer prepared with a molar ratio of sodium carbonate and ammonia w...

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Abstract

The invention belongs to the technical field of tail gas combustion catalyst, and especially relates to a liquid nitrogen washed tail gas high temperature catalytic combustion catalyst, and a preparation method and applications thereof. The liquid nitrogen washed tail gas high temperature catalytic combustion catalyst possesses a stable structure and large specific surface area; after 5h of roasting aging of the catalyst at 1000 DEG C in the air, the specific surface area is still larger than 40m<2> / g. The catalyst is capable of realizing stable high efficiency reaction of liquid nitrogen washed tail gas catalytic combustion at 800 DEG C for longer than 10000h, liquid nitrogen washed tail gas catalytic combustion efficiency is extremely high, liquid nitrogen washed tail gas CO concentration can be reduced to be lower than 50ppm, CH4 concentration can be reduced to be lower than 300ppm, H2 can be removed completely, and energy saving emission reducing effect is obvious.

Description

technical field [0001] The invention relates to the technical field of tail gas combustion catalysts, in particular to a high-temperature catalytic combustion catalyst for washing tail gas with liquid nitrogen and its preparation method and application. Background technique [0002] At present, the main method of producing synthetic ammonia in my country is the coal-to-gas process, but the synthetic gas produced from coal needs to be refined to remove impurity components to obtain pure H 2 to avoid poisoning of the subsequent ammonia synthesis catalyst. At present, the use of liquid nitrogen washing method to finely remove trace CO and other impurity components in coal gas is a commonly used process in large-scale ammonia synthesis plants. The crude hydrogen after decarburization is washed and purified by liquid nitrogen and then used to prepare synthetic ammonia, and the tail gas discharged from the liquid nitrogen after absorbing impurity components such as CO in the crud...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/656B01J35/10F23G7/07
CPCB01J23/002B01J23/6562B01J35/1014B01J2523/00F23G7/07F23G2209/14B01J2523/25B01J2523/31B01J2523/36B01J2523/3706B01J2523/72B01J2523/824B01J2523/48B01J2523/24
Inventor 张秋林宁平王继封
Owner KUNMING UNIV OF SCI & TECH
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