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Silver exchange molecular sieve adsorbent for efficiently separating N2O/CO2 and preparation method of silver exchange molecular sieve adsorbent

A technology of molecular sieves and adsorbents, which is applied in the field of silver-exchanged molecular sieve adsorbents for efficient separation of N2O/CO2 and its preparation, can solve problems such as separation difficulties, and achieve the effects of simple preparation methods, good application prospects, and easy mass production

Active Publication Date: 2021-04-20
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In order to solve the N in the tail gas generated by adipic acid and nitric acid 2 O and CO 2 The problem of difficult separation, the invention discloses a high-efficiency separation of N 2 O / CO 2 The silver-exchanged molecular sieve adsorbent and preparation method thereof can be obtained from N 2 O and CO 2 Preferential adsorption of N in the mixed exhaust gas 2 O with better N 2 O / CO 2 seperate effect

Method used

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  • Silver exchange molecular sieve adsorbent for efficiently separating N2O/CO2 and preparation method of silver exchange molecular sieve adsorbent
  • Silver exchange molecular sieve adsorbent for efficiently separating N2O/CO2 and preparation method of silver exchange molecular sieve adsorbent
  • Silver exchange molecular sieve adsorbent for efficiently separating N2O/CO2 and preparation method of silver exchange molecular sieve adsorbent

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Effect test

Embodiment 1

[0030] A high-efficiency separation of N 2 O / CO 2 The preparation method of the silver-exchanged molecular sieve adsorbent is realized through the following steps:

[0031] (1) Add 1g of 13X molecular sieve to 60mL of 0.1mol / mL AgNO 3 In the aqueous solution, heat and stir at 80°C for 1 hour, perform a silver exchange, and keep the total amount of the solution unchanged during the heating process;

[0032] (2) The silver-exchanged molecular sieves in step (1) were washed with deionized water, filtered, and dried at 120°C for 24 hours to obtain silver-exchanged 13X molecular sieves;

[0033] (3) The silver-exchanged 13X molecular sieve obtained in step (2) was vacuum activated at 200°C for 5 hours to obtain Ag + The X-2 molecular sieve adsorbent with an exchange degree of 84%; then test the N of the X-2 molecular sieve 2 O / CO 2 gas adsorption separation performance.

Embodiment 2

[0035] A high-efficiency separation of N 2 O / CO 2 The preparation method of the silver-exchanged molecular sieve adsorbent is realized through the following steps:

[0036] (1) Add 1g of 5A molecular sieve to 60mL of 0.1mol / mL AgNO 3 In the aqueous solution, heat and stir at 80°C for 1 hour, perform a silver exchange, and keep the total amount of the solution unchanged during the heating process;

[0037] (2) The silver-exchanged molecular sieve in step (1) was washed with deionized water, filtered, and dried at 120°C for 24 hours to obtain a silver-exchanged 5A molecular sieve;

[0038] (3) Vacuumize and activate the 5A molecular sieve obtained in step (2) at 200°C for 5 hours to obtain Ag + The A-2 molecular sieve adsorbent with an exchange degree of 73%; then test the N of the A-2 molecular sieve 2 O / CO 2 gas adsorption separation performance.

Embodiment 3

[0040] A high-efficiency separation of N 2 O / CO 2 The preparation method of the silver-exchanged molecular sieve adsorbent is realized through the following steps:

[0041] (1) Add 1g of 13X molecular sieve to 70mL of 0.3mol / mL AgNO 3 solution, and then heated and stirred at 60°C for 2 hours to perform a silver exchange, keeping the total amount of the solution unchanged during the heating process;

[0042] (2) The silver-exchanged molecular sieves in step (1) were washed with deionized water, filtered, and dried at 100°C for 24 hours to obtain silver-exchanged 13X molecular sieves;

[0043] (3) The silver-exchanged 13X molecular sieve obtained in step (2) was vacuum activated at 180°C for 10 hours to obtain Ag + The X-3 molecular sieve adsorbent with an exchange degree of 88%; then test the N of the X-3 molecular sieve 2 O / CO 2 gas adsorption separation performance.

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Abstract

The invention belongs to the technical field of separation materials, and discloses a silver exchange molecular sieve adsorbent for efficiently separating N2O / CO2 and a preparation method of the silver exchange molecular sieve adsorbent, 13X and 5A molecular sieves are used as basic framework materials, and AgX and AgA molecular sieves with a certain Ag < + > exchange degree are prepared by adjusting and balancing cation composition. According to the invention, since the equilibrium cations are changed from alkali metals or alkaline earth metals to Ag < + >, the adsorbent shows excellent N2O preferential adsorption capacity, and has high selectivity and adsorption capacity for N2O / CO2. The adsorbent can be suitable for separating and recycling N2O in the tail gas generated in the industrial production process of nitric acid, adipic acid and the like, and has a good application prospect and a very important practical value.

Description

technical field [0001] The invention belongs to the technical field of separation materials and relates to a N 2 O and CO 2 The preparation method of separation material, especially relates to a kind of high-efficiency separation N 2 O / CO 2 Silver-exchanged molecular sieve adsorbent and preparation method thereof. Background technique [0002] Nitrous oxide (N 2 O, laughing gas) is the carbon dioxide (CO 2 ), methane (CH 4 ) after the third largest greenhouse gas, its greenhouse effect is 298 times that of carbon dioxide and it will cause damage to the stratospheric ozone. In addition, N 2 O has important applications in the fields of medicine, food, and aerospace. Therefore, for N 2 O Recycling has a double meaning. N 2 40% of O emissions are caused by human activities, mainly agriculture, transportation and industry. Industrially, during the production of adipic acid and nitric acid, N 2 O is often emitted as a by-product. At present, the industry for N 2 Th...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/18B01J20/30B01D53/02
CPCY02C20/10
Inventor 杨江峰王丽刘佳奇李晋平
Owner TAIYUAN UNIV OF TECH