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Modified lithium low-silicon zeolite molecular sieve and preparation method thereof

A technology of zeolite molecular sieve and silicon molecular sieve, which is applied in the direction of separation method, molecular sieve catalyst, crystalline aluminosilicate zeolite, etc., can solve the problems of less research on adsorption performance, and achieve superior selective adsorption performance, improved adsorption performance, and large pore size. Effect

Pending Publication Date: 2021-09-07
SICHUAN TIANYI SCI & TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0012] The present invention aims at the problems that the existing molecular sieve adsorbents have to improve the adsorption capacity and adsorption separation efficiency of nitrogen, methane and carbon monoxide, and the present situation that low-silica zeolite molecular sieves have little research on the adsorption properties of methane and carbon monoxide, and provides a modified lithium low-silica zeolite Molecular sieve: The modified lithium low-silica zeolite molecular sieve can significantly increase the adsorption capacity of nitrogen, methane, and carbon monoxide, and has wide application potential in the fields of oil and gas separation, fine chemical industry, adsorption exchange, and gas separation and purification.

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  • Modified lithium low-silicon zeolite molecular sieve and preparation method thereof

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preparation example Construction

[0042] A method for preparing the modified low-silica X zeolite molecular sieve described above, comprising the following steps:

[0043] 1) Raw powder pretreatment

[0044] Dry sodium-type low silica X zeolite molecular sieve (Na-LSX) powder at 100-15°C for 1-3 hours, then heat up to 400-550°C at a rate of 5-10°C per minute and roast for 1-4 hours. hours, put it in a desiccator to cool for later use;

[0045] 2) Ion modification

[0046] 2.1) Lithium ion solution modification

[0047] Mix the above-mentioned pretreated Na-LSX raw powder with 0.1-0.5mol / L lithium ion solution, so that the molar ratio of sodium ions in the Na-LSX raw powder to lithium ions in the solution is within the range of 1:0.4-1:2.0 , and stirred at 85-95°C for 1-2 hours, then filtered and washed; the washed solid powder was re-added to the above-mentioned lithium chloride solution, and the above-mentioned process was repeated, so that the lithium-ion exchange degree was within the range of 65-99%. E...

Embodiment 1

[0064] Take 100g of pretreated Na-LSX zeolite molecular sieve and mix it with a lithium chloride solution with a concentration of 0.5mol / L, so that the molar ratio of sodium ions in the original Na-LSX powder to lithium ions in the solution is 1.5, and maintain at 85°C under stirring Constant temperature for 2 hours, filter and wash; mix the washed sample with the above lithium chloride solution again, repeat the mixing, constant temperature stirring, filter and wash for a total of 3 times, then dry the sample at 100°C for 2 hours, and then bake it at 450°C for 1 After 1 hour, the (Li, Na)-LSX zeolite molecular sieve was obtained.

[0065] The above-mentioned low-silicon molecular sieve modified by lithium ions is fully mixed with a 20% mass ratio binder, and the binder is sheepskin; forming adopts rolling ball molding. The formed spherical molecular sieve is calcined under vacuum or inert gas protection in the temperature range of 400°C for 12 hours, and cooled under the prot...

Embodiment 2

[0068] Take 10g of pretreated Na-LSX zeolite molecular sieve and mix it with a lithium nitrate solution with a concentration of 0.1mol / L, so that the molar ratio of sodium ions in the original Na-LSX powder to lithium ions in the solution is 0.6, and maintain a constant temperature of 95°C under stirring for 2 hours, filtered and washed; the washed sample was re-mixed with the above lithium nitrate solution, repeated mixing, constant temperature stirring, filtered and washed twice, and then the sample was dried at 100°C for 3 hours, and then roasted at 450°C for 1 hour to obtain (Li, Na)-LSX zeolite molecular sieve.

[0069] The above-mentioned low-silicon molecular sieve modified by lithium ions is fully mixed with a 5% mass ratio binder, and the binder is kaolin; extrusion molding is adopted for molding. The strip-shaped molecular sieve after forming is roasted for 2 hours under vacuum or inert gas protection within the temperature range of 550°C, and cooled under the protec...

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Abstract

The invention relates to a low-silicon X-type modified zeolite molecular sieve applied to adsorption of nitrogen, methane, carbon monoxide and other gases, and the molecular sieve can be used in various fields of gas adsorption separation, catalysis, ion exchange and the like, in particular to a modified lithium low-silicon zeolite molecular sieve and a preparation method thereof. According to the molecular sieve, low-silicon X-type zeolite molecular sieve raw powder is used as a raw material, sodium ions in Na-LXS are removed through lithium ion exchange, the modified zeolite molecular sieve remarkably improves the adsorption capacity of nitrogen, methane, carbon monoxide and other gases, and the molecular sieve can be widely applied to the fields of catalysis, ion exchange, adsorption separation and the like.

Description

technical field [0001] The invention relates to a low-silicon X-type modified zeolite molecular sieve applied to adsorb nitrogen, methane, carbon monoxide and other gases. A silicalite molecular sieve and a preparation method thereof. Background technique [0002] The X-type zeolite molecular sieve with a faujasite structure (FAU) and a silicon-aluminum atomic ratio in the range of 1.0 to 1.1 is called a low-silicon X-type zeolite molecular sieve (LSX for short), and its synthetic raw powder is basically composed of sodium ion (Na -LXS), which has attracted much attention because of its crystal framework with high charge density and large pore size, which has good adsorption properties. [0003] The gas separation effect of LXS is due to the interaction between the cation electric field in the molecular sieve and the gas. This interaction is related to the position of the cation in the molecular sieve and the type of the cation. Due to the low silicon-aluminum atomic ratio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/18B01J20/28B01J20/30B01J29/08B01J35/02B01J35/08B01J35/10C01B39/22B01J35/00
CPCC01B39/22B01J20/186B01J20/2803B01J20/28019B01J20/28016B01J20/04B01J20/28057B01J20/28078B01J29/082B01D53/02B01D2257/102B01D2257/502B01D2257/7025C01P2006/16C01P2006/12B01J35/50B01J35/51B01J35/61B01J35/64Y02C20/20
Inventor 管英富张剑锋杨云李旭李娅玲梁力友
Owner SICHUAN TIANYI SCI & TECH