Molecular sieve adsorbent for separating oxygen from air by means of pressure swing adsorption and preparation method thereof

A pressure swing adsorption and molecular sieve technology, applied in separation methods, oxygen preparation, chemical instruments and methods, etc., can solve the problems of high cost, high price and complicated preparation process of adsorbents, and achieve good oxygen and nitrogen separation performance and high adsorption speed Fast and large adsorption capacity

Active Publication Date: 2013-03-06
LUOYANG JALON MICRO NANO NEW MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] U.S. Patent US4557736 reported X-zeolite exchanged by divalent cation calcium and strontium, claiming that it has higher nitrogen adsorption capacity and better nitrogen selectivity in air separation, but strontium resources are scarce and expensive
Chinese patent CN1034913 reported the use of divalent cation-exchanged lithium X zeolite adsorbent for oxygen and nitrogen separation, which improved the oxygen and nitrogen separation capacity, and the divalent cation was selected from Ba 2+ 、Co 2+ 、Cu 2+ 、Cr 2+ , Fe 2+ , Mg 2+ , Mn 2+ , Zn 2+ , but Li is still the main component, Li is expensive, and the preparation process is complicated, the utilization rate of Li is low, and the cost of the adsorbent is high.
However, it is difficult and expensive to prepare lithium-exchanged X-zeolite with high exchange degree, which makes the cost of adsorbent very high.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] First mix and grind 80 grams of CaLSX molecular sieve on a dry basis with 20 grams of binder (25% sheepsan and 75% kaolin), pass through a 120-mesh sieve, then mix wet with an appropriate amount of 5% acrylic latex solution, and extrude into a diameter of 1. Smm strips were dried at 100°C, processed into columnar particles of 2-3mm, and roasted at 525°C for 3 hours under the condition of dry air to obtain the finished CaLSX molecular sieve adsorbent, and its compressive strength was measured to be 55N / particle.

[0031] Put 1 gram of the finished bar into the BET sample tube, raise the temperature to 370°C, and at the same time evacuate to 2 , its pressure is 760mmHg, measure its saturated N 2 The adsorption capacity is 22.35ml / g, and the same method is used to measure O 2 The saturated adsorption capacity is 4.26ml / g, and the ratio of the moles of the saturated adsorption capacity of oxygen and nitrogen is regarded as the separation capacity of oxygen and nitrogen, the...

Embodiment 2

[0033]The operation is the same as in Example 1, only the CaLSX molecular sieve is changed to 85g, the binder is changed to 15g, and the calcination temperature is 535°C.

[0034] The obtained finished CaLSX molecular sieve adsorbent has a compressive strength of 45N / particle.

[0035] saturated N 2 The adsorption capacity is 26.90ml / g, O 2 Its saturated adsorption capacity is 5.03ml / g, and its oxygen and nitrogen separation ability is 4.69.

[0036] Test condition is also with embodiment 1.

Embodiment 3

[0038] First mix and grind 82.5 kg of dry base CaLSX powder with 17.5 kg of binder (25% sheepsan and 75% kaolin), pass through a 120-mesh sieve, and then add 5% of the mixed powder and co-binding agent on the rolling ball machine Roll the acrylic latex solution into 1.5mm pellets, dry them at 100°C, pass through dry air with a dew point lower than -40°C at 530°C, and bake them for 3 hours. The measured strength is 51N / ball.

[0039] Saturation N measured on BET 2 The adsorption capacity is 25.5ml / g, saturated with O 2 The adsorption capacity is 4.65ml / g, and its oxygen and nitrogen separation ability is 4.80.

[0040] Test condition is also with embodiment 1.

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Abstract

The invention provides a molecular sieve adsorbent for separating oxygen from air by means of pressure swing adsorption and a preparation method thereof. The molecular sieve adsorbent comprises the following components based on parts by weight percent: 80-95% of CaLS molecular sieve with SiO2 / Al2O3=2.0, and 5-20% of binder. The preparation method comprises the steps of: preparing sodium potassium type low-silicon X type molecular sieve KNaLSX with SiO2 / Al2O3=2.0; exchanging 0.5-1.5ml of CaCl2 solution with the KNaLSX molecular sieve at 80-85 DEG C for 1-2h; washing and drying; mixing the molecular sieve with the binder; smashing; wetly stirring with auxiliary binder; drying to be shaped; and roasting at 450-550 DEG C for 1-5h. Compared with the prior art, the adsorbent has high Ca2+exchange degree, high molecular sieve crystallinity, large absorption quantity, fast absorption speed, low cost and good oxygen-nitrogen separation performance.

Description

technical field [0001] The invention relates to a molecular sieve adsorbent technology, in particular to a molecular sieve adsorbent for pressure swing adsorption air separation and oxygen production and a preparation method thereof. Background technique [0002] Low-silicon X-type molecular sieve, referred to as LSX, its SiO 2 / Al 2 o 3 It is 2.0-2.1, its cation position reaches the maximum and has the most adsorption centers, while the cation of the synthetic LSX molecular sieve is Na + and K + , directly used as pressure swing adsorption air separation oxygen generation adsorbent, its oxygen and nitrogen separation coefficient is not significantly higher than that of traditional air separation oxygen generation molecular sieve adsorbent 5A type molecular sieve and ordinary X type molecular sieve. Ordinary X-type molecular sieve, its SiO 2 / Al 2 o 3 2.35-2.50, the cation is Na + , also known as NaX. Therefore, Na must be + and K + Change to other metal cations, ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/18B01J20/30B01D53/047C01B13/02
Inventor 李宏愿魏渝伟庞玲玲尹伟民王玉峰何连清
Owner LUOYANG JALON MICRO NANO NEW MATERIALS CO LTD
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