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A kind of preparation method of 5a molecular sieve adsorbent

A molecular sieve and adsorbent technology, applied in the field of spherical adsorbent preparation, can solve the problems of reduced adsorption capacity, reduced adsorption selectivity and adsorption-desorption rate, etc., and achieve high methanol adsorption capacity, high compressive strength, and mass transfer efficiency high effect

Active Publication Date: 2019-03-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the addition of binder not only reduces the adsorption capacity, but also reduces the adsorption selectivity and adsorption-desorption rate.

Method used

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  • A kind of preparation method of 5a molecular sieve adsorbent

Examples

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Comparison scheme
Effect test

example 1

[0030] Take 50kg of NaA molecular sieve original powder and 8kg of CaO fine powder (purity of 99% by mass) with a particle size of less than 50 μm and mix uniformly to form a mixed powder. Take 45kg of mixed powder into the high-speed granulator, spray 25kg of deionized water and throw the remaining mixed powder while rolling, sieve the formed pellets, and take the pellets with a particle size of 0.3~0.8mm into 100 Drying at ℃ for 4h, roasting at 550℃ for 4h, then washing with deionized water at 90℃ until the pH of the washing solution is less than 10, drying at 80℃ for 4h, and activating in air at 350℃ for 3h to prepare 5A molecular sieve adsorbent A-1. Its physical and chemical properties See Table 1.

example 2

[0032] Take 50kg of NaA molecular sieve raw powder and 10kg of CaO fine powder (purity of 99% by mass) with a particle size of less than 50μm and mix uniformly to form a mixed powder. Take 40kg of mixed powder into the sugar-coating pan, spray 27kg of deionized water while rolling and throw the remaining mixed powder, sieve the formed pellets, and take pellets with a particle size of 0.3~0.8mm and dry at 110℃ 4h, roasted at 570℃ for 3.5h, washed with 95℃ deionized water until the pH of the washing solution was less than 10, dried at 80℃ for 4h, activated in the air at 400℃ for 2h to prepare 5A molecular sieve adsorbent A-2, its physical and chemical properties are shown in the table 1.

example 3

[0034] Take 50kg of NaA molecular sieve powder, 15kg of CaO fine powder (purity of 99% by mass) with a particle size of less than 50μm, and 20kg of deionized water and mix them evenly, then use a rotary tablet press to compress them into tablets at 100MPa, crush and screen them, Take particles with a particle size of 0.3~0.8mm, dry at 120℃ for 3h, roast at 600℃ for 2.5h, then wash with 93℃ deionized water until the pH value of the washing solution is less than 10, dry at 80℃ for 4h, activate in the air at 450℃ for 2h , Prepared 5A molecular sieve adsorbent A-3, its physical and chemical properties are shown in Table 1.

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Abstract

The method discloses a preparation method of a 5A molecular sieve adsorbent. The preparation method comprises (1) uniformly mixing NaA molecular sieve raw powder and CaO powder with particle sizes less than 50 microns according to a mass ratio of 75-95: 5-25 to obtain mixed powder, 2) uniformly mixing the mixed powder and water, carrying out tabletting or extrusion stripe formation and crushing the stripes to obtain granules, or spraying water into the mixed powder along with rolling so that rolling molding is realized, wherein the added water content of the mixed powder is 30-48% by mass, and selecting the particles or pellets with particle sizes of 0.3-0.8mm and drying them at 80 to 200 DEG C, and (3) roasting the dried particles or pellets at 500 to 700 DEG C, washing the roasting products through water until pH is less than 10, and carrying out activation at 350 to 500 DEG C to obtain the 5A molecular sieve adsorbent. The preparation method can prepare a binder-less 5A molecular sieve adsorbent without alkali treatment in-situ crystallization. The 5A molecular sieve adsorbent has a high adsorption capacity, a fast mass transfer rate and good compressive strength.

Description

Technical field [0001] The present invention is a preparation method of spherical adsorbent, specifically, a preparation method of 5A molecular sieve adsorbent. Background technique [0002] Separating n-paraffins from various petroleum products has important economic value. For example, separating n-paraffins from gasoline fractions can significantly increase the octane number of gasoline; separating C from kerosene fractions 10 ~C 14 The normal paraffins can be used to prepare detergent; C separated from diesel fraction 14 + Normal paraffins can synthesize high value-added products such as petroleum protein, chlorinated paraffins, plasticizers, lubricant additives, etc.; separation of normal paraffins and other hydrocarbons (isoparaffins, naphthenes and aromatics) in naphtha can optimize raw materials , Improve the efficiency of downstream ethylene and reforming units. The above-mentioned petroleum products have a wide distillation range, and the difference in boiling points be...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/18B01J20/30C10G25/00G01N5/02
Inventor 王红超王辉国王德华
Owner CHINA PETROLEUM & CHEM CORP