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Preparation method of 5A molecular sieve adsorbent

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

Active Publication Date: 2017-03-08
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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  • Preparation method of 5A molecular sieve adsorbent

Examples

Experimental program
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Effect test

example 1

[0030] Take 50kg of NaA molecular sieve raw powder and 8kg of CaO fine powder (purity: 99% by mass) with a particle size less than 50 μm and mix them uniformly to form a mixed powder. Take 45kg of mixed powder and put it into a high-speed granulator, spray 25kg of deionized water while rolling and sprinkle the remaining mixed powder, sieve the formed pellets, and take pellets with a particle size of 0.3-0.8mm in 100 Dry at ℃ for 4 hours, roast at 550℃ for 4 hours, wash with deionized water at 90℃ until the pH of the washing solution is less than 10, dry at 80℃ for 4 hours, and activate in air at 350℃ for 3 hours 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: 99% by mass) with a particle size less than 50 μm and mix them uniformly to form a mixed powder. Put 40kg of mixed powder into the sugar coating pan, spray 27kg of deionized water while rolling and sprinkle the remaining mixed powder, sieve the formed pellets, take pellets with a particle size of 0.3-0.8mm and dry at 110°C 4h, roasted at 570°C for 3.5h, then washed with deionized water at 95°C until the pH of the washing solution was less than 10, dried at 80°C for 4h, and activated in air at 400°C for 2h to prepare 5A molecular sieve adsorbent A-2, whose physical and chemical properties are shown in the table 1.

example 3

[0034] Get 50kg of NaA molecular sieve former powder, 15kg of CaO fine powder (purity is 99% by mass) and 20kg of deionized water with a particle size less than 50 μm and mix evenly, then press it into a tablet form with a rotary tablet press at 100MPa, crush and sieve, Take particles with a particle size of 0.3-0.8 mm, dry at 120°C for 3 hours, bake at 600°C for 2.5 hours, wash with deionized water at 93°C until the pH of the washing solution is less than 10, dry at 80°C for 4 hours, and activate in air at 450°C for 2 hours , and obtained 5A molecular sieve adsorbent A-3, whose physicochemical 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 invention is a preparation method of a spherical adsorbent, specifically, a preparation method of a 5A molecular sieve adsorbent. Background technique [0002] The separation of normal paraffins from various petroleum products has important economic value, for example, the separation of normal paraffins from gasoline fractions can significantly increase the octane number of gasoline; the separation of C from kerosene fractions 10 ~C 14 The n-paraffins can be used to make detergents; the C separated from the diesel fraction 14 + N-alkanes can be used to synthesize high value-added products such as petroleum protein, chlorinated paraffins, plasticizers, and lubricating oil additives; the separation of n-alkanes 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 ran...

Claims

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Application Information

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