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Zeolite adsorbent and its preparation method

A technology of adsorbent and zeolite, which is applied in the field of zeolite adsorbent and its preparation, can solve the problems of large particle size, complicated preparation process, difficult filtration, etc., and achieve the effect of large exchange capacity

Active Publication Date: 2007-08-01
岳阳明科催化技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] CN86 1 0692 IA uses natural clinoptilolite or mordenite as the main raw material, adds a certain amount of aluminum hydroxide, potassium chloride, sodium hydroxide and water to mix, and then performs complicated and long-term gelation, crystallization and other steps. Synthesize an adsorbent that can be used to adsorb potassium ions or press ions in water, and its preparation process is relatively complicated
[0011] Chinese patent CN1485281A discloses a method of using 13X molecular sieve to treat ammonia nitrogen sewage. The metered 13X molecular sieve is put into the sewage, stirred, left still, filtered, the filtrate is discharged directly, and the filter residue is regenerated with 20% NaCl solution and baked at 105 degrees. Dried to obtain circulating molecular sieve, but the original powder of 13X molecular sieve is too fine, the separation time is long, and filtration is difficult
[0012] Chinese patent CN1611294A discloses a kind of NaY molecular sieve and aluminum hydroxide powder as the main raw materials, which are formed by extruding and roasting at 300-500°C for 4-10 hours to obtain a rod with a diameter of 0.5-2 mm and a length of 1-5 mm. It adopts fixed bed adsorption to treat 2905~4855mg / L ammonia nitrogen sewage, and the dynamic ammonia nitrogen exchange capacity is about 34~38mg / g. At the same time, it can adsorb Ca, Mg and other ions, but the particle diameter is large and the adsorption capacity is low. Fixed bed process, when dealing with large flow of ammonia nitrogen sewage, the amount of one-time regeneration solution is large

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Use the synthetic 13X molecular sieve with Si / Al atomic ratio of 1.3 as the main raw material, mix with Suzhou machine-selected kaolin, 25% silica sol, and CMC in the following weight ratio 80:10:5:5, and add a certain amount of water to uniformly form a solid content It is 45% colloid, which is pumped into the spray drying tower with a temperature of 650°C for drying, and the tail gas temperature is 180°C. After the material is collected by a cyclone separator, the product that meets the particle size distribution of 20-500 microns is screened out and sent to Enter in the roasting furnace and roast, under the control roasting temperature 450 ℃, roasting time 1 hour, obtain adsorbent A, analyze its water drop method pore volume to be 0.65ml / g.

[0028] The test sewage is taken from a stream of ammonia-containing sewage produced during the production process of oil refining catalysts, with a pH value of 6.8 and NH 3 -N concentration is 4652ppm, Na + The concentration is...

Embodiment 2

[0031]Use the synthetic NaY molecular sieve with Si / Al atomic ratio of 2.6 as the main raw material, and add a certain amount of kaolin, activated aluminum hydroxide, aluminum sol, CMC and hydrochloric acid in the following weight ratio of 70:10:12:5:3 The water is mixed evenly to form a colloid with a solid content of 40%, which is pumped into a spray drying tower with a temperature of 600-650°C for drying, and the temperature of the tail gas is 150°C. The product required for the distribution of 20 to 500 microns is sent into a roasting furnace for roasting, and the roasting temperature is controlled at 500° C. for 1.5 hours to obtain adsorbent B. The pore volume of the water drop method is analyzed to be 0.60 ml / g.

[0032] Test sewage is got the same sewage 1000ml with embodiment 1, adds the adsorbent B of different quantity respectively, stirs 30 minutes, filters, and gets filtrate and analyzes its ammonia nitrogen concentration, and result is as follows:

[0033] ...

Embodiment 3

[0035] The synthetic 13X molecular sieve with Si / Al atomic ratio of 1.3 is used as the main raw material, mixed with halloysite and 25% silica sol in a weight ratio of 95:2:3, and a certain amount of water is added to form a colloid with a solid content of 45%. It is pumped into the spray drying tower with a temperature of 650°C for drying, and the tail gas temperature is 170°C. After the materials are collected by a cyclone separator, the products that meet the particle size distribution requirements of 20-500 microns are screened and sent to the roaster for roasting , control the calcination temperature at 430° C., and the calcination time is 1.2 hours to obtain the adsorbent C, and analyze its pore volume by the water drop method to be 0.7 ml / g.

[0036] The test sewage was taken from a stream of ammonia-containing sewage produced during the production process of oil refining catalysts, and some MgCl was added 2 , its pH value is 7.0, NH 3 -N concentration is 4640ppm, Mg ...

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PUM

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Abstract

The invention discloses a zeolite adsorbent and its preparation method, the zeolite adsorbent is powder particles using zeolite as main raw material; it mixes 60-95% zeolite, 30% filler, 1-30% binding agent, 0-20% hole agent and 0-20% acid to prepare colloid which solid content is 10-60%; After spray-dries it, then it roasts power particles which droplet method volume>0.5 ml / g. The exchange capacity is large, it can remove the ammonia nitrogen, calcium magnesium ion, fluorinion or heavy metallic ion in sewage water effectively and reach sewage water emission standard.

Description

1. Technical field: [0001] The invention relates to an adsorbent and a preparation method thereof, in particular to a zeolite adsorbent capable of adsorbing nitrogen ammonium ions, fluorine ions or heavy metal ions in water bodies and a preparation method thereof. 2. Background technology [0002] Ammonia nitrogen is the main pollutant in rivers and lakes. At high concentrations, it can directly poison fish and shrimp in the water body, and also make the water body eutrophic, thereby breeding bacteria and algae, and domestic sewage. Chemical sewage is the main source of ammonia nitrogen. my country has strict standards for the discharge of ammonia nitrogen in sewage. The national primary discharge standard is 15mg / L, and the secondary standard is 50mg / L. In the advanced treatment of ammonia nitrogen, adsorption is one of the effective methods. The adsorbents in the prior art include: activated carbon, activated coal, clay, diatomaceous earth, bentonite, montmorillonite, cla...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/18C02F1/28
Inventor 于向真袁海亮潘兴红周平
Owner 岳阳明科催化技术有限公司
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