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Preparation method of porous coated iron-based molecular sieve catalyst

A molecular sieve and coating technology, which is applied in the field of preparation of porous coated iron-based molecular sieve catalysts, achieves the effects of good anti-sulfur effect, good high-temperature NOx conversion rate, and strong practical application value

Active Publication Date: 2019-12-31
CHINA FIRST AUTOMOBILE
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, with the increasingly stringent environmental protection regulations, the requirements for the NOx limit are getting higher and higher. The NOx limit of the Euro VI stage is 0.4g / Kwh, which is 80% lower than that of the Euro V. In fact, in the sulfur-free and dust-free , Under anhydrous conditions, many catalysts exhibit excellent NOx activity, but in road verification, most molecular sieve catalysts do not meet the requirements of high temperature NOx conversion rate, good sulfur resistance and high temperature thermal shock

Method used

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  • Preparation method of porous coated iron-based molecular sieve catalyst
  • Preparation method of porous coated iron-based molecular sieve catalyst
  • Preparation method of porous coated iron-based molecular sieve catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] (1) Dissolve 1200g of ferric nitrate in deionized water, stir to dissolve, add 3000g Beta40 molecular sieve carrier, mix and stir for 2h; (2) Add 140g of ammonium carbamate and stir for 3h at 45℃ to obtain a mixed solution; (3) Mixed solution After drying at 90°C, calcining at 530°C for 4h, and grinding to obtain Fe modified molecular sieve powder; (4) Dissolve 2400g of lanthanum acetate in 3600g of deionized water to prepare a solution, then add 165g of ammonium formate and 2400g of 1% mass fraction CMC and 195g ethanol, stirred vigorously at 45°C for 5h; (5) Add 3000g of the Fe-modified molecular sieve powder obtained in (3) and stir vigorously at 65°C for 3h to obtain a paste; (6) Put the paste in Drying in an oven at 85°C, crushing, calcining at 480°C for 6 hours, and grinding to obtain a porous coated iron-based molecular sieve catalyst.

[0017] figure 1 For the TEM image of the catalyst prepared in Example 1, it can be seen that the outer layer of pores is relativel...

Embodiment 2

[0024] (1) Dissolve 3000g of ferric nitrate in deionized water, stir to dissolve, add 3000g of Sapo34 molecular sieve carrier, mix and stir for 4h; (2) Add 213g of ammonium carbamate and stir for 2h at 60℃ to obtain a mixed solution; (3) Mixed solution After drying at 110°C, calcining at 580°C for 4 hours, and grinding to obtain Fe modified molecular sieve powder; (4) Dissolve 3,600g of cerium acetate in 4800g of deionized water to prepare a solution, then add 375g of formamide, 3000g with a mass fraction of 1% CMC and 510g propanol, stirred vigorously at 105°C for 6h; (5) Add 3000g of the Fe-modified molecular sieve powder obtained in (3), and stir vigorously at 105°C for 5h to obtain a paste; (6) Combine the paste Drying in an oven at 105°C, crushing, calcining at 550°C for 4 hours, and grinding to obtain a porous coated iron-based molecular sieve catalyst.

Embodiment 3

[0026] (1) Dissolve 2500g of ferric nitrate in deionized water, stir to dissolve, add 3000g of ZSM5 molecular sieve carrier, and mix and stir for 4h; (2) Add 185g of ammonium carbamate and stir for 1h at 60℃ to obtain a mixed solution; (3) Mixed solution After drying at 105°C, calcining at 550°C, and grinding, the Fe modified molecular sieve powder is obtained; (4) Dissolve 2500g of manganese acetate in 4500g of deionized water to prepare a solution, then add 305g of ammonium oxalate, 2500g of 1.0% CMC mass fraction And 462g of absolute ethanol, stirred vigorously at 85°C for 2h; (5) Add 3000g of the Fe-modified molecular sieve powder obtained in (3), and stir vigorously at 105°C for 3h to obtain a paste; (6) add the paste Drying in an oven at 120°C, crushing, calcining at 530°C for 4 hours, and grinding to obtain a porous coated iron-based molecular sieve catalyst.

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Abstract

The invention relates to a preparing method of a porous clad iron-based molecular sieve catalyst. The method is characterized in that the NOx conversion ratio of the prepared catalyst is as high as 65% or above at 200-550 DEG C, and can still be 70% or above at 550 DEG C so a high-temperature NOx conversion ratio is good; the catalyst can meet using requirements on high-temperature thermal shock resistance and has high practical application value; and an inside-outside clad structure has good anti-sulfur effects. In addition, the preparing process of the catalyst is simplified, synthetic conditions are easy to control and the method is prone to industrial application.

Description

Technical field [0001] The invention relates to a preparation method of a porous coated iron-based molecular sieve catalyst, which belongs to the technical field of automobile emission, in particular to the field of preparation of SCR denitration catalysts. Background technique [0002] In order to meet emission regulations, Urea-SCR technology has become the first choice for medium- and heavy-duty diesel engine companies to reduce NOx, and is increasingly accepted by people and has become the mainstream research direction for diesel engine exhaust NOx aftertreatment. The core of Urea-SCR technology is the catalyst. Currently, Urea-SCR catalysts include metal oxide catalysts, precious metal catalysts and zeolite molecular sieve catalysts. Among them, the cost of precious metal catalysts is too high and it is easy to form sulfates with the sulfides in the exhaust gas, resulting in catalyst deactivation. Vanadium-based catalysts are currently widely used in China and have the adva...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/46B01J29/72B01J29/85B01J33/00B01D53/86B01D53/56
CPCB01D53/8628B01D2255/20738B01D2255/50B01D2255/502B01D2255/504B01D2255/65B01J29/46B01J29/7215B01J29/723B01J29/85B01J33/00B01J37/0018B01J2229/18
Inventor 于力娜张克金崔龙米新艳曹婷婷杨帅
Owner CHINA FIRST AUTOMOBILE