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A method for preparing SSZ-39 molecular sieve using fluorine-modified Y-type molecular sieve as raw material

A technology of SSZ-39 and molecular sieves, applied in molecular sieve catalysts, chemical instruments and methods, and hydrocarbon production from oxygen-containing organic compounds, etc., can solve the problems of inapplicable control indicators, complicated preparation process, and high preparation cost

Active Publication Date: 2021-08-17
CHINA CATALYST HLDG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The most researched and applied molecular sieves are Y-type molecular sieves, mainly hydrogen-type and ammonium-type, and the silicon-aluminum ratio is usually above 10, such as CBV712 and CBV720 of Zeolyst Company. The higher the silicon-aluminum ratio of Y-type molecular sieves, the corresponding preparation process The more complex, the higher the production cost
However, the control indicators such as the silicon-aluminum ratio and crystallinity of the existing commercial Y molecular sieves are mainly designed for the application fields such as catalytic cracking catalysts. For the application of crystal conversion to prepare SSZ-39 molecular sieves, the control indicators may not be applicable. At the same time Its quality will also directly affect the quality of SSZ-39 molecular sieve, resulting in many uncertain factors in the scale-up production of SSZ-39 molecular sieve
[0006] In summary, in many patent documents, there are relatively few studies on the preparation of SSZ-39 molecular sieve by heteroatom-doped modified Y-type molecular sieve through crystallization

Method used

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  • A method for preparing SSZ-39 molecular sieve using fluorine-modified Y-type molecular sieve as raw material
  • A method for preparing SSZ-39 molecular sieve using fluorine-modified Y-type molecular sieve as raw material
  • A method for preparing SSZ-39 molecular sieve using fluorine-modified Y-type molecular sieve as raw material

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Weigh 2247.6g of deionized water, 359.7g of 30wt% sodium hydroxide aqueous solution and 1385.2g of 31.5wt% N,N-dimethyl-3,5-dimethylpiperidinium hydroxide aqueous solution, After stirring and mixing for 0.5 hours at 35°C, add 1004.7g of fluorine-modified Y-type molecular sieve F-USY-3 (SiO 2 / Al 2 o 3 Molar ratio=22.60), continue stirring and mixing at 25~35° C. for 0.5 hour.

[0045] SiO in the final sol 2 :Al 2 o 3 :Na 2 O:ROH:H 2 O molar ratio 22.60:1.00:2.10:4.20:300.00

[0046] The above sol was transferred to a steel autoclave lined with polytetrafluoroethylene, and crystallized at a stirring speed of 50 rpm and a temperature of 135° C. for 7 days.

[0047] After the crystallization reaction is completed, the obtained crystallized product is recovered by filtration, washed with deionized water until the pH is 7-8, and finally dried at 90-120°C. According to powder X-ray powder diffraction (XRD) analysis, the obtained crystallized sample is AEI type zeolit...

Embodiment 2

[0050] Weigh 3579.5g of deionized water, 377.3g of 30wt% sodium hydroxide aqueous solution and 697.8g of 30.2wt% N,N-diethyl-2,6-dimethylpiperidinium hydroxide aqueous solution, After stirring and mixing for 0.5 hours at 35°C, add 346.0g of fluorine-modified Y-type molecular sieve F-USY-4 (SiO 2 / Al 2 o 3 Molar ratio=30.51), continue stirring and mixing at 25~35° C. for 6 hours.

[0051] SiO in the final sol 2 :Al 2 o 3 :Na 2 O:ROH:H 2 O molar ratio 30.51:1.00:8.20:6.50:1400.00

[0052] The above sol was transferred to a steel autoclave lined with polytetrafluoroethylene, and crystallized at a stirring speed of 300 rpm and a temperature of 135° C. for 7 days.

[0053] After the crystallization reaction is completed, the obtained crystallized product is recovered by filtration, washed with deionized water until the pH is 7-8, and finally dried at 90-120°C. According to XRD test, the obtained crystallized sample is AEI type zeolite; figure 1 Scanning electron micrograp...

Embodiment 3

[0056] Weigh 2824.9g of deionized water, 361.3g of 30wt% sodium hydroxide aqueous solution, 287.2g of 31.5wt% N,N-dimethyl-3,5-dimethylpiperidinium hydroxide aqueous solution, 30.2wt% 352.4g of N,N-diethyl-2,6-dimethylpiperidinium hydroxide aqueous solution and 1111.2g of 29.5wt% silica sol were stirred and mixed at 25-35°C for 6 hours, and then 63.0g of Fluorine-modified Y-type molecular sieve F-HY(SiO 2 / Al 2 o 3 Molar ratio=5.19), continue stirring and mixing at 25~35° C. for 6 hours.

[0057] SiO in the final sol 2 :Al 2 o 3 :Na 2 O:ROH:H 2 O molar ratio 46.00:1.00:10.20:8.50:1800.00, where N,N-dimethyl-3,5-dimethylpiperidinium hydroxide and N,N-diethyl-2,6-di The molar ratio of methylpiperidinium hydroxide is 1:1.

[0058] The above sol was transferred to a steel autoclave lined with polytetrafluoroethylene, and crystallized at a stirring speed of 300 rpm and a temperature of 145° C. for 4 days.

[0059]After the crystallization reaction is completed, the obtain...

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Abstract

The invention discloses a method for preparing SSZ‑39 molecular sieves by using fluorine-modified Y-type molecular sieves as raw materials. Y-type molecular sieve is impregnated with fluorine-containing aqueous solution, dried, and roasted to obtain fluorine-doped Y-type molecular sieve; mix and stir deionized water, alkali source, template agent, and silicon source according to the ratio, and add the above-mentioned fluorine-doped Y-type molecular sieve. Sol: transfer the sol to a crystallization kettle, after the crystallization is complete, the crystallized product is filtered, washed, dried, ion-exchanged, and then roasted to prepare a hydrogen-type SSZ‑39 molecular sieve. The present invention modifies the raw material of Y-type molecular sieve by fluorine doping method, so that it can completely transform crystal to prepare SSZ-39 molecular sieve in a relatively short period of time under the condition of relatively low silicon-aluminum ratio, so that the raw material and Cost of production. The SSZ-39 molecular sieve prepared by the invention has the characteristics of short crystallization time, high crystallinity, controllable grain size, good grain dispersion, etc., and can be applied to the fields of methanol-to-olefin reaction, carrier of selective catalytic reduction catalyst, and the like.

Description

technical field [0001] The invention relates to a method for preparing SSZ-39 molecular sieve by using fluorine-modified Y-type molecular sieve as a raw material, in particular to using fluorine-modified Y-type molecular sieve as all aluminum source and part or all silicon source, and preparing silicon A method for preparing SSZ-39 molecular sieves after crystallization reaction of aluminum sol. The invention also relates to the application of the SSZ-39 molecular sieve as a methanol-to-olefin (MTO) catalyst and a selective catalytic reduction (SCR) catalyst carrier. Background technique [0002] Zones et al. synthesized SSZ-39 aluminosilicate molecular sieve for the first time in 1999. The molar ratio of silicon dioxide and aluminum oxide (silicon-aluminum ratio) is between 10 and 100. The skeleton topology of the molecular sieve is AEI. The basic structural units of double six-membered rings (D6R) are linked by some four-membered rings to form a three-dimensional channel ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/24B01J29/70C07C1/20C07C11/02
CPCB01J29/70C01B39/24C01P2002/72C01P2004/03C07C1/20C07C11/02
Inventor 王于于浩淼栾忠凌董兆亮王贤彬王炳春李进
Owner CHINA CATALYST HLDG CO LTD
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