Symbiotic composite molecular sieve catalyst applied to MTO reaction, and preparation method thereof

A composite molecular sieve and molecular sieve technology, applied in the direction of molecular sieve catalysts, catalyst activation/preparation, chemical instruments and methods, etc., can solve problems such as catalyst deactivation, achieve high catalytic activity, good stability, and improve selectivity.

Pending Publication Date: 2020-05-12
中催技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the MTO catalytic reaction, the outer surface of the SAPO-34 molecular sieve and the cages and pores tend to form larger carbon deposits, which can easily lead to the deactivation of the catalyst.

Method used

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  • Symbiotic composite molecular sieve catalyst applied to MTO reaction, and preparation method thereof
  • Symbiotic composite molecular sieve catalyst applied to MTO reaction, and preparation method thereof
  • Symbiotic composite molecular sieve catalyst applied to MTO reaction, and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] (1) Take 1000g SAPO-34 (composition ratio 0.25SiO 2 ·Al 2 o 3 0.89P 2 o 5 1.07H 2 O) Molecular sieve, 110.87g HY(nSiO 2 / nAl 2 o 3 =5.2, dry basis 78wt%) molecular sieve, 108.40g water glass (Na 2 O: 7.48wt%, SiO 2 : 24.61wt%), 572.52g silica gel solution (Na 2 O: 0.23wt%, SiO 2 : 29.49wt%) and deionized water to prepare a slurry with a solid content of 35%, spray drying (inlet temperature 140°C, outlet temperature 80°C) to form microspheres with an average particle size of 60-80μm, and roast at 700°C 4 hours to obtain pretreated microspheres.

[0029](2) Mix the pretreated microspheres with 16.24g of NaOH, 357.60g of diethyldimethylammonium hydroxide (referred to as OSDA, concentration 20wt%) and 2813.54g of deionized water. After subtracting the weight of SAPO-34, the proportion in the remaining mixture sol is nNa 2 O:nSiO 2 :nAl 2 o 3 :nOSDA:nH 2 The molar ratio of O=0.09:1:0.05:0.15:50. Put the above mixed sol into a crystallization synthesis kettl...

Embodiment 2

[0032] The processing method of synthesizing SAPO-34 / RUB-50 symbiotic composite molecular sieve is similar to embodiment 1, and difference is: the slurry concentration that carries out spray drying is 25%, and using template agent is diethyldimethylammonium chloride solution ( Template agent solution concentration 20.0wt%), the obtained SAPO-34 / RUB-50 symbiotic composite molecular sieve microspheres and 1.0mol / L nickel nitrate aqueous solution were ion-exchanged according to the mass ratio of 1:10. figure 2 The XRD diffraction pattern shown in proves that the material is SAPO-34 / RUB-50 intergrowth composite molecular sieve, which is denoted as SARU-2.

Embodiment 3

[0034] The processing method of synthesizing SAPO-34 / RUB-50 symbiotic composite molecular sieve is similar to embodiment 1, and difference is: the slurry concentration that carries out spray drying is 45%, and using template agent is N-methylquinuclidinium (template agent Concentration 20.0wt%), crystallization synthesis conditions are stirring at 80rpm speed, crystallization at 180°C for 96 hours. The obtained SAPO-34 / RUB-50 symbiotic composite molecular sieve microspheres were ion-exchanged with a 1.0 mol / L aqueous solution of lanthanum nitrate at a mass ratio of 1:10. The addition amount of various raw materials synthesized by crystallization is shown in Table 1, image 3 The XRD diffraction pattern shown in proves that the material is a SAPO-34 / RUB-50 intergrowth composite molecular sieve, which is denoted as SARU-3.

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Abstract

The invention discloses a symbiotic composite molecular sieve catalyst applied to a MTO reaction, and a preparation method thereof. The catalyst is mainly formed by symbiotic compounding of SAPO-34 and RUB-50 molecular sieve structures, wherein the SAPO-34 molecular sieve accounts for 60-99% of the total weight of the catalyst, the RUB-50 molecular sieve accounts for 1.0-40% of the total weight ofthe catalyst, the silicon-to-aluminum molar ratio of the oxide in the symbiotic composite molecular sieve is 20-200, and the X-ray diffraction spectrogram of the symbiotic composite molecular sieve shows that the symbiotic composite molecular sieve has a characteristic diffraction peak with relative intensity at a specific 2theta angle. According to the invention, the RUB-50 with the LEV structure and the SAPO-34 with the CHA structure form a symbiotic composite molecular sieve, and the symbiotic composite molecular sieve has two molecular sieve structure characteristics to generate the specificity of the structure, so that the composite molecular sieve has reasonably distributed acidity and good hydrothermal stability, overcomes the limitations of the components, has good catalytic activity, high ethylene and/or propylene selectivity and excellent service life in MTO reaction, well meets the requirements of industrial application, and has broad application prospects.

Description

technical field [0001] The invention relates to a symbiotic composite molecular sieve catalyst applied to MTO reaction and a preparation method thereof, in particular to a SAPO-34 / RUB-50 symbiotic composite molecular sieve catalyst, and belongs to the field of chemical synthesis technology and its application. Background technique [0002] RUB-50 molecular sieve belongs to the LEV topological configuration type molecular sieve, which has two-dimensional intersecting eight-membered ring channels along the [001] and [010] directions, and relatively small channel size. With a lower skeleton density, its theoretical micropore volume can reach 0.3ml / g. Similar to SAPO-34 molecular sieve, RUB-50 molecular sieve also has a larger molecular sieve cage, indicating that this type of small-pore RUB-50 molecular sieve catalyst with large micropore volume has excellent selection in the conversion of methanol and ethanol to light olefins sex. The RUB-50 molecular sieve cage (0.63nm×0.7...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/85B01J37/08C07C1/20C07C11/04C07C11/06C07C11/08
CPCB01J29/005B01J37/08C07C1/20B01J29/85B01J29/08B01J2229/20C07C11/04C07C11/06C07C11/08Y02P20/52Y02P30/20Y02P30/40
Inventor 冯志武袁秋华李伟斌程计红赵广
Owner 中催技术有限公司
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