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Preparation method of SSZ-13 molecular sieve for MTO catalytic reaction

A catalytic reaction and molecular sieve technology, applied in the field of preparation of SSZ-13 molecular sieve, can solve the problems of easy clogging of copper and difficulty in preparing copper content, and achieve the effects of improving relative crystallinity, reducing preparation cost and reducing synthesis cost.

Active Publication Date: 2020-06-19
SHANGHAI LVQIANG NEW MATERIALS CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] The purpose of the present invention is exactly to provide a kind of preparation method of the SSZ-13 molecular sieve that is used for MTO catalytic reaction in order to overcome the defective that above-mentioned prior art exists, solves the difficult allotment of copper content in the Cu-SSZ-13 molecular sieve in the prior art, It is used for the technical problem that copper is easy to block in the MTO reaction. It has the advantages of controllable copper content, adjustable silicon-aluminum molar ratio, and high catalytic activity.

Method used

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  • Preparation method of SSZ-13 molecular sieve for MTO catalytic reaction
  • Preparation method of SSZ-13 molecular sieve for MTO catalytic reaction
  • Preparation method of SSZ-13 molecular sieve for MTO catalytic reaction

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preparation example Construction

[0037] A kind of preparation method for the SSZ-13 molecular sieve of MTO catalytic reaction, comprises the following steps:

[0038] (1) Preparation of Cu-SSZ-13 molecular sieve: the aluminum source, silicon source, sodium source, water and copper amine complex according to 1.0Al 2 o 3 :10~35SiO2 2 :3.0~5.0Na 2 O:200~300H 2 O: 2.0~4.0Cu-TEPA molar ratio mixed at room temperature, stirred with a stirring paddle for 30min, put into a polytetrafluoroethylene-lined steel reaction kettle, reacted at 130℃~175℃ for 96h~144h, reacted After completion, the product was washed with deionized water and dried at 100°C for 12 hours to obtain Cu-SSZ-13 molecular sieve (S1). The silicon source used in this step was water glass, silica sol, silica gel, amorphous SiO 2 Powder, Si(OCH 3 ) 4 and Si(OC 2 h 5 ) 4 One or several mixtures of them, the aluminum source is sodium metaaluminate, pseudoboehmite, amorphous aluminum hydroxide powder and aluminum isopropoxide, and the sodium source...

Embodiment 1

[0048] Preparation of SSZ-13 molecular sieve with copper amine complex as template

[0049] The preparation of Cu-SSZ-13 molecular sieve: Sodium metaaluminate, water glass, sodium hydroxide, deionized water and copper ammonium complex are according to n(Al 2 o 3 ):n(SiO 2 ):n(Na 2 O):n(H 2 The molar ratio of O):n(Cu-TEPA) is 1:10:3.0:200:2.0, mixed at room temperature, and stirred with a stirring paddle for 30min. Put it into a polytetrafluoroethylene-lined steel reactor and react at 130°C for 96h. After the reaction was completed, the product was washed with deionized water and dried at 100° C. for 12 hours to obtain Cu-SSZ-13 molecular sieve (S1).

[0050] Removal of Cu: Add 2 g of the synthesized S1 sample into 50 mL of ammonium nitrate solution with a concentration of 1 mol / L, ion exchange for 4 h in a water bath at 80 °C, wash, and dry at a constant temperature of 100 °C for 2 h, repeating 3 times. A molecular sieve sample (S2) is obtained.

[0051] Secondary cryst...

Embodiment 2

[0053] Preparation of SSZ-13 molecular sieve with copper amine complex as template

[0054] Preparation of Cu-SSZ-13 molecular sieve: Pseudoboehmite (CP), Si(OCH 3 ) 4 (AR), sodium oxide (AR), deionized water and copper ammonium complex according to n(Al 2 o 3 ):n(SiO 2 ):n(Na 2 O):n(H 2 The molar ratio of O):n(Cu-TEPA) is 1:20:3.5:220:2.5. Mix at room temperature and stir with a stirring paddle for 30min. Put it into a polytetrafluoroethylene-lined steel reactor and react at 140°C for 108h. After the reaction was completed, the product was washed with deionized water and dried at 100° C. for 12 hours to obtain Cu-SSZ-13 molecular sieve (S1).

[0055]Removal of Cu: Add 2 g of the synthesized S1 sample into 50 mL of ammonium chloride solution with a concentration of 1.2 mol / L, ion exchange for 6 h in a water bath at 80 °C, wash, and dry at a constant temperature of 100 °C for 2 h, repeating 3 times. A molecular sieve sample (S2) is obtained.

[0056] Secondary crystall...

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Abstract

The invention relates to a preparation method of an SSZ-13 molecular sieve for a MTO catalytic reaction. The method comprises the following steps: preparing a Cu-SSZ-13 molecular sieve by using a cheap copper amine coordination compound as a template agent, and removing Cu in the Cu-SSZ-13 molecular sieve so as to catalyze a MTO reaction. According to the method, the SSZ-13 molecular sieve capableof being used for catalyzing a MTO reaction is obtained by removing copper in a Cu-SSZ-13 molecular sieve; compared with the existing MTO catalyst, the SSZ-13 molecular sieve capable of being used for catalyzing a MTO reaction is obtained by removing copper in the Cu-SSZ-13 molecular sieve avoids the use of a large amount of expensive N,N,N-trimethyl-1-adamantane ammonium hydroxide (TMAdaOH) template agent, can reduce the cost, and further reduces the energy consumption and reduces the operation cost by reducing the MTO reaction temperature.

Description

technical field [0001] The invention relates to the field of catalysts, in particular to a method for preparing SSZ-13 molecular sieves used in MTO catalytic reactions. Background technique [0002] With the rapid development of my country's chemical industry, ethylene and propylene, as the basic raw materials of the chemical industry, occupy an important position in the chemical industry and are the leading products in the petrochemical industry. Methanol-to-olefins (MTO) technology is a new route to produce olefins from non-petroleum resources. The MTO process can provide new development space for the chemical utilization of coal or natural gas, especially for remote areas rich in natural gas or coal resources, creating opportunities for large-scale development of methanol, low-carbon olefins and their downstream industries using natural gas or coal. Therefore, the research and development of MTO catalysts is of great significance to reduce my country's dependence on oil ...

Claims

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Application Information

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IPC IPC(8): B01J29/76B01J37/00B01J37/30C07C1/20C07C11/04C07C11/06
CPCB01J29/763B01J37/30B01J37/0009C07C1/20B01J2229/18C07C2529/76C07C11/04C07C11/06Y02P20/52Y02P30/20Y02P30/40
Inventor 张春秀余金鹏张伏军徐华胜胡杰朱琳张丽王鹏飞
Owner SHANGHAI LVQIANG NEW MATERIALS CO LTD