Hierarchical porous structure SAPO molecular sieve material and preparation method thereof
A technology of multi-stage pores and molecular sieves, which is applied in the direction of molecular sieve catalysts, molecular sieves and alkali-exchanged phosphates, molecular sieve characteristic silicoaluminophosphates, etc., can solve the problems of poor diffusion performance of SAPO molecular sieves, and achieve easy control, high crystallinity, and preparation The effect of simple process
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Embodiment 1
[0026] Mix 2.4 grams of PEG (polyethylene glycol) and 45 grams of deionized water evenly, then add 12.3 grams of aluminum isopropoxide and 11.97 grams of orthophosphoric acid (85% by weight) to it in turn, and form solution a after fully stirring; 60 grams of four Ethyl ammonium hydroxide (25% by weight) and 6 grams of silica sol (40% by weight) were mixed uniformly to form solution b; a and b were mixed and stirred at room temperature for 6 hours to obtain the crystallization liquid of synthetic SAPO-34 molecular sieve; The prepared crystallization solution was stirred and aged at room temperature for 24 h, and the aged crystallization solution was put into a crystallization kettle lined with polytetrafluoroethylene, and crystallized at 200 °C for 24 hours;
[0027] The weight ratio of each component is: R1 / Al2O3=0.4; R2 / Al2O3=10; H2O / Al2O3=7; SiO2 / Al2O3=0.4; P2O5 / Al2O3=1.1, wherein R1, R2 represent PEG (polyethylene glycol ) and TEAOH (tetraethylammonium hydroxide).
[0028...
Embodiment 2~14
[0031] According to the various steps and conditions of [Example 1], a molecular sieve with a multi-level pore structure was produced, only the parameters such as the ratio of raw materials (Table 1), the type of alkali, and the alkali treatment temperature were changed, which are specifically listed in Table 1. The characterization of the synthesized product shows that it has a crystal structure similar to that of [Example 1] and the product, and its specific physical and chemical parameters are shown in Table 2.
[0032]
[0033] Table 1
[0034]
[0035] Table 2
[0036]
Embodiment 15
[0038] A fixed-bed catalytic reaction device is adopted, and the reactor is a stainless steel tube. The catalyst prepared in Example 1 and the cubic catalyst prepared by the traditional method are evaluated for the reaction activity of methanol conversion to light olefins. The process conditions used for the investigation are: catalyst loading 0.5 g, the reaction temperature is 450°C, the reaction pressure is 0.1MPa, the water / raw material weight ratio is 0.25, and the gravimetric space velocity is 1 h -1 . Online analysis of all products. The evaluation results are shown in Table 3.
[0039]
[0040] table 3
[0041]
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