Application of nanosheet sapo molecular sieve aggregates in methanol to olefins reaction
A nanosheet and molecular technology, which is applied in the direction of molecular sieve catalyst, molecular sieve characteristic silicoaluminophosphate, molecular sieve and alkali exchange phosphate, etc., can solve the problems such as poor performance of SAPO molecular sieve
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Embodiment 1
[0028] First, 12.3 grams of aluminum isopropoxide was stirred in ammonia solution at 40° C. for 24 hours to obtain solution A; then 5.5 grams of phosphoric acid (85% by weight), 45 grams of deionized water, 60 grams of tetraethylammonium hydroxide (25% by weight) ), 6 grams of silica sol (40% by weight) were successively added into the mixed solution A, and placed in a reaction kettle after being stirred uniformly at 60°C, and crystallized for 1 day at 180°C; the sample was washed after the reaction , drying and roasting to obtain nanosheet SAPO molecular sieve aggregates (99nm long, 78nm wide, and 15nm high).
[0029] The weight ratio of each component is: TEAOH / Al 2 o 3 =10;H 2 O / Al 2 o 3 = 7; SiO 2 / Al 2 o 3=0.4;P 2 o 5 / Al 2 o 3 = 1.1.
[0030] The obtained product was washed, centrifuged, and dried at 110°C to obtain a solid sample. XRD results showed that the obtained product was SAPO-34 molecular sieve powder. see SEM figure 1 , see XRD figure 2 .
Embodiment 2~14
[0032] According to the various steps and conditions of [Example 1], the nanosheet SAPO molecular sieve aggregates were prepared, only the parameters such as the ratio of raw materials (Table 1) and the type of alkali were changed, which are specifically listed in Table 1. 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 1.
[0033] Table 1
[0034]
[0035]
Embodiment 15
[0037] A fixed-bed catalytic reaction device is adopted, and the reactor is a stainless steel tube. The catalyst prepared in Example 1 is evaluated for the reaction activity of methanol conversion to light olefins. The process conditions used for the investigation are: catalyst loading 0.5g, reaction temperature 450 ° C, The reaction pressure is 0.1MPa, the water / raw material weight ratio is 0.25, and the weight space velocity is 1h -1 . Online analysis of all products. The evaluation results are shown in Table 2.
[0038] Table 2
[0039]
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