Molecular sieve catalyst, preparing method and use thereof
A molecular sieve and catalyst technology, applied in the field of modified molecular sieve catalyst, can solve the problems of reducing the economic benefit of aromatization, and achieve the effect of high reaction stability
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Embodiment 1
[0030] Preparation of common catalysts:
[0031] 1) Na-type ZSM-5 molecular sieve (silicon-aluminum ratio is 55) and 30%wt SB powder (that is, styrene-butadiene, imported from Germany) after roasting are extruded, dried, roasted, and then The H-type molecular sieve catalyst used is obtained by ammonia exchange and roasting, and the catalyst is crushed into 20-40 mesh particles before loading into the reactor, which is recorded as P.
[0032] 2) Place 5 g of the catalyst obtained in Step 1 in a continuous-flow fixed-bed reactor with an inner diameter of 10 mm. -1 The catalyst was contacted under the condition of weight space velocity, and the reaction results are shown in Table 1.
[0033] Prepare catalyst of the present invention:
[0034] Put 20 g of the calcined Na-type ZSM-5 molecular sieve (the ratio of silicon to aluminum is 55) into 1000 ml of 0.2 M NaOH solution, stir at 80 °C for 6 hours, cool to room temperature, then filter, wash until neutral, and dry Finally, it...
example 2
[0040] The above catalysts P and AT were respectively subjected to steam treatment, the steam treatment temperature was 530° C., and the treatment time was 3 hours. The obtained catalysts were respectively marked as P-530 and AT-530. Except that the reaction temperature was increased to 365° C., other reaction conditions were the same as in Example 1, and the reaction results are shown in Table 2.
[0041] Cumulative response
[0042] It can be seen from Table 2 that after high-temperature hydrothermal treatment of catalysts P and AT, the modified catalyst AT-530 of the present invention shows better aromatization stability than P-530, and the amount of carbon deposited on the catalyst is still almost equal .
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