Application of hierarchical pore molecular sieve in preparation process of cyclopentadiene and JP-10 aviation fuel
A cyclopentadiene and molecular sieve technology, applied in molecular sieve catalysts, including molecular sieve catalysts, preparation of heterocyclic compounds, etc., can solve the problems of serious environmental pollution, many by-products, complex separation processes, etc., and achieve low catalyst cost and reduced process. cost effect
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Embodiment 113、114
[0157] Examples 113 and 114 of the present invention use Amberlyst-36 as a catalyst and react at the same temperature (140° C.) for 8 hours, and the yield of cyclopentadiene is 90%. But the resin was recycled a second time and the yield of cyclopentadiene dropped to 13%. This shows that this catalyst cannot be recycled in the dehydration reaction of cyclopentanediol.
Embodiment 168-170
[0162] In Examples 168-170 of the present invention, the hierarchical porous SAPO-34 molecular sieve catalyst was used, and the initial yield of cyclopentadiene was 63%, which was basically equivalent to the reactivity of other hierarchical porous molecular sieves. But the cyclopentadiene yield of its reaction for 40 hours has dropped to 33%; After reacting for 100 hours, the cyclopentadiene yield is only 13%. It can be seen that the hierarchically porous SAPO-34 molecular sieve cannot effectively improve the dehydration stability of cyclopentanediol. Hierarchical pore SAPO-34 molecular sieve is not the catalyst protected in this patent.
Embodiment 253
[0166] The acid treatment preparation of embodiment 253 hierarchical porous molecular sieves
[0167] Add 2g of ZSM-5 or 2g of Y-type molecular sieve into 100mL of 0.05mol / L oxalic acid solution, stir at 90°C for 2 hours, wash three times, filter, dry at 120°C for 6 hours, and roast at 550°C for 2 hours to prepare the acid Treated hierarchical porous ZSM-5 molecular sieve. The nitrogen physical adsorption of hierarchical porous ZSM-5 is shown in Fig. 7(a), which shows a hysteresis loop characteristic curve of mesoporous materials. The pore size distribution of the hierarchically porous ZSM-5 thus calculated is shown in Figure 7(b), and its pore size is in the range of 5-30 nm. The prepared catalyst is recorded as Hierarchical HZSM-5-253 and Hierarchical HY-253.
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