Catalytic cracking method
A catalytic cracking and nano-catalyst technology, applied in the field of catalytic cracking, can solve the problems of low utilization rate, frequent regeneration, and containment, and achieve the effects of improving utilization rate, simple method and reducing cost.
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Embodiment 1
[0041] Taking Yanhua naphtha as raw material, its composition is as follows (w%):
[0042] C4-1.85, C5 6.96, C6 21.29, C7 19.29, C8 23.66, C9 16.04, C10 7.40, C11 2.61, C12 0.64. Among them, 26.18 normal alkanes, 33.66 isoparaffins, 27.35 naphthenes, 0.20 olefins, 12.35 aromatics, and 0.26 unknowns.
[0043] Naphtha with a water-to-oil ratio of 1 enters the preheater 2 at a flow rate of 0.3g / min, and the water liquid containing 700ppm nano-sized alumina is fed into the preheater through the peristaltic pump 4 at a flow rate of 0.3g / min under stirring 2 and the pipeline between reactor 6. The catalytic cracking reaction was carried out at 785°C, and gas samples were taken every 0.5hr to analyze its composition. After about 1 hour of reaction, the cumulative amounts of gaseous and liquid phase products were metered. The reaction results and yields of main products in the gas phase are shown in Table 1.
Embodiment 2
[0048] Except that the catalytic cracking reaction was carried out at 790° C., other reaction conditions were the same as in Example 1. Table 2 shows the reaction results and yields of main products in the gas phase.
Embodiment 3
[0053] Taking Yanhua naphtha as raw material, its composition is as follows (% by weight):
[0054] C4-1.85, C5 6.96, C6 21.29, C7 19.29, C8 23.66, C9 16.04, C10 7.40, C11 2.61, C12 0.64. Among them, 26.18 normal alkanes, 33.66 isoparaffins, 27.35 naphthenes, 0.20 olefins, 12.35 aromatics, and 0.26 unknowns.
[0055] Naphtha with a water-to-oil ratio of 1 enters the preheater 2 at a flow rate of 0.3 g / min, and the aqueous solution containing 700 ppm alkaline earth metal-modified ZSM-5 molecular sieve (particle size <160 mesh) is stirred at a rate of 0.- The flow rate of 1g / min is added into the pipeline between the preheater 2 and the reactor 6 through the peristaltic pump 4 . Catalytic cracking reactions were carried out at 750°C, and gas samples were taken every 0.5hr to analyze its composition. After about 1 hour of reaction, the cumulative amounts of gaseous and liquid phase products were metered. The reaction results and yields of main products in the gas phase are sho...
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