Method for use of modified molecular sieve catalyst in catalytic cracking of propane
A catalytic cracking and catalyst technology, applied in the direction of molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as inability to obtain catalysts
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Embodiment 1
[0114] The preparation method of 0.1%Au / HZSM-5:
[0115] (1) Synthesize ZSM-5 molecular sieve raw powder with reference to the method disclosed in the published patent CN100364890C. Calcined at 540 DEG C for 4 hours to obtain ZSM-5 molecular sieves.
[0116] (2). Ammonium exchange treatment: the calcined molecular sieve is subjected to ion exchange treatment with an ammonium salt solution at a suitable temperature. Then, it is washed with deionized water to neutrality, then dried and calcined to obtain a hydrogen-type catalyst. Said ammonium salt is ammonium nitrate, and ammonium salt solution concentration is 0.6mol / L, and the liquid-solid volume ratio of catalyzer and ammonium salt solution is 5:1, and exchange temperature is 30 ℃, and exchange time is 1 hour, and exchange number of times is 2 Second-rate. 110 DEG C of drying temperature, 12 hours of drying time, 540 DEG C of roasting temperature, 6 hours of roasting time. Na after exchange + The content is not higher t...
Embodiment 2
[0122] Repeat Example 1, but change the amount of chloroauric acid solution into 3.14ml and add water to 10ml, and the roasting temperature is 300°C. A supported gold catalyst 0.3%Au / HZSM-5 was obtained. Labeled: A-2.
Embodiment 3
[0124] Repeat embodiment 1, but change the degree of vacuum into-0.05MPa, and the consumption of chloroauric acid solution is changed into 10.46ml. The supported gold catalyst 1.0%Au / HZSM-5 was obtained. Labeled: A-3.
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