A kind of preparation method of ZSM-5 molecular sieve with high silicon-aluminum ratio
A high-silicon-aluminum ratio, ZSM-5 technology, applied in the direction of crystalline aluminosilicate zeolite, borocarbane silicone crystalline aluminosilicate zeolite, etc., can solve the problems of difficult synthesis, large amount of template agent and environmental pollution, etc. Achieve the effects of stable product performance, continuous gas phase ultra-stable reaction, and low labor intensity
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[0025] The method for preparing the ZSM-5 molecular sieve with high silicon-aluminum ratio provided by the present invention is to continuously introduce NaZSM-5 molecular sieve into the gas-phase superstable reactor, so that the NaZSM-5 molecular sieve can generally be transported from the molecular sieve without carrier gas The inlet continuously moves to the outlet of the molecular sieve, and contacts with silicon tetrachloride gas in the gas phase ultrastable reactor for ultrastable reaction. Simultaneously, silicon tetrachloride was continuously introduced into the reactor.
[0026] In the method for preparing the ZSM-5 molecular sieve with high silicon-aluminum ratio provided by the invention, silicon tetrachloride can be introduced in the reactor with liquid phase and then vaporized in the reactor and reacted with NaZSM-5 molecular sieve, but in order to make the reaction uniform, Preferably silicon tetrachloride is vaporized and introduced into the gas phase ultrastabl...
Embodiment 1
[0062] Made of industrial grade stainless steel with a thickness of 3mm NiCr18Ti figure 2 In the molecular sieve gas-phase silicon replenishment equipment shown, the upper part of the gas-solid separator 2 is cylindrical with a diameter of 6 meters and a height of 14 meters, and the lower part is conical with an opening with a cone angle of 45°, and a valve is provided at the opening , the outlet is located at a position 1 meter away from the top of the gas-solid separator, and the absorption tower 3 is filled with an aqueous sodium hydroxide solution with a concentration of 10 mol / liter. The absorption tower 3 and the gas-solid separator 2 are connected by a conduit, and the conduit goes deep into the Sodium hydroxide aqueous solution.
[0063] Reactor 1 is a tubular reactor, such as Figure 5As shown, the total length of the pipe body is 80 meters, and the diameter of the pipe body is 0.8 meters. The pipe body of the reactor is made into a ring. The reactor includes an upp...
Embodiment 2
[0066] Made of industrial grade stainless steel with a thickness of 3mm NiCr18Ti figure 2 In the molecular sieve gas-phase silicon replenishment equipment shown, the upper part of the gas-solid separator 2 is cylindrical with a diameter of 6 meters and a height of 14 meters, and the lower part is conical with an opening with a cone angle of 45°, and a valve is provided at the opening , the outlet is located at a position 1 meter away from the top of the gas-solid separator, and the absorption tower 3 is filled with an aqueous sodium hydroxide solution with a concentration of 10 mol / liter. The absorption tower 3 and the gas-solid separator 2 are connected by a conduit, and the conduit goes deep into the Sodium hydroxide aqueous solution.
[0067] The length of the tubular reactor 1 is 60 meters, which is a straight tube, the angle between the axis of the tubular reactor and the horizontal plane is 45°, and the diameter (inner diameter) of the tubular reactor is 1 meter, such a...
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