Method for preparing molecular sieve
A technology of molecular sieve and feed port, which is applied in the field of molecular sieve preparation, can solve the problems that the gas-phase ultra-stable process is difficult to industrialize, increase production costs and environmental protection costs, and endanger the health of operators, and achieve continuous gas-phase ultra-stable reactions. Reduced work intensity and low labor intensity
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preparation example Construction
[0019] According to the method for preparing molecular sieve provided by the present invention, although as long as described molecular sieve and gas phase SiCl 4 Contacting molecular sieves with SiCl in a continuous flow 4 The purpose of the present invention can be achieved by suspending contact, but preferably, in order to ensure that the molecular sieve is suspended in the SiCl-containing 4 The absence of gas flow in the tubular reactor further reduces the SiCl 4 The consumption of gas, the present invention preferably described molecular sieve and gas phase SiCl 4 The contacting is carried out in the presence of an inert carrier gas flow. The inert gas flow can be a variety of non-interfering molecular sieves and gas phase SiCl 4 The gas flow for the reaction may be, for example, one or more of air flow, nitrogen flow, and gas flow of Group 0 elements in the periodic table. Due to SiCl 4 Sensitive to water, therefore, preferably, the above-mentioned inert carrier gas...
Embodiment approach
[0033] According to a preferred embodiment of the present invention, the pipe body 13 further includes a second inclined section 133, one end of the second inclined section 133 is connected to the other end of the vertical section 132, and the first The feed port is located at the other end of the second inclined section 133 . This can prevent the molecular sieve solid material from flowing too fast under the action of gravity, and increase the contact reaction time between the reaction materials.
[0034] Further preferably, the position of the first feed inlet is higher than the position where the second inclined section 133 is connected to the vertical section 132, so that the molecular sieve solid material can directly enter the second inclined section 133 by its own gravity. In section 133, it can then be transported further under the entrainment of the carrier gas.
[0035] The included angle between the second inclined section 133 and the vertical section 132 can be 10...
Embodiment 1
[0053] Made of industrial grade stainless steel with a thickness of 3mm NiCr18Ti figure 2 In the shown molecular sieve vapor phase silicon replenishment equipment, the tube body 13 of the tubular reactor 1 is composed of a first inclined section 131, a vertical section 132 and a second inclined section 133, the length of the first inclined section 131 is 20 meters, and the diameter is 0.8 meters, the length of the vertical section 132 is 40 meters, and the diameter is 0.8 meters. The length of the second inclined section 133 is 15 meters, and the diameter is 0.8 meters. The vertical section 132 is perpendicular to the horizontal plane, and the axis of the first inclined section 131 and The angle α between the horizontal planes is 75° (that is, the angle between the first inclined section 131 and the vertical section 132 is 15°), and the angle β between the axis of the second inclined section 133 and the horizontal plane is 65° (that is, the angle between the second inclined s...
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