System for purifying trichlorosilane by utilizing quadruple-effect coupled distillation and treatment method thereof
A technology for purifying trichlorosilane and rectification, which is applied to chemical instruments and methods, silicon compounds, halosilanes, etc. It can solve the problem that the purity of silicon trichloride does not reach the electronic level and cannot effectively solve the problem of raw material preheating and other issues to achieve the effects of saving consumption, reducing device costs and optimizing process conditions
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Example Embodiment
[0050] Example 1:
[0051] This embodiment provides a system for purifying trichlorosilane using four-effect coupling rectification, which is characterized in that the first light removal tower 1, the first light removal tower 2, the second light removal tower 3, and the second Weight removal tower 4, feed preheater 5, first light removal tower reboiler 6, first light removal tower reboiler 7, second light removal tower reboiler 8, second light removal tower reboiler 9 and the heat pump compressor 10; wherein the top steam outlet of the first light removal tower 1 is connected to the light miscellaneous storage tank through the heat pump compressor 10 and the second light removal tower reboiler 9 in turn. The outlet of the bottom material is connected with the inlet of the first de-weighting tower 2; the top steam outlet of the first de-weighting tower 2 is connected with the inlet of the second de-lighting tower 3 through the first de-lighting tower reboiler 6 ; The top steam o...
Example Embodiment
[0053] Example 2:
[0054] This embodiment provides a processing method of the system described in Embodiment 1. The method is as follows:
[0055] The raw materials to be treated are subjected to the first light removal treatment through the first light removal tower 1, and the light components at the top of the tower are sequentially heated by the heat pump compressor 10, and are heated in the second light removal tower by the reboiler 9 and the second light removal tower. The material at the bottom of the tower 4 is recovered as light impurities after heat exchange, a part of the obtained heavy components is returned as reboiled gas, and a part enters the first heavy removal tower 2 for the first heavy removal treatment;
[0056] Wherein, the top temperature of the first light removal tower 1 is 43-45°C, the bottom temperature is 57-60°C, the top pressure is 250-270kPa, and the pressure drop of the entire first light removal tower 1 is less than 30kPa , The reflux feed ratio is 3...
Example Embodiment
[0064] Example 3:
[0065] This embodiment provides a treatment method for the system described in Example 1, except that the top temperature of the first light removal tower 1 is 40-43°C, the bottom temperature is 55-57°C, and the top pressure 200~230kPa, the pressure drop of the first light removal tower 1 is less than 20kPa, and its reflux feed ratio is 1.0~2.0; the top temperature of the first light removal tower 2 is 60~63℃, and the bottom temperature The temperature at the top of the tower is 70~73℃, the pressure at the top of the tower is 300~330kPa, the pressure drop of the whole tower is less than 20kPa, and the reflux feed ratio is 1.0~2.0; the top temperature of the second light removal tower 3 is 75~77℃, and the bottom The temperature is 85~87℃, the pressure at the top of the tower is 400~430kPa, the pressure drop of the whole tower is less than 50kPa, and the reflux feed ratio is 5.0~6.0; the top temperature of the second deweighting tower 4 is 90~93℃, and the bottom...
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