Method for refining and purifying electronic-grade silane in polysilicon production process
A technology of production process and purification method, which is applied in the direction of silicon hydride, etc., can solve the problems that the purity is difficult to reach a high standard, silicon tetrachloride cannot be recycled, and energy consumption is high.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0026] Put the crude silane into the light removal tower through the silane compressor, and remove nitrogen, methane, and hydrogen under the conditions that the temperature at the top of the light removal tower is -120 ° C, the pressure is 1.85 MPa, and the operating pressure difference is 0.5 kPa; The liquid silane is passed into the first weight-removing tower, and ethane, ethylsilane, diethylsilane, boron, Phosphorus; the silane gas discharged from the top of the tower passes through a three-stage adsorption tower, which is equipped with 4A molecular sieves, and the operating pressure of the adsorption tower is 1.6MP to remove ethylene; the purified silane gas comes out of the adsorption tower and enters the second weight removal tower , under the condition that the temperature at the top of the tower is -70°C, the pressure is 1.6MPa, and the operating pressure difference is 1kPa, ethyl silane is removed, and the pure silane gas leaves the top of the second weight removal to...
Embodiment 2
[0030] Put the crude silane into the light removal tower through the silane compressor, and remove nitrogen, methane, and hydrogen under the conditions of the top temperature of the light removal tower being -80°C, the pressure of 2.5 MPa, and the operating pressure difference of 5 kPa; the liquid at the bottom of the light removal tower Silane is passed into the first weight removal tower, and the temperature at the top of the tower is -40°C, the pressure is 2.49MPa, and the operating pressure difference is 15kPa to remove ethane, ethylsilane, diethylsilane, boron, and phosphorus at the bottom of the tower. The silane gas discharged from the top of the tower is passed through a three-stage adsorption tower, the adsorption tower is equipped with 4A molecular sieve, and the operating pressure of the adsorption tower is 2.3MP to remove ethylene; the purified silane gas enters the second weight removal tower from the adsorption tower, Ethyl silane is removed under the condition th...
Embodiment 3
[0034] Put the crude silane into the light removal tower through the silane compressor, and remove nitrogen, methane, and hydrogen under the conditions that the temperature at the top of the light removal tower is -120 ° C, the pressure is 2.2 MPa, and the operating pressure difference is 2.0 kPa; The liquid silane is passed into the first weight-removing tower, and ethane, ethylsilane, diethylsilane, boron, Phosphorus; the silane gas discharged from the top of the tower passes through a three-stage adsorption tower, which is equipped with 4A molecular sieves, and the operating pressure of the adsorption tower is 1.8MP to remove ethylene; the purified silane gas comes out of the adsorption tower and enters the second weight removal tower , under the condition that the temperature at the top of the tower is -60°C, the pressure is 1.6MPa, and the operating pressure difference is 8kPa, ethyl silane is removed, and the pure silane gas leaves the top of the second weight removal tow...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More - R&D
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com
