Device for recovering hydrogen from exhaust gas of silicon epitaxy furnace and method for producing high-purity hydrogen
A technology of silicon epitaxy and hydrogen, which is applied in the direction of hydrogen separation, liquid contact hydrogen separation, solid contact hydrogen separation, etc., can solve the problems of non-renewable, large investment, limited application range, etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0051] (1) Epitaxial furnace tail gas
[0052] Epitaxy tail gas volume: 200m 3 / h Temperature: 25°C Pressure: 0.15 atmospheres
[0053] Main components: H 2 97.5%, O 2 2%, Cl 2 ≥100ppm, the rest is a small amount of carbon dioxide, silane, phosphine, etc.
[0054] (2) Dechlorination agent
[0055] Filled with QT-C1 high-efficiency dechlorination agent (main component: ZnO / Al 2 o 3 / CaO / activated carbon / accelerator added, Dalian Zhongding Chemical Co., Ltd. self-made mass ratio 20%, 40%, 15%, 20%, 5%), use space velocity: 1000h -1 Total loading: 0.2m 3
[0056] Fine dechlorination tower aspect ratio: 5
[0057] (3) Catalyst
[0058] Catalytic deoxidation CTC-1 precious metal catalyst (active component is palladium, carrier is alumina, active component accounts for 0.2% to 0.5% of the weight of the carrier component)
[0059] Noble metal catalyst use space velocity: 5000h -1
[0060] The total amount of precious catalyst loaded: 0.04m 3
[0061] Catalytic deoxida...
Embodiment 2
[0067] (1) Epitaxial furnace tail gas
[0068] Exhaust gas volume: 100m 3 / h Temperature: 25°C Pressure: 0.13 atmospheres
[0069] Main components: H 2 99%, O 2 0.5%, Cl 2 ≤100ppm, the rest is a small amount of carbon dioxide, silane, phosphine, etc.
[0070] (2) Dechlorination agent
[0071] Filled with QT-C1 high-efficiency dechlorination agent (main component: ZnO / Al 2 o 3 / CaO / activated carbon / accelerator added, Dalian Zhongding Chemical Co., Ltd. self-made mass ratio 20%, 40%, 15%, 20%, 5%), use space velocity: 2000h -1 Total loading: 0.1m 3
[0072] Fine dechlorination tower aspect ratio: 7
[0073] (3) Catalyst (same as above embodiment 1) precious metal catalyst use space velocity: 5000h -1
[0074] The total amount of precious catalyst loaded: 0.02m 3
[0075] Catalytic deoxidation tower aspect ratio: 6
[0076] (4) steps
[0077] The epitaxy tail gas hydrogen (100m 3 / h) (wherein the chlorine content ≤ 100ppm, oxygen content 0.5%) is directly passed ...
PUM
| Property | Measurement | Unit |
|---|---|---|
| recovery rate | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 
