Method and device for preparing superfine copper powder
A technology of ultra-fine copper powder and copper oxide, which is applied in separation methods, combined devices, chemical instruments and methods, etc. flow etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0056] Nano-copper oxide powder (particle size 110nm) enters the cyclone preheater 4 to preheat to 250°C through the vibrating feeder 2 and the airflow conveying device 3, and sends it into the first fluidization through the first feed valve 5 and the riser 6. The bed reactor 7 is in contact with the first fluidized bed carrier gas PG1 from the bottom of the first fluidized bed reactor 7 and undergoes a reduction reaction, the reaction temperature is 210° C., and the superficial gas velocity of the carrier gas is 1 m / s, Reducing gas H 2 The volume concentration is 10%, and the contact method is countercurrent, so that the material is in a bubbling fluidized state. The residence time of the material in the first fluidized bed reactor 7 is 20min, so that the conversion rate of the copper oxide after the reaction in the first fluidized bed reactor is about 70%; Bed reactor 9; tail gas is discharged through the outlet of the first cyclone separator 13, and enters the combustion c...
Embodiment 2
[0058] Nano-copper oxide powder (particle size 120nm) enters the cyclone preheater 4 to preheat to 200°C through the vibrating feeder 2 and the air conveying device 3, and sends it into the first fluidization through the first feed valve 5 and the riser 6. The bed reactor 7 is in contact with the first fluidized bed carrier gas PG1 from the bottom of the first fluidized bed reactor 7 and undergoes a reduction reaction, the reaction temperature is 180°C, and the superficial gas velocity of the carrier gas is 0.5m / s , the reducing gas H 2 The volume concentration is 30%, and the contact method is countercurrent, so that the material is in a bubbling fluidized state. The residence time of the material in the first fluidized bed reactor 7 is 3min, so that the conversion rate of the copper oxide after the reaction in the first fluidized bed reactor is about 70%; Bed reactor 9; tail gas is discharged through the outlet of the first cyclone separator 13, and enters the combustion ch...
Embodiment 3
[0060] Ultrafine copper oxide powder (particle size 1-2μm) enters the cyclone preheater 4 to preheat to 200°C through the vibrating feeder 2 and the air conveying device 3, and sends it into the first feed valve 5 and the riser 6 into the first The fluidized bed reactor 7 is in contact with the first fluidized bed carrier gas PG1 from the bottom of the first fluidized bed reactor 7 and undergoes a reduction reaction. The reaction temperature is 150° C., and the superficial gas velocity of the carrier gas is 0.1 m / s, reducing gas H 2 The volume concentration is 20%, and the contact method is cross-flow, so that the material is in a bubbling fluidized state. The residence time of the material in the first fluidized bed reactor 7 is 60min, so that the conversion rate of copper oxide after the reaction in the first fluidized bed reactor is about 80%; Bed reactor 9; tail gas is discharged through the outlet of the first cyclone separator 13, and enters the combustion chamber 15 bu...
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



