7N Tellurium Crystal Growth and Purification
I. Raw Material Pretreatment and Preliminary Purification
- Raw Material Selection and Crushing
- Material Requirements: Use tellurium ore or anode slime (Te content ≥5%), preferably copper smelting anode slime (containing Cu₂Te, Cu₂Se) as raw material .
- Pretreatment Process:
- Coarse crushing to particle size ≤5mm, followed by ball milling to ≤200 mesh ;
- Magnetic separation (magnetic field intensity ≥0.8T) to remove Fe, Ni, and other magnetic impurities ;
- Froth flotation (pH=8-9, xanthate collectors) to separate SiO₂, CuO, and other non-magnetic impurities .
- Precautions: Avoid introducing moisture during wet pretreatment (requires drying before roasting); control ambient humidity ≤30% .
- Pyrometallurgical Roasting and Oxidation
- Process Parameters:
- Oxidation roasting temperature: 350–600°C (staged control: low temperature for desulfurization, high temperature for oxidation) ;
- Roasting time: 6–8 hours, with O₂ flow rate of 5–10 L/min ;
- Reagent: Concentrated sulfuric acid (98% H₂SO₄), mass ratio Te₂SO₄ = 1:1.5 .
- Chemical Reaction:
Cu2Te+2O2+2H2SO4→2CuSO4+TeO2+2H2OCu2Te+2O2+2H2SO4→2CuSO4+TeO2+2H2O - Precautions: Control temperature ≤600°C to prevent TeO₂ volatilization (boiling point 387°C); treat exhaust gas with NaOH scrubbers .
II. Electrorefining and Vacuum Distillation
- Electrorefining
- Electrolyte System:
- Electrolyte composition: H₂SO₄ (80–120g/L), TeO₂ (40–60g/L), additive (gelatin 0.1–0.3g/L) ;
- Temperature control: 30–40°C, circulation flow rate 1.5–2 m³/h .
- Process Parameters:
- Current density: 100–150 A/m², cell voltage 0.2–0.4V ;
- Electrode spacing: 80–120mm, cathode deposition thickness 2–3mm/8h ;
- Impurity removal efficiency: Cu ≤5ppm, Pb ≤1ppm .
- Precautions: Regularly filter electrolyte (accuracy ≤1μm); mechanically polish anode surfaces to prevent passivation .
- Vacuum Distillation
- Process Parameters:
- Vacuum level: ≤1×10⁻²Pa, distillation temperature 600–650°C ;
- Condenser zone temperature: 200–250°C, Te vapor condensation efficiency ≥95% ;
- Distillation time: 8–12h, single-batch capacity ≤50kg .
- Impurity Distribution: Low-boiling impurities (Se, S) accumulate at the condenser front; high-boiling impurities (Pb, Ag) remain in residues .
- Precautions: Pre-pump vacuum system to ≤5×10⁻³Pa before heating to prevent Te oxidation .
III. Crystal Growth (Directional Crystallization)
- Equipment Configuration
- Crystal Growth Furnace Models: TDR-70A/B (30kg capacity) or TRDL-800 (60kg capacity) ;
- Crucible material: High-purity graphite (ash content ≤5ppm), dimensions Φ300×400mm ;
- Heating method: Graphite resistance heating, maximum temperature 1200°C .
- Process Parameters
- Melt Control:
- Melting temperature: 500–520°C, melt pool depth 80–120mm ;
- Protective gas: Ar (purity ≥99.999%), flow rate 10–15 L/min .
- Crystallization Parameters:
- Pulling rate: 1–3mm/h, crystal rotation speed 8–12rpm ;
- Temperature gradient: Axial 30–50°C/cm, radial ≤10°C/cm ;
- Cooling method: Water-cooled copper base (water temperature 20–25°C), top radiative cooling .
- Impurity Control
- Segregation Effect: Impurities like Fe, Ni (segregation coefficient <0.1) accumulate at grain boundaries ;
- Remelting Cycles: 3–5 cycles, final total impurities ≤0.1ppm .
- Precautions:
- Cover melt surface with graphite plates to suppress Te volatilization (loss rate ≤0.5%) ;
- Monitor crystal diameter in real time using laser gauges (accuracy ±0.1mm) ;
- Avoid temperature fluctuations >±2°C to prevent dislocation density increase (target ≤10³/cm²) .
IV. Quality Inspection and Key Metrics
Test Item |
Standard Value |
Test Method |
Source |
Purity |
≥99.99999% (7N) |
ICP-MS |
|
Total Metallic Impurities |
≤0.1ppm |
GD-MS (Glow Discharge Mass Spectrometry) |
|
Oxygen Content |
≤5ppm |
Inert Gas Fusion-IR Absorption |
|
Crystal Integrity |
Dislocation Density ≤10³/cm² |
X-ray Topography |
|
Resistivity (300K) |
0.1–0.3Ω·cm |
Four-Probe Method |
V. Environmental and Safety Protocols
- Exhaust Gas Treatment:
- Roasting exhaust: Neutralize SO₂ and SeO₂ with NaOH scrubbers (pH≥10) ;
- Vacuum distillation exhaust: Condense and recover Te vapor; residual gases adsorbed via activated carbon .
- Slag Recycling:
- Anode slime (containing Ag, Au): Recover via hydrometallurgy (H₂SO₄-HCl system) ;
- Electrolysis residues (containing Pb, Cu): Return to copper smelting systems .
- Safety Measures:
- Operators must wear gas masks (Te vapor is toxic); maintain negative pressure ventilation (air exchange rate ≥10 cycles/h) .
Process Optimization Guidelines
- Raw Material Adaptation: Adjust roasting temperature and acid ratio dynamically based on anode slime sources (e.g., copper vs. lead smelting) ;
- Crystal Pulling Rate Matching: Adjust pulling speed according to melt convection (Reynolds number Re≥2000) to suppress constitutional supercooling ;
- Energy Efficiency: Use dual-temperature zone heating (main zone 500°C, sub-zone 400°C) to reduce graphite resistance power consumption by 30% .
Post time: Mar-24-2025