Rb3In(SO4)3 Crystal for UV Laser Frequency Conversion (SHG/OPO/OPA): Hydrothermal Preparation & Applications
Rubidium indium sulfate, Rb3In(SO4)3, is an inorganic mixed-metal sulfate designed for second-order nonlinear optical (NLO) functions where UV capability is required. The crystal is trigonal (space group R3c) with typical unit-cell parameters a=b=15.3–15.5 Å, c=9.0–9.2 Å, α=β=90°, γ=120°, Z=2 and unit-cell volume V=1884–1886 ų. It combines a wide optical bandgap (~5.75 eV, corresponding to an absorption edge near 215 nm) with moderate SHG response (powder SHG ≈ 0.5× KH2PO4 (KDP) at 1064 nm) and can achieve phase matching under 1064 nm excitation (Type I). Reported transmission spans approximately 0.2–8 μm, and thermal stability is above 800°C, making it relevant for UV/visible frequency conversion modules and related photonic systems.
Data note for R&D: the formula mass of Rb3In(SO4)3 is ~659.4 g/mol. If you encounter ~1978.2 g/mol, that value corresponds to 3× the formula unit and should be re-checked during documentation/QC.
1) Detailed Preparation Process (Hydrothermal Route)
Raw materials (engineer-facing)
- Rubidium source: Rb2SO4 (rubidium sulfate). Use high-purity grade to control Na/K/Cl and insolubles.
- Indium source: In2O3 (indium oxide).
- Sulfate chemistry control: H2SO4 (e.g., ~98% mass fraction as commonly used in lab/scale-up practice).
- Solvent: deionized water.
- Reactor: sealed hydrothermal autoclave with PTFE liner (chemical resistance to hot acidic sulfate media).
Target composition window
In the initial mixture, the molar ratio of Rb : In : H2SO4 is controlled within:
| Parameter | Recommended range | Preferred setting |
|---|---|---|
| Rb : In : H2SO4 (molar) | (1.5–7) : (0.5–1) : (1.84–3.68) | (3–6) : 1 : 1.84 |
| Hydrothermal temperature | 180–230°C | 220–230°C |
| Crystallization time | ≥ 48 h | ≥ 72 h |
| Cooling rate | 0.5–15°C/h | 0.5–6°C/h |
Step-by-step workflow
- Batch design & stoichiometry: calculate reactant amounts to fall within the stated Rb : In : H2SO4 molar window (preferred (3–6) : 1 : 1.84). Use Rb2SO4 as the primary rubidium feed to directly supply Rb+ in a sulfate-consistent environment.
- Initial mixing: combine Rb2SO4, In2O3, H2SO4, and deionized water to form a homogeneous starting mixture (typically a slurry due to In2O3). Ensure wetting and dispersion to reduce local concentration gradients.
- Charge the reactor: transfer the mixture into a PTFE-lined autoclave and seal. Maintain appropriate fill level for hydrothermal operation (leave headspace for pressure development).
- Hydrothermal crystallization: heat to 180–230°C (preferred 220–230°C) and hold for at least 48 h (preferred ≥72 h). Under high-temperature/high-pressure aqueous conditions, dissolution–reprecipitation accelerates reaction kinetics and crystal growth, enabling formation of crystalline Rb3In(SO4)3.
- Controlled cooling: cool from crystallization temperature down to room temperature at 0.5–15°C/h (preferred 0.5–6°C/h). Slower cooling supports larger, higher-quality single crystals and reduces thermal stress/defect density.
- Solid–liquid separation: open the reactor after reaching room temperature, collect crystals by filtration, and rinse to remove residual mother liquor (sulfate/acid traces).
- Drying & handling: dry under conditions appropriate for sulfate salts and store to prevent contamination. The product is commonly obtained as colorless, rod-like crystals.
- R&D characterization (typical QC checkpoints): confirm phase purity by powder XRD (peak positions consistent across batches), verify optical window by UV–Vis–NIR/IR measurements, validate thermal stability by TGA (no mass change prior to ~800°C), and benchmark SHG response versus KDP at 1064 nm with particle-size controlled powders for phase-matching assessment.
2) Comparison Summary: This Hydrothermal Process vs Traditional Crystal Growth Routes
For UV-capable NLO crystals, traditional industrial routes often rely on high-temperature melt growth (e.g., Bridgman/Czochralski) or high-temperature solution/flux growth. In sulfate-based systems, elevated-temperature processing can be limited by sulfate chemistry constraints (corrosive melts, volatility, decomposition risks, and impurity incorporation). By contrast, the hydrothermal route here operates at 180–230°C, using hot-compressed water in a sealed vessel to drive dissolution–reaction–crystallization in one pot.
| Dimension | Hydrothermal Rb3In(SO4)3 route | Typical traditional routes (melt/flux/high-T solution) |
|---|---|---|
| Process temperature | Moderate (180–230°C) | Often much higher; may stress sulfate chemistry and equipment |
| Reaction & crystallization | Coupled in one sealed step; high-pressure aqueous environment boosts kinetics | Often multi-step (synthesis → purification → growth) with tighter thermal constraints |
| Purity control | Fewer extraneous anions if Rb2SO4 is used; reduced risk of halide/nitrate residues | Flux components/foreign anions can increase impurity pathways and UV absorption risk |
| Scale-up profile | Autoclave-based; time-driven (48–72 h+) and cooling-rate sensitive | Furnace-based; energy intensive; sensitive to thermal gradients and melt chemistry |
| Crystal quality levers | Cooling rate (0.5–6°C/h) and composition window are primary knobs | Thermal gradient control, pulling rate/rotation, flux composition, atmosphere, crucible interactions |
Practical takeaway for engineers: this route prioritizes composition control, sealed-vessel compatibility, and slow cooling to realize phase-pure Rb3In(SO4)3 with UV-relevant transparency and stable SHG performance.
3) Advantages of Using Rubidium Sulfate and This Process
Why rubidium sulfate (Rb2SO4) is a high-value feedstock here
- Direct sulfate alignment: the target lattice is a sulfate framework ([In(SO4)3]∞ chains with Rb+ charge balance). Starting from Rb2SO4 keeps the rubidium source chemically consistent with the final sulfate coordination environment.
- Cleaner anion landscape for UV optics: using Rb2SO4 avoids introducing halides or nitrates as primary counter-ions, reducing downstream risk of residual anion-related defects or UV absorption tails that can penalize frequency conversion performance.
- Impurity management (critical for optical loss): high-purity Rb2SO4 enables tighter control of alkali impurities (Na/K), chloride, and insolubles—parameters that matter for scattering centers, laser damage threshold behavior, and reproducible growth.
- Stoichiometry & reproducibility: a stable, well-characterized rubidium sulfate feed supports consistent batch-to-batch Rb : In : H2SO4 control, which is one of the main determinants of phase purity and crystallization outcome in hydrothermal synthesis.
Why this hydrothermal workflow is attractive for development-to-production
- Balanced UV criteria: supports materials that combine wide bandgap (~5.75 eV) with usable SHG (~0.5× KDP at 1064 nm) and phase-matching capability.
- Process simplicity: “mix → seal → crystallize → slow-cool → filter/wash” reduces unit operations versus many high-temperature crystal growth chains.
- Engineering knobs are clear: temperature (180–230°C), time (≥48–72 h), and cooling rate (0.5–15°C/h) provide straightforward, scalable control variables.
- Application readiness: the crystal is positioned for UV/visible frequency conversion modules including frequency doublers, optical parametric oscillators (OPO), optical parametric amplifiers (OPA), and optical rectifiers—where wide transparency and thermal stability are practical requirements.
Application focus (for laser system teams): integrate Rb3In(SO4)3 as a nonlinear medium in frequency conversio. The mentioned synthesis method references patent document number CN202110262067.2