Crystal quality first. Supersaturated liquor flows up through a fluidized bed of crystals at very low velocity; crystals grow slowly in suspension and classify themselves by size. The largest crystals of any configuration — 1–5 mm, very uniform — earned on feeds with verified stability.
Reference ranges under typical operating conditions on inorganic salt systems.
Supersaturation is generated externally and fed gently through the bed; the crystal population grades itself from fines at the top to product at the bottom.
Liquor → External supersaturation generation (Dimension C method) → Upflow through fluidized crystal bed (0.02–0.05 m/s) → Classified growth → Large product drawn from bed bottom → Clarified mother liquor overhead
The bed is the classifier: small crystals ride high, grown crystals sink to the discharge zone — no mechanical classification hardware.
The driving force is generated outside the bed — by evaporation or cooling per the plant's Dimension C method — and kept at ≤1–2 g/L.
Liquor rises through the bed at 0.02–0.05 m/s; crystals remain suspended and grade by size.
Crystals spend hours to tens of hours in the bed, growing large and uniform with very low fines.
The largest crystals concentrate at the bottom of the bed and are drawn off as product; clarified liquor leaves overhead.
The fluidized bed holds the entire crystal population inside the metastable zone — that single constraint explains both what Oslo delivers and what it cannot tolerate.
| Condition | What happens in the bed |
|---|---|
| Driving force ≤1–2 g/L | All growth occurs on existing bed crystals — large, uniform product with very low fines |
| Driving force above ~1–2 g/L | Spontaneous nucleation fires inside the bed: new fines appear, classification degrades, and the bed can cement |
| Unstable or fouling-prone feed | Feed excursions spike supersaturation — Oslo earns its higher CapEx only on feeds with verified stability |
This is why Oslo is specified for value-bearing, well-characterized systems — battery-grade sulfates, electronic-grade salts — and not for uncertain liquors: the failure mode is structural, not gradual.
Three vessel configurations, three priorities: FC puts engineering reliability first, DTB puts product quality first, Oslo puts crystal quality first.
| Parameter | FC | DTB | Oslo (this page) |
|---|---|---|---|
| Selection priority | Engineering reliability | Product quality (narrow PSD) | Crystal quality (large, pure) |
| Typical crystal size | 0.2–0.8 mm — moderate, wide distribution | 0.5–2.0 mm — larger, controlled | 1.0–5.0 mm — large, very uniform |
| Fines removal | None standard — no internal classification | Yes — classified-fines removal loop (elutriation zone) | Natural — classification by fluidization |
| Circulation velocity | 2–3 m/s external loop | 1–2 m/s internal draft tube | 0.02–0.05 m/s fluidization upward velocity |
| Supersaturation tolerance | High — recirculation dilutes | Medium — controlled by draft-tube velocity | Low — ≤1–2 g/L to avoid spontaneous nucleation |
| Best for | High-salinity, scaling-prone, mixed-salt systems: NaCl, Na₂SO₄, ZLD mixed salts | Fertilizer (NH₄)₂SO₄, KCl, battery-grade Li₂CO₃ precursor, organic acids | Battery-grade NiSO₄ / CoSO₄ / MnSO₄, pharma intermediates, electronic-grade salts |
| Residence time | Medium (hours) | Medium (hours) | Long (tens of hours) |
d50 ranges reflect typical operating distributions on inorganic salt systems; actual PSD depends on residence time, bed management and the driving-force profile.
Oslo is the answer when large, high-purity crystals justify higher CapEx, long residence and a verified-stable feed; the wrong answer on uncertain liquors.
Oslo is a Dimension D crystal growth configuration, pairing with any Dimension C supersaturation method that can deliver its output gently and at ≤1–2 g/L driving force. The selection logic is explicit: crystal quality first — large particles, narrow distribution — with the acknowledged costs of higher CapEx, long crystal residence and sensitivity to feed stability. All figures are indicative ranges for preliminary screening, not a process guarantee.
Recurring questions from engineers choosing a growth configuration.
The fluidized bed holds the entire crystal population inside the metastable zone. Above roughly 1–2 g/L of driving force, spontaneous nucleation fires inside the bed: new fines appear, the classification that produces those 1–5 mm crystals degrades, and the bed can cement.
Long crystal residence means a large vessel per tonne of product, and the feed must be characterized well enough to hold the sub-metastable driving force continuously. You pay for size and certainty — which is why the configuration pencils out on value-bearing salts.
Not usually. ZLD mixed-salt brines are scaling-prone and composition-variable — exactly the feed instability Oslo cannot tolerate. FC bodies carry that duty; Oslo is reserved for product crystallization on stable liquors.
Both reach battery-grade purity. Oslo delivers 1–5 mm with very low fines and long residence; DTB delivers 0.5–2 mm with classified-fines removal at higher throughput per vessel. If crystal size and downstream handling of large crystals dominate, Oslo; if capacity and centrifuge throughput dominate, DTB.
Send us the chemical system, solubility data, target PSD and purity. We will return a preliminary Oslo vs. DTB vs. FC screening with indicative crystal size — not a brochure.
Send your feed characterization (TDS, COD, main salts, viscosity), throughput and product targets — we respond with a preliminary process route within two business days.