Product quality first. An internal draft tube directs circulation while a baffle separates the growth zone from a fines-removal zone — classified-fines destruction produces large crystals (0.5–2 mm) with a narrow distribution that centrifuges easily and carries little mother liquor.
Reference ranges under typical operating conditions on inorganic salt systems.
Two zones, two jobs: the draft tube circulates the growing crystal population; the baffle annuity classifies it — fines leave, product stays.
Slurry → Draft tube (1–2 m/s growth circulation) → Baffle annulus (0.5–1 m/s fines elutriation) → Fines dissolved/removed → Product crystals to discharge
Fines removed at the baffle are dissolved and recycled — the crystal population that remains grows into the narrow, large-crystal distribution DTB is known for.
The internal draft tube directs flow at a controlled 1–2 m/s — the growing population stays suspended and mixed.
Inside the draft tube, crystals grow under controlled supersaturation delivered by the Dimension C method of the plant.
The baffle annulus runs at 0.5–1 m/s: fine crystals are elutriated out, dissolved and returned — keeping them out of the product.
Product crystals leave at 0.5–2 mm — narrow PSD, easy centrifugation, little mother-liquor carryover.
Three vessel configurations, three priorities: FC puts engineering reliability first, DTB puts product quality first, Oslo puts crystal quality first.
| Parameter | FC | DTB (this page) | Oslo |
|---|---|---|---|
| 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 |
d50 ranges reflect typical operating distributions on inorganic salt systems; actual PSD depends on residence time, fines management, seed control and the cooling/evaporation profile.
Chemical systems where large crystals with narrow PSD justify classified growth.
| Chemical | Recommended configuration | Why |
|---|---|---|
| Ammonium sulfate (fertilizer grade) | DTB / Oslo | Fertilizer-grade spec demands large granules — the reference DTB duty |
| Urea | DTB | Fertilizer-grade large-granule standard process |
| Potassium chloride | DTB | Potash-industry standard |
| PTA | DTB / cooling crystallization | Large-capacity continuous crystallization |
| Oxalic acid | DTB / continuous | Continuous crystallization replacing batch operation |
| Battery-grade Li₂CO₃ | DTB (growth stage) | Reaction precipitation followed by DTB growth in the reference route |
Chemical-configuration mapping from the crystallizer-type technical reference; final selection requires solubility data, impurity profiling and crystallization trials.
DTB is the answer when product spec (PSD, centrifuge yield, mother-liquor carryover) is the priority and the feed is not extreme.
DTB is a Dimension D crystal growth configuration — the selection logic is explicit: product quality first, with stable crystal size, easy centrifugation and minimal mother-liquor carryover. It pairs with any Dimension C supersaturation method (evaporative, cooling, vacuum cooling). d50 and PSD outcomes depend on residence time, fines-management settings, slurry density (15–30 wt% band) and the driving-force profile. All figures are indicative ranges for preliminary screening, not a process guarantee.
Recurring questions from engineers choosing a growth configuration.
It creates a low-velocity annulus (0.5–1 m/s) where fine crystals are elutriated out of the growth zone, dissolved and recycled. Removing fines continuously is what keeps the product distribution narrow — without it, the fines compete for solute and the PSD widens.
DTB delivers 0.5–2 mm with classified-fines removal — preferred when downstream centrifugation throughput is the priority. Oslo produces larger crystals (1–5 mm) with very low fines — preferred when crystal size and purity matter most. Both reach high purity; the choice depends on which downstream property you value.
Good but not FC-grade. DTB tolerates moderate scaling tendency; on high-TDS, heavily scaling mixed-salt liquors, FC's high-velocity loop is the reliable choice. Putting classified equipment on an unstable feed trades availability for PSD you may never collect.
The 15–30 wt% band is a primary size lever — higher slurry density gives more crystal surface area, lower per-crystal supersaturation and larger product. It is one of the main operating variables, tuned against the fines-removal rate.
Send us the chemical system, target PSD and purity, and feed conditions. We will return a preliminary DTB vs. FC vs. Oslo 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.