Engineer-to-order MVR (Mechanical Vapor Recompression) evaporator and crystallization line designed to concentrate unsaturated NaCl solutions to the crystallization zone and produce controlled sodium chloride crystals. Recompressing secondary vapor as the heating medium delivers low OPEX, stable supersaturation, and consistent product quality.
Unsaturated brine is purified and concentrated under vacuum. The MVR compressor raises vapor temperature, which is reused as the primary heat source. Controlled circulation and seeding bring the liquor into the metastable region, enabling predictable NaCl crystallization at low specific energy consumption.
Wetted parts in SS316L/duplex; drainable layouts and CIP-ready design. Optional food-contact finishes and documentation for edible salt production.
Parameter | Typical Target / Range* |
---|---|
NaCl purity (dry) | ≥ 99.2% (up to 99.7% with enhanced purification) |
Moisture (final) | ≤ 0.2% (grade-dependent) |
Crystal size bands | Fine 0.2–0.5 mm; Table 0.5–1.2 mm; Coarse 1.2–2.5 mm |
Electric use (MVR) | ~15–40 kWh per ton H₂O evaporated (duty/CR dependent) |
Fresh steam demand | Very low after start-up (backup/ancillary only) |
Campaign length | ≥ 10–20 days between CIP (feed-dependent) |
*Performance depends on feed composition, scaling tendency, compression ratio, and exchanger/crystallizer design.
Yes—recipes adjust ΔT, circulation, and seeding to stabilize supersaturation and crystal quality despite feed drift.
Proper softening, optimized LMTD/velocity, anti-scale dosing, and scheduled CIP maintain heat-transfer coefficients.
We provide SS316L/duplex construction, drainable hygienic layouts, and documentation to support HACCP/ISO programs.