Produce high-purity edible salt with a continuous, energy-efficient line that integrates brine purification, MVR evaporative crystallization, centrifugation, drying, sizing, iodization, and packaging.
MVR compresses secondary vapor and recycles it as the heating medium, recovering latent heat and cutting utilities while maintaining crystal quality and throughput. Designed for food and chemical plants seeking predictable OPEX and stable output.
Typical electric consumption ~15-40 kWh per ton of water evaporated (design-dependent), with very low fresh steam after start-up.
Forced-circulation crystallization with controlled supersaturation delivers tight size distribution and high clarity.
316L/duplex materials, smooth finishes, drainability, CIP validation, and documentation to support HACCP/ISO programs.
Design inputs: raw salt/brine quality, target NaCl grade, grain size bands, campaign length, utilities, ambient, and hygiene requirements.
Parameter | Typical Target / Range* |
---|---|
NaCl (dry basis) | ≥ 99.2% (up to 99.7% with enhanced purification) |
Moisture (final product) | ≤ 0.2% (grade-dependent) |
Insolubles | ≤ 0.05% (with proper brine polishing) |
Crystal size options | Fine 0.2-0.5 mm; Table 0.5-1.2 mm; Coarse 1.2-2.5 mm |
Line capacity (product salt) | 5-500 t/day (modular trains) |
Electric use (MVR) | ~15-40 kWh per ton of H₂O evaporated |
Campaign length | ≥ 10-20 days between CIP (feed-dependent) |
*Performance depends on feed composition, purification efficiency, compression ratio, and heat-exchange area.
Criterion | MVR Evaporation Line | Multi-Effect (MEE) | TVR |
---|---|---|---|
Fresh Steam Dependence | Very low (mostly electric) | Medium-High | Medium |
Crystal Size Control | Excellent with FC crystallizer | Good (more effects needed) | Fair |
OPEX Stability | High (predictable electric cost) | Variable (steam price/availability) | Variable |
Start/Stop & Load Following | Good | Fair | Fair |
Total Cost of Ownership | Medium-High (shorter payback) | Medium | Medium |
Brine: 24-26 wt% NaCl after purification -> Target: refined table salt with 0.5-1.2 mm grain size.
Train: MVR forced-circulation crystallizer + peeler centrifuge + fluid-bed dryer + sieving + inline iodization + packing.
Takeaways: low fresh steam demand, electric-driven evaporation, continuous recycle of mother liquor, stable product quality, long campaigns between CIP.
Note: Example only. Final design confirmed by lab tests and full heat/mass balance.
Jiangsu Hanpu Mechanical Technology Co., Ltd. is a project engineering company jointly established by Jiangsu Saideli Machinery Co., Ltd., Jiangsu Zhongyi Environmental Technology Co., Ltd., FERREO A/S in Denmark, Shanghai Jiaotong University and Nanjing Kingreat Machinery Co., Ltd.
Hanpu main projects include but are not limited to: MVR evaporation system, powder washing salt and vacuum salt production project, oil tank sludge cleaning project, landfill leachate treatment project, plant/animal oil processing production line, urban wastewater treatment project, various wastewater treatment projects.
The main products are centrifuge series, multi-effect and MVR evaporation and crystallization equipment, laser welding heat transfer board, lithium battery material mixing equipment, pressure vessel and titanium, zirconium, nickel, and other non-standard special equipment.
Proper brine softening (Ca/Mg removal), filtration, and controlled ΔT/velocity minimize scale; CIP restores peak heat transfer.
Yes--inline dosing and mixing are standard, with precise control to meet local regulations.
Fine, table, and coarse grades via sieving/polishing; multi-grade packaging available.
SS316L or duplex for wetted parts; titanium/Hastelloy available for corrosives or special duties.
Absolutely--common flowsheets pair brine purification and RO/NF with MVR crystallization for best energy balance.