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SS316L NaCl Evaporation System For Sodium Chloride

Categories MVR Evaporator
Brand Name: Hanpu
Model Number: MVR
Certification: CE ISO
Place of Origin: China
MOQ: 1set
Price: USD180,000-USD650,000
Supply Ability: 1sets per 3 months
Delivery Time: 120days
Packaging Details: Pallet or Wooden case
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SS316L NaCl Evaporation System For Sodium Chloride

SS316L NaCl Evaporation System For Sodium Chloride
SS316L evaporation and crystallization system for sodium chloride refining

Food- and chemical-grade SS316L NaCl evaporation & crystallization line engineered for refined sodium chloride. The system integrates brine purification with vacuum evaporation (MEE and/or MVR) and controlled crystallization to deliver consistent grain size, high purity, and low moisture—ready for centrifuging, drying, sizing, iodization, and packing.

Key Benefits
  • High purity output: Stable NaCl grade with low insolubles and moisture.
  • Crystal size control: Tunable nucleation/growth for fine, table, or coarse salt.
  • Energy efficient: Multi-effect staging with optional MVR minimizes steam/OPEX.
  • Hygienic & durable: SS316L wetted parts, drainable layouts, CIP-ready design.
  • Line integration: Seamless tie-in to centrifuge, dryer, screens, and dosing skids.
Process & Thermal Economy

Clarified/polished brine is concentrated under vacuum using multi-effect and/or MVR duty. Tight control of ΔT/LMTD, circulation rate, and residence time stabilizes supersaturation, ensuring repeatable crystallization and low energy consumption.

Materials & Compliance

Wetted parts in SS316L (duplex/Ti on request). Sanitary finishes, traceable materials, drainable piping, and validated CIP supporting HACCP/ISO programs for edible salt production.

Process Overview — Refined Sodium Chloride
Flow: brine make-up & purification → vacuum evaporation (MEE/MVR) → crystallization → centrifugation → drying/sizing → iodization & packing
  • Brine make-up & purification: dissolving, Ca/Mg removal, clarification/filtration, polishing.
  • Vacuum evaporation: multi-effect and/or MVR to achieve target density at low temperature.
  • Crystallization: controlled supersaturation for target grain bands and clarity.
  • Solid–liquid separation: peeler/pusher centrifuge; mother liquor recycle.
  • Drying & sizing: fluid-bed/vibratory drying, sieving/polishing; iodization/anti-caking dosing.
  • Packing: retail 1 kg to 25–50 kg or bulk; weight checks and metal detection.
Key Components
  • Evaporator (falling film / forced circulation) with vapor–liquid separator
  • MVR compressor (turbo/Roots) and/or multi-effect heaters, condensers, vacuum system
  • Brine purification skid: dissolver, softening, clarification, filters/polishers
  • Crystallizer with slurry density control; peeler/pusher centrifuge
  • Fluid-bed/vibratory dryer; screens/polisher; iodization & anti-caking skid
  • PLC/HMI/SCADA; instruments (T/P/flow/cond/level); CIP skid
Performance & Sizing
ParameterTypical Target / Range*
NaCl purity (dry)≥ 99.2% (up to 99.7% with enhanced purification)
Final moisture≤ 0.2% (grade-dependent)
Crystal sizesFine 0.2–0.5 mm; Table 0.5–1.2 mm; Coarse 1.2–2.5 mm
Line capacity5–500 t/day (modular trains)
Energy use (MVR)~15–40 kWh per ton H₂O evaporated
Fresh steam demandVery low after start-up (with MVR)
Campaign length≥ 10–20 days between CIP (feed-dependent)

*Performance depends on feed composition, scaling tendency, compression ratio, and heat-transfer area.

FAQ
Can the system produce multiple grain sizes?

Yes. We tune nucleation/growth and add post-sieving/polishing to supply fine, table, or coarse grades.

Is food-grade documentation available?

Material traceability, surface-finish records, and CIP validation are provided to support HACCP/ISO 22000.

How is energy consumption minimized?

Through multi-effect staging and optional MVR, plus heat recovery and optimized ΔT/LMTD and circulation.

Application
Applications: refined edible salt, industrial NaCl production, and brine upgrading
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