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FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project

Jiangsu Hanpu Mechanical Technology Co., Ltd
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    Buy cheap FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project from wholesalers
     
    Buy cheap FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project from wholesalers
    • Buy cheap FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project from wholesalers
    • Buy cheap FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project from wholesalers
    • Buy cheap FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project from wholesalers
    • Buy cheap FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project from wholesalers

    FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project

    Ask Lasest Price
    Brand Name : Hanpu
    Model Number : MVR
    Certification : CE ISO
    Price : USD180,000-USD650,000
    Supply Ability : 1sets per 3 months
    Delivery Time : 120days
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    FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project

    FC Crystallizer MVR Evaporator — 3T/Hr for Potassium Chloride Project
    Forced-circulation crystallizer with MVR evaporator rated 3 t/h for potassium chloride (KCl) production

    Engineer-to-order MVR (Mechanical Vapor Recompression) evaporator integrated with an FC (Forced-Circulation) crystallizer for potassium chloride (KCl) concentration and crystal production. The train is sized for a nominal 3 t/h water removal, delivering stable supersaturation control, narrow crystal size distribution, and low OPEX for potash brines and carnallite conversion lines.

    Key Benefits
    • Energy saving: Electric-driven vapor recompression minimizes fresh steam after start-up.
    • Crystal quality: FC loop stabilizes supersaturation and residence time for tight KCl PSD.
    • Scaling mitigation: High-velocity circulation maintains coefficients and limits deposition.
    • Process flexibility: Handles sylvinite/carnallite liquors; integrates with flotation or hot-leach routes.
    • Automated uptime: PLC/HMI recipes, alarms, historian, and remote diagnostics for 24/7 operation.
    Process & Thermal Economy

    Potash brine is purified and concentrated under vacuum in the MVR body. The forced-circulation crystallizer runs at controlled slurry density and ΔT/LMTD; recompressed vapor provides the primary duty, achieving low specific energy while promoting predictable KCl crystallization and clarity.

    Materials & Cleanability

    Wetted parts in SS316L/duplex (Ti/Hastelloy on request) for chloride-rich brines. Drainable layouts, large clean-outs, and validated CIP extend campaign length and simplify turnarounds.

    Process Overview — KCl Brine to Crystals
    Flow: brine polishing → MVR evaporation (vacuum) → FC crystallizer → centrifuge → dryer/sizing → packing
    • Brine polishing: clarification/filtration; Mg/Ca control as required.
    • MVR evaporation (vacuum): compressor discharge sets ΔT; shell pressure defines boiling point.
    • FC crystallization: seed addition; slurry density and residence time tuned for target PSD.
    • Solid–liquid separation: pusher/peeler centrifuge; mother liquor recycle to circuit.
    • Drying & sizing: fluid-bed/vibratory drying; screens for granular grades.
    Key Components
    • MVR evaporator (falling film / forced circulation) with vapor–liquid separator
    • Mechanical vapor compressor (turbo/Roots) with VFD for ΔT/capacity control
    • FC crystallizer with circulation pump, draft tube/heat exchanger, slurry density control
    • Surface condenser, vacuum/NCG handling, preheaters/heat-recovery HX
    • PLC/HMI/SCADA; instruments (T/P/flow/cond/level/solids); CIP skid and antiscalant dosing
    Performance & Sizing
    ParameterTypical Target / Range*
    Evaporation rate3 t/h (water removal), adjustable via compressor VFD
    Operating modeVacuum, continuous
    KCl purity (dry)≥ 98–99% (feed-dependent, with proper purification)
    Crystal size bandsFine 0.3–0.6 mm; Standard 0.6–1.0 mm; Coarse 1.0–2.0 mm
    Electric use (MVR)~15–40 kWh per ton H₂O evaporated (duty/CR dependent)
    Fresh steam demandVery low after start-up (backup/ancillary only)
    MaterialsSS316L / duplex; Ti/Hastelloy on request

    *Performance depends on brine composition (K⁺/Mg²⁺/Na⁺), scaling tendency, compression ratio, and crystallizer design.

    FAQ
    Can the line process carnallite liquors?

    Yes—flowsheets can include Mg control and hot leach steps; the FC crystallizer is tuned for KCl selectivity and PSD.

    How do you control scaling?

    Optimized ΔT/velocity, antiscalant dosing, and scheduled CIP maintain heat-transfer coefficients and crystal purity.

    Can we integrate with existing flotation/drying?

    Yes—the MVR+FC module ties into upstream purification and downstream centrifuge/dryer/screening with minimal retrofit.

    Application
    Applications: potash (KCl) production, carnallite conversion, and potash brine upgrading with FC crystallizer MVR
    Quality FC Crystallizer MVR Evaporator 3T / Hr For Potassium Chloride Project for sale
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