RO Reject Treatment for ZLD
Treatment of high-TDS RO concentrate using MEE, MVR, ATFD, and crystallisation — achieving 93–98% total water recovery and CPCB-compliant Zero Liquid Discharge for industrial facilities
Overview
About RO Reject Treatment for ZLD
Reverse Osmosis is the backbone of industrial Zero Liquid Discharge (ZLD) systems — but RO alone cannot achieve ZLD. An industrial RO plant recovers 65–75% of its feed as purified permeate and rejects 25–35% as a high-TDS brine concentrate. Under CPCB ZLD mandates — applicable to food processing, pharmaceutical, textile, distillery, and tannery industries in water-stressed zones — this RO reject cannot be discharged. It must be further concentrated and dried to zero liquid using thermal evaporation and crystallisation technology.
Spans Envirotech designs and commissions complete RO reject treatment systems as part of integrated ZLD plants. Our approach begins with a detailed analysis of the RO reject stream — TDS, specific ions (sulphates, chlorides, silica, calcium, magnesium), organic content, and temperature — to select the appropriate evaporation technology and materials of construction. Silica scaling, calcium sulphate fouling, and chloride-driven corrosion are the three dominant failure modes in RO reject treatment systems; each is addressed through anti-scalant dosing, softening pre-treatment, and careful material selection (316L SS, duplex steel, or titanium for high-chloride streams).
The standard Spans ZLD technology stack for RO reject treatment begins with pre-treatment softening or anti-scalant dosing to prevent mineral scaling in evaporator tubes. The primary evaporation stage uses either MEE (Multiple Effect Evaporator) for steam-available or lower-volume applications, or MVR (Mechanical Vapour Recompressor) for high-volume continuous operation. MVR is significantly more energy-efficient at 25–35 kWh/tonne evaporated versus 65–90 kWh/tonne for double-effect MEE. The evaporator concentrates the reject TDS from 8,000–20,000 mg/L up to 150,000–200,000 mg/L (15–20% solids).
The concentrated liquor from the evaporator then feeds an Agitated Thin Film Dryer (ATFD) or spray dryer for final drying to a semi-solid or dry cake. Where the dissolved solids are predominantly sodium chloride or sodium sulphate, a crystalliser can produce a crystalline salt product — which may have commercial value or can be disposed of as non-hazardous solid waste. The condensate from all evaporation stages is collected as distillate with TDS typically <20 mg/L, suitable for boiler feed or cooling tower makeup water.
Specifications
Technical Specifications
| RO Feed TDS Range | 500 – 15,000 mg/L |
| RO Reject TDS (Typical) | 5,000 – 60,000 mg/L |
| RO Permeate Recovery | 65 – 75% |
| MEE Energy Consumption | 65 – 90 kWh/tonne (double effect) |
| MVR Energy Consumption | 25 – 35 kWh/tonne evaporated |
| Total ZLD Water Recovery | 93 – 99% |
| ATFD Outlet Moisture | 3 – 8% (w/w) |
| Distillate TDS | < 20 mg/L |
| Evaporator Capacity Range | 1 – 500 tonnes/hr (MVR / MEE) |
| Materials (High Chloride) | Duplex SS / Titanium heat exchangers |
Process
RO Reject to ZLD: Treatment Stages
Pre-Treatment: Softening & Anti-Scalant
RO reject is conditioned prior to evaporation to prevent scaling. Calcium and magnesium hardness ions are removed via ion exchange softening or chemical precipitation. Anti-scalant dosing inhibits silica and calcium sulphate deposition on heat transfer surfaces in the evaporator.
Primary Evaporation: MEE or MVR
The conditioned reject enters a Multiple Effect Evaporator (MEE) or Mechanical Vapour Recompressor (MVR). Water is evaporated using steam (MEE) or the latent heat of the evaporated vapour itself (MVR). TDS is concentrated from 8,000–20,000 mg/L to 150,000–200,000 mg/L. Distillate is collected for reuse.
Secondary Drying: ATFD or Spray Dryer
The concentrated liquor (15–20% dissolved solids) from the evaporator feeds an Agitated Thin Film Dryer (ATFD). The ATFD uses heated rotating blades to spread the liquor as a thin film on a heated cylindrical shell, evaporating remaining water and producing a dry solid or semi-solid cake with 3–8% residual moisture.
Crystallisation (Optional)
Where the dissolved solids are predominantly sodium chloride or sodium sulphate, a crystalliser replaces or supplements the ATFD. Crystallisers produce defined crystalline salts — NaCl or Na₂SO₄ — that can be marketed or disposed of as non-hazardous solid waste, achieving true ZLD with minimum solid waste generation.
Distillate Collection & Polishing
All condensate from evaporation stages is collected and polished through a condensate polisher (mixed bed ion exchange or RO) to achieve TDS <10 mg/L. Polished distillate is returned to the process water system for boiler feed, cooling tower makeup, or CIP water reuse.
Benefits
Key Advantages
CPCB ZLD Compliance
Systems designed to achieve Zero Liquid Discharge as mandated by CPCB for food processing, pharma, textile, and distillery industries in water-stressed zones.
High Water Recovery
Combined RO + evaporation achieves 93–99% total water recovery, returning treated water to production processes and dramatically reducing freshwater intake.
Energy Optimisation
MVR technology reduces evaporation energy to 25–35 kWh/tonne versus 65–90 kWh/tonne for MEE, reducing operating costs significantly over the plant life.
Scaling and Corrosion Control
Pre-treatment design (softening, anti-scalant) and materials selection (duplex SS, titanium) protect heat transfer surfaces and maximise evaporator availability.
Minimal Solid Waste
ZLD systems produce only dry solid cake or crystalline salt — no liquid waste. Crystalline salt may be saleable or disposed of as non-hazardous solid waste.
Proven Technology Stack
Spans integrates established MEE, MVR, and ATFD technology from global OEM partners with in-house process design expertise for the complete RO + evaporation system.
Applications
Industries & Use Cases
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