Mechanical Vapour Recompressor (MVR)
High-efficiency evaporation technology using vapour recompression to achieve up to 90% energy savings over conventional multi-effect evaporators — for zero liquid discharge, high-TDS wastewater concentration, and industrial process liquor treatment
Overview
About Mechanical Vapour Recompressor (MVR)
Mechanical Vapour Recompression (MVR) is an energy-efficient evaporation technology in which the secondary vapour generated during evaporation is mechanically recompressed by a high-speed centrifugal or positive-displacement compressor and returned as the heating medium to the same evaporator. By recycling the latent heat of evaporation rather than discarding it to a condenser, MVR systems achieve thermal efficiencies far beyond those of conventional multi-effect evaporators — making them particularly suited to applications where steam costs are high or where zero liquid discharge (ZLD) is a regulatory requirement.
In a conventional multi-effect evaporator (MEE), each additional effect recovers heat from the previous stage's vapour at a progressively lower pressure and temperature, typically achieving a steam economy (kg water evaporated per kg steam consumed) of 3–6. In contrast, an MVR system achieves steam economies equivalent to a 10–40 effect MEE using only electrical energy for the compressor, dramatically reducing operating costs in high-evaporation-rate applications. The trade-off is higher capital cost of the compressor versus lower ongoing steam and cooling water consumption.
MVR systems are most economically attractive when the temperature difference required across the heat transfer surface (boiling point elevation) is small — typically in clean or moderately fouling liquors where operating temperatures are moderate. For heavily scaling liquors (high CaSO₄, CaCO₃, or silica concentrations), forced circulation MVR evaporators with anti-scale provisions and regular chemical cleaning cycles are used. MVR is the enabling technology for economically viable Zero Liquid Discharge (ZLD) plants in industries such as power generation, chemicals, textiles, and pharmaceuticals.
Integration of MVR with a crystalliser in a ZLD train enables concentration of the evaporator concentrate to the point of crystallisation, producing a dry salt cake for landfill disposal or recovery. The combination of MVR evaporation (low energy cost, high throughput) with a Forced Circulation Crystalliser achieves the lowest operating cost path to zero liquid discharge for high-volume high-TDS streams.
Process
How MVR Evaporation Works
Feed Preheating
Incoming wastewater or process liquor is preheated against hot condensate and product concentrate in plate heat exchangers, recovering available heat before entering the evaporator vessel. Preheating reduces the thermal load on the evaporator and improves overall energy efficiency.
Evaporation in the Heat Exchanger
Preheated feed enters the evaporator vessel (falling film, forced circulation, or rising film type depending on fouling tendency). Steam or compressed vapour on the shell side provides heat through the tube wall; the feed boils on the tube side and generates secondary vapour.
Vapour Separation
The vapour-liquid mixture from the evaporator tubes rises into the vapour-liquid separator. Liquid droplets disengage and fall back to the circulation loop; clean secondary vapour exits the top of the separator for recompression.
Mechanical Vapour Recompression
The centrifugal compressor draws secondary vapour from the separator and compresses it to a slightly higher pressure and temperature — typically raising the dew point by 3–10°C. This recompressed vapour is now hot enough to serve as the heating medium for the evaporator, closing the energy loop.
Recompressed Vapour as Heating Steam
Recompressed vapour is fed to the shell side of the evaporator heat exchanger, where it condenses and gives up its latent heat to the boiling feed. The condensate (distillate quality) is removed continuously, representing the evaporated water that has been extracted from the feed.
Concentrate Withdrawal
As water is evaporated, the feed concentration rises. Concentrated liquor is continuously or intermittently withdrawn from the circulation loop and sent to a crystalliser, dryer, or disposal system depending on the ZLD configuration. Product condensate is collected for reuse as process water.
Benefits
Key Advantages
- Steam economy equivalent to a 10–40 effect MEE using only electrical energy — up to 90% reduction in steam consumption versus single-effect evaporation
- Dramatically lower operating costs for high-volume evaporation duties in energy-intensive industries
- Enables economically viable Zero Liquid Discharge (ZLD) for high-TDS industrial wastewater streams
- Falling film configuration minimises fouling and provides gentle treatment for heat-sensitive liquors
- Forced circulation option handles scaling, viscous, and crystallising liquors prone to fouling
- Compact single-vessel design compared to multi-effect trains occupying large floor areas
- High-quality distillate output — condensate suitable for boiler feed water or process water reuse
- Fully automated operation with PLC/SCADA control of temperatures, pressures, and feed-product ratios
- Reduced cooling water requirement — no large condenser needed since vapour is recycled
- Compatible with crystalliser integration for complete ZLD train achieving dry salt disposal
Applications
Industries & Use Cases
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