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Available: 1–100+ m³/hr evaporation duty

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

Manufactured in India
Pan-India Supply & Installation
Genuine Spare Parts
AMC & After-Sales Support

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.

MVR
Representative single-stage MVR evaporator skid — evaporator, vapour-liquid separator, and recompressor package. Illustration for reference; not to scale.

Schematic

Typical System Schematic

FeedPreheaterFalling-filmevaporatorVapour–liquidseparatorVapour recompressor (blower)Distillateto reuseConcentrate tocrystalliser / ATFDRaw feed / RO rejectSecondaryvapourRecompressed vapourConcentrateFeedSecondary vapourRecompressed vapourDistillateConcentrate
Typical MVR evaporation loop: secondary vapour from the separator is recompressed and returned as the heating medium, so the latent heat is recycled instead of being lost to a condenser.

Specifications

Technical Specifications

Evaporation capacity1–100+ m³/hr per train (multiple trains for higher duty)
Steam economyEquivalent to a 10–40 effect MEE (electrical drive only)
Energy inputElectrical to compressor; ~15–40 kWh per m³ water evaporated (duty-dependent)
Evaporator typeFalling film (clean liquors) or forced circulation (scaling / viscous liquors)
CompressorHigh-speed centrifugal or positive-displacement blower; ΔT lift 3–10 °C
Feed TDS handlingDilute streams up to near-saturation; crystalliser integration for ZLD
Distillate qualityCondensate typically <50–100 µS/cm — reusable as boiler feed / process water
Materials of constructionSS 316L / SS 904L / duplex / titanium as per liquor chemistry
AutomationPLC / SCADA control of temperature, level, feed–product ratio and CIP

Process

How MVR Evaporation Works

1

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.

2

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.

3

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.

4

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.

5

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.

6

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

Zero Liquid Discharge (ZLD) PlantsPower Plant Boiler Blowdown ConcentrationPharmaceutical & API Manufacturing EffluentChemical & Specialty Chemical Industry WastewaterTextile Dyeing & Processing EffluentFertiliser & Agrochemical ManufacturingDistillery & Fermentation Stillage ConcentrationFood & Dairy Industry Process LiquorsPulp & Paper Black Liquor EvaporationReverse Osmosis Reject ConcentrationFlue Gas Desulfurization (FGD) WastewaterLandfill Leachate Treatment & Concentration

FAQ

Frequently Asked Questions

How much energy does MVR save compared with a multi-effect evaporator (MEE)?
MVR recycles the latent heat of the vapour it produces, so a single MVR stage delivers a steam economy equivalent to a 10–40 effect MEE while consuming only electrical energy for the compressor. In high-evaporation-rate duties this typically cuts thermal energy cost by up to 90% versus single-effect evaporation, at the expense of a higher compressor capital cost.
When is MVR preferred over MEE for a ZLD plant?
MVR is preferred where electricity is available and reasonably priced, the boiling point elevation is moderate, and evaporation volumes are large enough for the compressor CAPEX to pay back through steam savings. MEE is often retained where cheap waste steam already exists or for very high-boiling-point-elevation liquors. Many ZLD trains combine both — MVR for bulk concentration, followed by a forced-circulation crystalliser or ATFD for the final drying step.
What distillate quality does an MVR system produce?
The condensate recovered from an MVR evaporator is high-purity distillate, typically below 50–100 µS/cm conductivity, suitable for reuse as boiler feed water, cooling tower make-up, or process water — which is a major part of the ZLD business case.
Can MVR handle scaling or high-TDS liquors?
Yes. For clean or mildly fouling liquors a falling-film MVR evaporator is used; for scaling, viscous, or crystallising liquors (high CaSO₄, CaCO₃, or silica) a forced-circulation MVR configuration with anti-scale dosing and periodic CIP is specified. Beyond the solubility limit the concentrate is sent to a crystalliser or ATFD.
What is the difference between MVR and TVR?
MVR (Mechanical Vapour Recompression) uses an electrically driven compressor to recompress the vapour, giving the highest energy efficiency. TVR (Thermal Vapour Recompression) uses a steam-driven ejector and is simpler and cheaper but far less efficient. MVR is the technology of choice where energy cost dominates operating economics.

Ready to Source Mechanical Vapour Recompressor (MVR)?

Our engineers will review your requirements and provide specifications, pricing, and delivery timelines — typically within 24 hours.

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