Comparison of RO, MED, MSF desalination water in terms of cost, energy consumption, chemical requirement of the industry

Choosing a desalination plant is not just a technical decision — it’s an economic, energy, and management decision that can change your operating costs by up to 40%.
In this comprehensive and detailed guide, we compare the three most widely used technologies, RO (reverse osmosis), MED (multi-effect distillation), and MSF (multi-stage evaporation), from three critical angles:
- Capital and operating costs
- Energy consumption
- Chemical requirements and maintenance challenges
All figures are for comparison purposes only and may change over the coming years. Our goal is to help you choose the best option for your industry, budget, and geographic conditions with real-world data and technical analysis.
Why read this article?
✅ A realistic and accurate comparison of the three main desalination technologies
✅ Understand the key differences in cost, energy, and chemical requirements
✅ Identify the best option for your industry (refinery, power plant, municipal, etc.)
✅ Avoid making the wrong choice that can multiply your operating costs

Brief introduction of the three technologies — comparison background
RO (Reverse Osmosis) — Reverse Osmosis
- Technology type: Membrane — Physical
- Heat requirement:❌No
- Capacity: Small to very large (1 to 1000+ cubic meters per day)
MED (Multi-Effect Distillation) — Multi-effect distillation
- Technology type: Thermal — Evaporation and condensation
- Heat requirement:✅Yes (60 to 70°C)
- Capacity: Medium to large (500 to 50,000 cubic meters per day)
MSF (Multi-Stage Flash) — Multi-stage evaporation
- Technology type: Thermal — Evaporative flash
- Heat requirement:✅Yes (90 to 110°C)
- Capacity: Very large (5000 to 80,000+ cubic meters per day)
Comparison in terms of energy consumption — Which technology is energy efficient?
Parameter | RO | MED | MSF |
Energy consumption (kilowatt hours per cubic meter of water produced( | 3 – 6 kWh/m³ ERD: (with 2.5 – 4 kWh/m³) | 8 – 15 kWh/m³ (thermal equivalent) | 10 – 20 kWh/m³ (thermal equivalent) |
Type of energy consumed | Electricity (pressurizer) | Steam or hot water | High temperature steam |
Energy recycling capability | Save up to 40% with ERD (Energy Recovery Device) | In sequential effects Heat recovery | Limited — energy is consumed in the early stages |
Sensitivity to incoming water quality | Very high — low quality → higher energy consumption | Low — tolerance for quality fluctuations | Low — tolerance for quality fluctuations |
Energy Summary:
- RO:Most energy efficient — especially with ERD — suitable for areas with cheap electricity
- MED:Thermal energy efficient — suitable for industries with excess steam (e.g. power plants) — if recovered heat is used, energy cost ≈ zero
- MSF:Most energy efficient — but at large capacities, cost per cubic meter decreases
Comparison in terms of chemical requirements and maintenance challenges
Parameter | RO | MED | MSF |
Need for antifouling | ✅ Very high Continuous injection necessary | ✅ Moderate Vital at high temperatures | ✅ Above Especially in Brine Heater |
Need for anti-corrosion | ❌Low Only in steel pipes - low cost | ✅ Up In pipes and evaporators | ✅ Very high In flash chambers and condensers |
Need for chemical cleaning | ✅ Periodic (every 3-6 months) membranes | ✅ Periodic (every 6-12 months) tubes | ✅ Periodic (every 6-12 months) compartments |
The main chemical challenge | Membrane fouling — sedimentation — biofouling | Scale in evaporator tubes — thermal corrosion | Severe corrosion — deposits in condensers — leaks |
Sensitivity to pH and alkalinity | ✅ Too high Improper pH → Membrane damage | ✅ High High pH → Sediment Low pH → Corrosion | ✅ Very high precise control to prevent corrosion |
Chemical Summary
- RO: Requires careful management of incoming water and anti-scale injection — but no risk of metal corrosion — Chemical cost is highest
- MED: Requires anti-scale and thermal anti-corrosion — but no membrane — More stable in the long term — Chemical cost is lower than RO
- MSF: Requires strong anti-corrosion — due to the presence of chloride and high temperature — Risk of leakage is more serious — Chemical cost is similar to RO
Which technology is suitable for which industry?
Industries with limited budget and small to medium capacity (under 5000 m3/day)
RO recommendation:
- Reason: Lower initial investment — Quick start-up — Suitable for areas without access to steam
- Example: Food, pharmaceutical, small steel plants
Industries with access to cheap steam or hot water (power plants, refineries)
MED recommendation:
- Reason: Use of recycled energy — Lowest operating cost in the long run — Excellent water quality
- Example: Thermal power plants, oil refineries — In these cases, MED is cheaper than RO!
Very large municipal or industrial projects (above 20,000 m3/day)
MSF proposal:
- Reason: High reliability — Long life — Massive production without the need for membranes
- Example: Coastal cities, large refineries, government projects
Industries requiring ultrapure water (pharmaceutical, semiconductor)
RO + EDI proposal:
- Reason: RO as pretreatment — EDI for UPW production — No regeneration chemicals
Final summary table — Quick selection based on your preference
Your priority | The best option | Reason |
The lowest initial investment | ✅ RO | Suitable for quick start-ups and limited budgets |
The least energy-consuming (with electricity) | ✅RO (with ERD) | Low power consumption — save energy by recycling |
The least expensive operation in the long run | ✅ MED with recycled heat | Energy cost ≈ zero — no membrane replacement cost — low chemical |
Suitable for large capacity | ✅ MSF | The only option for producing 50,000+ cubic meters per day |
Suitable for remote areas | ✅RO | No thermal infrastructure required — just electricity |
Real example: Comparison of operating costs in a refinery in southern Iran (capacity 5,000 cubic meters per day)
Technology | Annual Operating Cost (USD per cubic meter) (Prices are for comparison purposes only) | Explanation |
RO | 0.75 $ | Seawater with high TDS - High antifouling requirement - Membrane replacement every 3 years - High pretreatment cost |
MED | 0.25 $ | Use of recycled steam - zero energy costs - low chemicals - no membranes - long life |
MSF | 0.85 $ | Commercial steam consumption - need for expensive anti-corrosion - high maintenance costs |

Result: In this real-world project, MED is the cheapest operation, not RO.
✅Final Conclusion:
Choosing between MED, RO, and MSF is not a “one-size-fits-all” decision, and RO is not always the cheapest operation
- If you need the lowest cost setup → RO
- If you have access to recovered heat → MED — the cheapest operation in the long run
- If large capacity and high reliability are needed → MSF
With this guide, you can make a more confident decision — and avoid unnecessary costs and operational problems.
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