By Challenge / Contaminant
Iron Removal Water Treatment Companies
Iron and manganese removal, oxidation, greensand, biological filters, and sequestration for well and surface water.
This page is a good fit if you need:
- Granular Activated Carbon (GAC) Filters or Ion Exchange capabilities
- Suppliers with manufacturing sector experience
- Providers operating in United Kingdom or Netherlands
- Providers
- 50
- Verified
- 5
- Countries
- 11
Can't find the right fit? Post a brief and let qualified suppliers come to you.
Post a projectHow to choose a iron removal water treatment provider
Start with providers that clearly operate in your target geography and project footprint.
Look for industry exposure that matches your water challenge, compliance constraints, and deployment context.
Use technologies, service scope, and proof signals to narrow the list before reaching out to suppliers.
Not sure where to start? Our experts can help.
Filter results
Verified providers
5 claimed companies in this category
Country
Industry
Technology
Find a Iron Removal Water Treatment Provider
Showing 1-20 of 50
50 results from 50 matched providers
Iron Removal from Water: Aeration, Oxidation, and Filtration Process Design
Iron occurs in groundwater as dissolved ferrous iron Fe(II) at concentrations of 0.1 to 20 mg per L under anoxic conditions (no dissolved oxygen). Contact with oxygen in the distribution system or at the tap causes Fe(II) to oxidise to ferric Fe(III) and precipitate as rust, discolouring water brown-red and causing taste complaints. WHO Drinking Water Guideline for iron: 0.3 mg per L (aesthetic); EU DWD 2020 parametric value: 0.2 mg per L; US EPA secondary MCL: 0.3 mg per L. Iron removal target for most utilities is below 0.05 mg per L to allow for some re-dissolution in the distribution system. Manganese (often co-present with iron in groundwater) must also be considered: WHO guideline 0.4 mg per L, EU DWD 2020: 0.05 mg per L.
Iron removal processes begin with oxidation: aeration (cascade aerator or packed tower, achieves dissolved oxygen above 7 mg per L, oxidising Fe2+ to Fe3+ at pH above 7, reaction complete in 15 to 30 minutes), chlorination (1 to 2 mg per L free chlorine, oxidation complete in 1 to 5 minutes, also disinfects), potassium permanganate (0.5 to 1 mg per L, immediate oxidation, used when aeration is insufficient), or ozonation (0.5 to 1 mg per L O3). Following oxidation, Fe(III) floc is removed by: gravity filtration (sand-anthracite multimedia filter, hydraulic loading 5 to 10 m per hr, run length 24 to 72 hours before backwash), or pressure filtration (higher throughput per unit area). For low-iron groundwater below 1 mg per L, contact filtration with oxidising media (greensand plus KMnO4 regeneration, or manganese dioxide-coated media) may be sufficient.
Design considerations: pH above 7 is required for efficient Fe(II) oxidation by dissolved oxygen (oxidation rate doubles per pH unit above 7 at constant DO). Organic complexed iron (tannins, humic acids) does not respond to simple aeration and oxidation; coagulation (alum or ferric sulphate, 5 to 20 mg per L) or oxidation with ozone at higher doses (2 to 4 mg per L) is required to break the organic-iron complex. High-iron groundwaters often contain co-contaminants (hydrogen sulphide: rotten egg odour, treated by aeration; arsenic: co-precipitation with Fe(III) at above 0.3 mg per L iron provides some natural removal). Backwash water from iron removal filters is typically 3 to 5 percent of throughput; backwash supernatant can be recycled to the head of the works while filter cake (iron hydroxide sludge) requires dewatering (centrifuge or filter press) and disposal as non-hazardous solid waste.
Frequently Asked Questions
What causes high iron in drinking water?
High iron in drinking water has two main sources: (1) Groundwater - dissolved ferrous iron Fe(II) is naturally present in anoxic (oxygen-depleted) groundwater where reducing conditions have dissolved iron from iron-bearing minerals (siderite, pyrite, iron-bearing silicates). Concentrations of 1 to 20 mg per L are common in many aquifer types globally. (2) Distribution system corrosion - iron pipes (cast iron, ductile iron) corrode in aggressive water (low pH, high chloride, low alkalinity, high dissolved CO2), releasing ferric hydroxide tubercles and corrosion products that discolour water. Source iron is best addressed at the treatment works. Distribution corrosion iron requires water chemistry adjustment (pH buffering to 7.5 to 8.5, orthophosphate dosing to form a protective corrosion barrier on pipe walls) and pipe replacement programme for severely tuberculated mains.
What is the most effective way to remove iron from borehole water?
For typical borehole water with iron 1 to 10 mg per L Fe(II) at pH 6.5 to 7.5: the most reliable process is cascade aeration (raising DO to above 7 mg per L) followed by dual-media gravity filtration (sand-anthracite, 0.8 to 1.2 mm effective size, 1.5 m bed depth). This achieves iron below 0.05 mg per L at hydraulic loading 5 to 8 m per hr. For pH below 6.5 where aeration oxidation is slow: add lime or sodium carbonate to raise pH to 7.5 before filtration. For high-iron water above 10 mg per L: consider pre-settling (20 to 30 minute contact time in aeration tank before filtration) to reduce filter loading. For small rural supplies: greensand pressure filters with potassium permanganate (KMnO4) regeneration provide a compact, effective solution requiring less civil engineering than a cascade aerator and gravity filter.
Does iron removal also remove manganese?
Iron and manganese co-occur in groundwater but require different conditions for removal. Fe(II) oxidises rapidly at pH above 7 in the presence of dissolved oxygen (half-life minutes at pH 7.5, DO 7 mg per L). Mn(II) oxidises much more slowly: at pH 7.5 and DO 7 mg per L, half-life is hours to days. For manganese removal by aeration alone, pH 9 to 10 is needed, which is impractical for potable water. Effective manganese removal uses: (1) Chlorination to 1 to 2 mg per L free residual, which oxidises Mn(II) to MnO2 within 1 to 5 minutes and allows removal by filtration; (2) Potassium permanganate oxidation (0.5 to 1 mg per L KMnO4 for Mn below 1 mg per L); (3) Biological manganese removal using MnO2-coated filter media where bacteria catalyse the oxidation - effective, chemical-free, and increasingly used in Europe; (4) Ozonation (0.5 to 1 mg per L O3, rapid and effective). Greensand filters (manganese-dioxide-coated) with continuous KMnO4 dosing achieve both iron and manganese removal in a single media.
Is high iron water dangerous to health?
Iron is not considered acutely toxic to humans and has no WHO health-based guideline for drinking water; the WHO 0.3 mg per L value and EU 0.2 mg per L parametric value are aesthetic/operational standards (preventing discolouration, taste, and laundry staining), not health limits. However: (1) High iron promotes biofilm growth in distribution systems by providing an energy source for iron-oxidising bacteria (Gallionella, Leptothrix), which can contribute to discolouration, taste, odour, and nitrification problems; (2) Very high iron concentrations (above 5 mg per L) impart significant metallic taste and astringency making water unpalatable; (3) Iron deposits in distribution systems reduce pipe capacity and provide attachment surfaces for pathogenic organisms; (4) In industrial applications (boiler feedwater, process water), even 0.05 mg per L iron causes equipment fouling, so treatment to below 0.01 mg per L is standard in high-purity water systems.
A small rural water supply in Lincolnshire serving 3,200 properties from a Triassic sandstone borehole experienced persistent iron discolouration complaints: 120 to 140 complaints per month, iron levels at the tap measuring 0.4 to 1.2 mg per L against a regulatory limit of 0.2 mg per L. The existing pressure filtration plant had inadequate aeration and undersized filter beds.
Installed a cascade aerator (6-tray stepped cascade, residence time 4 minutes, achieving DO above 8 mg per L) followed by two dual-media gravity filters (sand-anthracite, 1.5 m bed depth, 5 m per hr hydraulic loading) with automated backwash on differential pressure trigger. Lime dosing (20 mg per L as Ca(OH)2) raised pH from 6.8 to 7.6, improving oxidation kinetics. Added potassium permanganate dosing (0.2 mg per L) as a supplementary oxidant for peak iron periods.
Iron at the treatment works output fell consistently below 0.05 mg per L within 6 weeks of commissioning. Customer discolouration complaints reduced from 130 per month to fewer than 5 per month. DWI regulatory sampling confirmed compliance with the 0.2 mg per L parametric value at all 12 regulatory compliance points across the supply zone. The asset has operated without unplanned shutdowns for 36 months.
Questions to Ask Shortlisted Providers
- 1
Is the iron in our water present as dissolved ferrous Fe(II) only, or as organically complexed iron, and has treatability testing confirmed which process is required?
Simple aerated gravity filtration achieves below 0.05 mg per L for dissolved Fe(II) at pH above 7. Organically complexed iron (indicated by coloured, turbid raw water with high TOC) does not respond to aeration and filtration alone. Coagulation, ozonation, or catalytic media may be required. Specifying the wrong process based on assumed iron form will result in a plant that fails to meet the DWI standard. A jar test or pilot plant run is the minimum required before design finalisation.
- 2
What is the design hydraulic loading rate for the filters, and is it consistent with achieving below 0.05 mg per L iron in the product water at peak flow?
Iron removal filter performance degrades at high hydraulic loading (above 8 to 10 m per hr), and short-circuit flow through cracked or channelled media prevents adequate contact time. A filter designed at 12 m per hr to minimise capital cost will fail to meet the iron standard at peak flow, resulting in DWI-reportable exceedances. Confirm the design loading rate and ask for evidence of performance at that rate from similar installations.
- 3
What is the backwash design, and how are backwash water volumes and filter cake solids managed?
Iron removal filters produce iron hydroxide sludge in the backwash water (typically 3 to 5 percent of throughput). If backwash supernatant is recycled to the head of the works without a settled sludge removal system, accumulated iron hydroxide floc increases the iron loading on the filters beyond design capacity. A lamella settler or thickener for backwash solids separation, and a sludge dewatering and disposal route for iron hydroxide cake, must be included in the design.
- 4
Does the raw water contain manganese as well as iron, and if so, what additional oxidation step is proposed for manganese removal?
Manganese co-occurs with iron in many UK groundwaters. The EU DWD 2020 parametric value for manganese is 0.05 mg per L (stricter than the previous 0.05 mg per L limit from 2004). Manganese does not oxidise at the pH and DO conditions that suffice for iron removal. Additional oxidation (permanganate, chlorination, ozonation, or biological manganese) must be specifically designed for manganese removal. A proposal that addresses iron but not manganese will fail to achieve DWI compliance if both are present.
- 5
What monitoring is included for process control and DWI compliance, and how will the plant respond automatically to an iron breakthrough event before water leaves the treatment works?
DWI requires reporting of individual sample exceedances of the 0.2 mg per L parametric value. A plant without online iron monitoring (photometric or turbidity-based proxy) on the filtered water outlet relies on laboratory samples (24 to 48 hour turnaround) to detect breakthrough. By the time a sample failure is identified, non-compliant water has already been supplied. Online iron monitoring with automated diversion to waste or return to head of works is the standard for iron removal plants serving above 1,000 properties.
What Drives Cost in This Category
A simple aeration plus gravity filtration plant for dissolved iron below 5 mg per L at 500 m3 per day costs 100,000 to 300,000 GBP in equipment and installation. Organically complexed iron requiring coagulation or ozonation at the same flow costs 300,000 to 700,000 GBP. Very high iron concentrations (above 10 mg per L) require pre-settling tanks before filtration, adding 50,000 to 150,000 GBP to capital cost.
Groundwater with pH below 6.5 requires lime or soda ash addition to raise pH to 7.5 to 8.0 before filtration. Lime dosing equipment (saturator, metering pump, lime storage silo for 25 tonnes) costs 20,000 to 60,000 GBP in capital. Annual lime consumption for a 500 m3 per day plant at pH 6.8 inlet: approximately 3 to 5 tonnes of lime at 100 to 150 GBP per tonne. Carbon dioxide stripping (packed tower) avoids chemical dosing at sites where high dissolved CO2 is the cause of low pH.
Iron removal filters produce 0.5 to 3 m3 of iron hydroxide sludge per day (at 2 to 5 percent dry solids) from backwash settled solids. Disposal as non-hazardous solid waste to licensed landfill or land application: 50 to 120 GBP per tonne wet weight. A filter press or centrifuge for sludge dewatering (capital 30,000 to 100,000 GBP) reduces disposal volume 3 to 5 times and is economically justified for plants above 2,000 m3 per day.
DWI water quality sampling requirements for an iron problem supply zone include more frequent compliance monitoring (weekly rather than monthly) until compliance is restored. Laboratory analysis of weekly iron samples: 20 to 50 GBP per sample, 1,000 to 2,500 GBP per year per zone. Online photometric iron monitors (5,000 to 25,000 GBP per instrument, 2,000 to 5,000 GBP per year maintenance) provide continuous data and enable immediate response to exceedances, more than paying for themselves in avoided DWI enforcement costs and consumer complaint handling.
Key Regulations & Standards
WS(WQ)R 2016 (as amended 2018 and 2021 to implement EU DWD revisions) sets the parametric value for iron in drinking water at 200 micrograms per L (0.2 mg per L) in England. Water undertakers must ensure water at the point of supply (customer tap) complies with this value. DWI audit sampling at consumer taps provides regulatory evidence; exceedances trigger DWI investigation and may require a Regulation 28 undertaking from the water company to investigate and remedy the cause.
Under WS(WQ)R 2016 Regulation 28, DWI can serve an undertaking requiring a water company to take specific remedial action following repeated non-compliance with iron or other parametric values. Undertakings specify the works required (e.g. install iron removal plant), the timescale for completion, and interim measures (flushing, temporary treatment). Failure to comply with an undertaking is an offence under the Regulations and can lead to prosecution with unlimited fines.
BS EN 15975-2 provides guidance on risk assessment for drinking water supply systems. Iron removal plant failures (aeration system breakdown, filter media breakthrough, sludge carryover) represent a quality risk to the supply. Risk assessments under BS EN 15975-2 are required for significant treatment processes including iron removal, identifying the hazardous events, their likelihood, and the control measures required. This standard supports the Water Safety Plan approach recommended by WHO and DWI.
Chemicals and materials used in drinking water iron removal treatment must be approved for use in contact with drinking water. WRAS (Water Regulations Advisory Scheme) approval, or DWI List of Approved Products (Regulation 31 approval) is required for: coagulants (aluminium sulphate, ferric sulphate), filter media (sand, anthracite, greensand, manganese dioxide coated media), pH correction chemicals (lime, sodium carbonate), and oxidants (potassium permanganate, chlorine). Use of non-approved products risks DWI enforcement action.