01773 521437

Sales & Customer Support

Mon - Fri: 9:00 - 17:00

Online store always open

Hydrox Iron & Manganese Removal Filter

Price range: £552.00 through £16,386.00

Hyrolox can be used for iron and manganese reduction by oxidation. Like Filox the pH needs to be controlled and there needs to be oxygen present. Hydrox can tolerate chlorine.

Derived from a naturally occurring manganese compound, HYDROX is commonly employed for catalytic removal of iron and manganese in both potable and mineral water processing. Thanks to its elevated reactive surface, it efficiently supports the oxidation of these metals especially in oxygen-rich environments leading to the generation of insoluble metal hydroxides that can be
readily captured through standard filtration.

HYDROX can be applied either as a standalone filtration layer or positioned at the base of a dual-media filter, substituting traditional gravel or quartz sand. It may also be used in a blended bed configuration with quartz, depending on system design.
When handling raw water with elevated iron levels, it is advisable to include a generously sized upper filtration layer. This top section traps most of the iron content, preserving the catalytic action of the lower manganese-selective layer. Due to its resistance to dissolved CO₂, HYDROX consistently removes manganese even under mildly acidic conditions (typically above pH 6.8). In many cases, this eliminates the need for pH correction prior to treatment.

Features

Backwashing procedure
The backwashing of HYDROX should be executed with air / water separately. A combined backwash cannot be recommended due to an increased abrasion of HYDROX. Before starting the backwash with air the water level has to be lowered to a few centimeters
above the filter material surface to avoid unexpected loss of filter material.

1) 1 - 3 minutes air approx. 60 m/h

2) 1 - 2 minutes pause

3) 4 - 8 minutes water approx. 55 m/h

Following the initial aeration phase, a rest period of approximately 2 minutes is advised to allow proper degassing of the filter media and support plate. During the backwash cycle, it is recommended to replace the filter volume at least twice to ensure effective cleaning. A backwash flow rate of around 55 meters per hour is typically required to achieve a bed expansion of roughly 10–15%.
If the outcome of the water backwash is inadequate, simply increasing the backwash duration will not improve performance. Instead, a full repetition of the cleaning cycle is recommended, following this sequence:
Lower the water level → perform air scouring → allow a brief pause → proceed with water backwash.

- +
SKU N/A Categories ,
ValveVesselMedia Volumn KgMax Declorination FlowBackwash Flow
Clack WS1 TC10"50Kg1.5m³/hr2m³/hr
Clack WS1 Cl 10"50Kg1.5m³/hr2m³/hr
Clack WS1 Cl 12"75Kg2.0m³/hr2.5m³/hr
Clack WS1 Cl 13"100Kg2.5m³/hr3m³/hr
Clack WS1 Cl 14"150Kg3m³/hr3.5m³/hr
Clack WS1 Cl16"200Kg3.7m³/hr4.6m³/hr
Clack WS1.25 Cl18"250Kg4.5m³/hr5.7m³/hr
Clack WS1.5 P Cl18"250Kg4.5m³/hr5.7m³/hr
Clack WS1.5 P Cl21"300Kg6.4m³/hr7.9m³/hr
Clack WS2 P Cl21"300Kg6.4m³/hr7.9m³/hr
Clack WS2 P Cl24"400Kg9m³/hr11m³/hr
Clack WS2 P Cl 30"550Kg15m³/hr18m³/hr
2 HF Top Mount36"32 Bags20m³/hr25m³/hr
2 HF Side Mounr36"32 Bags20m³/hr25m³/hr
WS3 Side Mount 42"1100Kg28m³/hr35m³/hr
WS3 Side Mount48"1600Kg38m³/hr48m³/hr