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Example of low-concentration iron removal and manganese removal treatment
We will introduce an example of iron removal and manganese removal treatment in groundwater using our filter material.
In order to use the groundwater in Osaka Prefecture as drinking water, iron, manganese, and chromaticity that exceed the tap water quality standards are removed by iron removal and manganese removal towers.
● Raw water quality
item | unit | Numerical value | Tap water standard |
---|---|---|---|
Water species | – | Groundwater | – |
place | – | Osaka prefecture | – |
pH | – | 7.2 | 5.8~8.6 |
iron | mg/L | 1.0 | 0.3 or less |
item | unit | Numerical value | Tap water standard |
---|---|---|---|
manganese | mg/L | 0.24 | 0.05 or less |
Turbidity | degree | 1.3 | 2 or less |
Saturation | degree | 12 | 5以下 |
TOC | mg/L | Less than 0.5 | 3 or less |
Iron in raw water is 1.0 mg / L and manganese is 0.24 mg / L, which are higher than the tap water quality standard. The raw water also contains chromaticity, but the TOC of the raw water is low, and the results of prior tests have revealed that it was colloidal iron hydroxide, so a flocculant was injected. It can be judged that the chromaticity can be removed to 5 degrees or less by performing physical filtration.
We examined the treatment method so that the target values of treated water were iron: 0.3 mg / L or less and manganese: 0.05 mg / L or less, and delivered the equipment for iron removal and manganese removal towers.
The filter medium to be filled in the filter tower has a relatively small load on the filter medium because both iron and manganese have low concentrations, but since a flocculant is injected, anthracite e.s 0.7 mm and manganese-free filter medium ferro It was done with multiple layers of Light MC3. In addition, the main purpose of backwashing the filter is to discharge the turbidity accumulated in the filter tower, but when using a coagulant such as PAC, the purpose is also to loosen the filter material, so one day. It is once.
item | Iron removal / manganese removal tower |
---|---|
Filter | φ2000mm×SH1830mm |
Filtration material filling amount (per tower) | Anthracite e.s0.7mm:1.0m3 FerroliteMC3:2.2m3 |
Filtration rate | LV12.7m/hr |
Chemical injection amount | NaClO: Inject free chlorine into treated water so that 0.5 mg / L is detected. PAC: 5 mg / L injection at the inlet of the filtration tower |
Backwash process | Backwash: LV 30m / hr x 10min Stand still: 3 minutes Filtration drainage: LV 19m / hr x 10min |
Backwash frequency | Once a day |
As a result of delivering the above iron and manganese removal equipment, we were able to obtain extremely clear water as shown in the table below and in the photo by removing iron and manganese.
The chromaticity was also reduced to 1 degree by removing iron. In addition, the turbidity of the raw water was already below the tap water quality standard, but it could be removed to less than 0.2 degrees, and it can be said that very good water was obtained.
item | unit | Filtration tower entrance | Filtration tower exit |
---|---|---|---|
pH | – | 7.2 | 7.3 |
iron | mg/L | 1.0 | Less than 0.01 |
manganese | mg/L | 0.24 | 0.01 |
item | unit | Filtration tower entrance | Filtration tower exit |
---|---|---|---|
Turbidity | degree | 1.3 | Less than 0.2 |
Saturation | degree | 12 | 1 |
Free chlorine | mg/L | 1.0 | 0.6 |
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