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AKV - DEFERUM for Non-Reagent Removal of High Iron SELF-BACKWASHING SYSTEM
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Flow rate, m 3 /day |
Diameter Height Length x Width x Height |
Top height of piping |
Note |
10 |
Diameter 0.75 m . Н =1.5 m . |
2.1 m . |
The system has a filtrate collector V =0.35 m 3 |
100 |
Diameter 1.1 m. Н=2.5 m. |
4.8 m .or 3.8m. |
Filtrate discharge is at the height of 2.40 m . |
500 |
Diameter 3.0 m. Н=2.5 m. or 3.4 3 m. |
5.8 m . or 4.0 m. |
The system has a filtrate collector V= 8 m 3 |
1 000 |
- |
5.8 m . or 4.0 m. |
Two systems of 500 m 3 /day |
5 000 |
Diameter 2.3 m. Н= 2 , 5 m. |
4.8 m . or 3.8m. |
Five filters, 1000 m 3 /day |
10 000 |
Diameter 2.3 m. Н= 2 , 5 m. |
4.8 m . or 3.8 m. |
Ten filters, 1000 m 3 /day |
20 000 |
Diameter 7.3 m. Н= 4 , 0 m. |
5.8 m .. |
Two filters, 10000 m 3 /day |
45 000 |
Diameter 9.0 m. Н= 4 , 0 m. . |
5.8 m . |
Three filters, 15000 m 3 /day |
Parameters |
Value |
Note |
Operating personnel |
- |
Systems of up to 2000 m 3 /day do not require an operator |
Mode of operation |
Continuous / periodic |
The system can be stopped for several hours a day |
Feed water pressure in front of the system at ground level, PSI ((MPa) |
65 (0.45) |
Bore pump should be selected for optimum operation |
Consumption of water for backwash, % of the daily flow capacity |
0.80 or 0.10 |
Depending on the initial concentrations of contaminants |
Duration of backwash, seconds |
180 |
Depending on the quality of filtrate after backwash |
Oxidants for ions and organics |
- |
Atmospheric oxygen, bacteria. In exceptional cases use of reagents. |
Automatic operation controls and filtrate quality controls |
- |
Hydroautomatic. In special cases – use of reagent dosing devices, pH monitoring probes, ion monitoring probes. |
Average energy consumption by a bore pump, kW / m 3 |
0.19 or 0.050 |
In some cases, where levels of dissolved gases are extremely high, a recycling pump for non-reagent raise of pH may consume additional electricity by aerator/degasifier. |
Operating cost is only the cost of electricity consumed by the bore pump to supply feed water to the system at 65 PSI and in some cases by a recycling pump. USD /m 3 |
Approx. 0.010 |
Based on USA and Australian costs |
Fabrication materials |
- |
Choice of plastic or steel for the body and pipes; polymer floating media and stainless steel mesh. |
System location |
- |
Suitable for both indoors and outdoors. |
Ground water characteristics
Parameters |
Unit |
Permissible levels |
Note |
Ions of two-valent iron |
mg/l |
From 0.30 to 75 |
Any forms of iron are removed |
Ions of two-valent manganese |
mg/l |
From 0.05 to 7 |
Oxidants: Atmospheric oxygen, catalyst, bacteria or reagent |
рН |
- |
From 5.4 to 8,2 |
рН of feed water can be raised without chemical reagents by using aerators/degasifiers. |
Hydrocarbonates |
mg/l |
From 30 to 500 |
Alkalinity of feed water can be raised by using natural minerals |
Hydrogen sulphide |
mg/l |
From 0.030 to 9.0 |
Removed by aerator/degasifier |
Free carbon dioxide |
mg/l |
Up to 300 |
Removed by aerator/degasifier |
Radon |
pCi / L |
From 60 to 1000000 |
Removed by aerator/degasifier |
Suspended and colloidal particles |
mg/l |
From 1.5 to 120 |
Removed by filter |
Water temperature |
о С |
From 4 to 40 deg. |
Water temperature may be raised by 0,5 up to 6 deg. if aerators/degasifiers operate in the recycling regimen. |
Quality of filtrate
Parameters |
Unit |
Achievable results |
Note |
Total iron |
mg/l |
Less than: from 0 . 0 to 0.30 |
Results achieved in 2 – 7 days after system commissioning |
Manganese |
mg/l |
Less than: from 0.05 to 0.10 |
Use combination “Deferum / Demagnum” |
рН |
- |
From 6.7 to 7.8 |
Results achieved in 2 – 7 days after system commissioning |
Hydrocarbonates |
mg/l |
Optimum level for system non-reagent operation |
- |
Hydrogen sulphide |
mg/l |
Less than 0,0 0 30 |
Results achieved in 2 – 7 days after system commissioning |
Carbon dioxide (corrodes steel and concrete) |
- |
Stability index From - 0.1 to +.0.1 |
Results achieved in 2 – 7 days after system commissioning |
Radon |
pCi / L |
Less than: 60 |
Results achieved in 2 – 7 days after system commissioning |
Suspended and colloidal particles |
mg/l |
Less than 1.5 |
Results achieved in 2 – 7 days after system commissioning |
Water temperature |
о С |
- |
Results achieved in 2 – 7 days after system commissioning |
Redox potential |
mV |
From +5 0 to +15 0 |
Results achieved in 2 – 7 days after system commissioning |
Technological solutions and their specifics
The system design is common for all flow-rates. However, individual systems may vary in configuration or add-ons depending on the quality of initial water and/or customer’s requirements.
The customers are requested to complete our questionnaire and the provided answers enable us to design a system that would provide a tailored solution to customer’s needs.
Photo gallery:

500 m 3/day “DEFERUM” system installed at “Coca-Cola” Beverages in Belarus.
The system is comprised of five standard 100 m 3/day systems arranged in a modular parallel set-up to suit customer’s space considerations.

Backwash

100 m 3/day combined “DEFERUM” and “DEMAGNUM” systems for the removal of 75 mg/l of iron and 4.2 mg/l of manganese from groundwater and non-reagent pH correction at one of the largest barramundi fish farms in NSW, Australia.
P arameter |
Ground water |
Treated water |
pH |
5.5 |
6.7 (7.3*) |
Iron |
75 mg/l |
0.0 mg/l |
Manganese |
4.2 mg/l |
0.05 mg/l |
* Optional additional aeration/degassing of treated water
Batch production : f rom 100 to 4 00 m 3/day “DEFERUM” system (ID1.50 m. HT=2.50 m.) for the removal of iron from groundwater in Australia.
Economic indicators:
Cost price of water from Deferum (without amortization Deferum) :
U* = N . C 1 + [(C 2 + C 3 + C 4 + C 5)/Q], USD/m 3
where,
N - consumption of electrical power for purification of water, e.g. 0.19 KW/m 3
C 1 - cost of electrical power, e.g. 0.05 USD/KW
C 2 - cost of reactants, e.g. 0.00 USD/year
C 3 - salary to the attendants, e.g. 0.00 USD/year
C 4 - maintenance service costs of Deferum, e.g. 0.00 USD/year
C 5 - other costs (sediment, transport, payment for the water drain, fines, etc.), e.g. 0.00 USD/year
Q - output, m 3/year
The costs of the customer on purification of water (minimum):
E = Q . U* = 0.010 Q , USD/year
Our contractual cost for Deferum:
C = M + t . D ; USD
where,
M - material costs for manufacturing DEFERUM ( ours or the customer) ; USD
t - our spent time for fulfillment of the agreement, days
D - our cost of time for fulfillment of the agreement, it is (taxes+ salary+ profit) or cash, USD/day
Cost price of water for our customer (with amortization of Deferum, e.g. L = 5 years):
U = U* + [C/(Q . L)] = 0.010 + [C/(Q . 5)] , USD/m 3
where,
L - amortization of Deferum, years.
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Please contact us for information about additional systems and services, or if you are ready to place an order. Remember, we can make arrangements for virtually any water treatment application - all you have to do is ask!
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