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AKV - DEFERUM for Non-Reagent Removal of High Iron

SELF-BACKWASHING SYSTEM
FOR THE PURIFICATION
AND STABILIZATION
OF GROUND WATER

The hydro-automatic system “DEFERUM” is designed for the non-reagent removal of high levels of dissolved iron (up to 75 mg/l), dissolved gases (hydrogen sulphide, carbon dioxide, methane, radon, etc), suspended and colloidal particles to drinking water standards. The “DEFERUM” is equally suitable for the removal of very high , moderate and low concentrations of contaminants.

The “DEFERUM” system also provides some partial removal of manganese. However, the targeted manganese removal can be provided by the “DEMAGNUM” system – a modification of “DEFERUM”.

The “DEFERUM” system can also be used as a pre-treatment stage before other conventional applications such as Reverse Osmosis, Ion-Exchange, micro-filtration, etc.

The “DEFERUM” is the most economical, effective and environment-friendly ground water treatment system on a market place. It is currently produced under licence in the USA, Australia, Russia, Ukraine and Belarus.

Cost for polymer floating media: approx $250.00 USD/m 3.

The “DEFERUM” system has the following advantages:

  • No chemical reagents are used in the process
  • The system is very inexpensive and easy to fabricate from only a few types of materials
  • The system does not require an operator
  • Very low failure factor due to absence of mechanical or electrical devices
  • Very low maintenance
  • Combined continuous removal of iron, dissolved gasses, suspended solids and turbidity
  • The system operation self-adapts to changing contaminant loadings
  • A very small amount of water is required for backwash
  • No electricity consumed in the process
  • No moving or rotating parts are used in the process
  • No electronic devices are used in the process
  • No valves are used in the process
  • No parts or elements to be replaced on a regular basis
  • No sheltering required in all weather conditions
  • Filtering media has a life-span of over 25 years
  • The plant is extremely resilient to physical mishandling
  • Backwash function is based entirely on gravity force and difference of water levels
  • The filter backwash is self-regulating
  • No specialised equipment is required for the construction of the plant
  • Quick construction and commissioning
  • Affordability

The “DEFERUM” system can be designed for flow rates ranging from 7.2 m 3/day to over 100,000 m 3/day. The principle technological design is the same for all flow rate ranges.

The “DEFERUM” system is comprised of an advanced AKV aerator/degasifier , a hydro-automatic floating filter and a hydro-robot.

The system configuration may slightly vary depending on the flow rate: for example, a 500 m 3/day system comprises two aerators/degasifiers, two hydro-automatic floating filters, two hydro-automatic backwash units (hydro-robots), a filtrate collector and a backwash water collector.

Technological process:

Feed water is pumped from the borehole and supplied at 65 PSI (0.45 MPa) to the aerator-degasifier (1) where dissolved gasses are removed from water and atmospheric air oxidizes bivalent iron and partially ions of manganese.

Further, feed water flows down the hydro-robot (2) and through the distribution system (3) arrives into the hydro-automatic filter with floating filtering media (4) where impurity particles are arrested throughout the depth of the filtering bed.

After filtration, treated water gravity-flows into a filtrate collector via the discharge pipe (6), and delivery pump forwards purified water to consumption.

As fouling of the filter increases, the water level in the hydro-robot rises, causing the filter to switch into backwash mode. Purified water from the above-filter section (5) drops down and expands the filtering bed, washing out the accumulated impurities. When the water level in the above-filter section drops down to a pre-set point (pre-set during commissioning), the hydro-robot stops the backwash and switches the filter into a new filtration cycle.

Backwash water is gravity discharged from the system and disposed of or additionally treated according to customer’s requirements.

Technical specifications of the “ Deferum ”system

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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