When making the treatment of water dispersed systems by outward magnetic field, precession
of individual electron shells and polarization of electron clouds in molecules occurs.
So, the latter gains induced magnetic moment anti-parallel to outside magnetic field.
Against the backdrop of these developments, the energy of hydrogen bonding undergoes changes.
The bonds are "bent" and partially broken which causes re-alignment of molecules and, therefore,
alterations of water structure. This also brings about changes in density, surface tension,
viscosity and other water properties when treated by magnetic field.
Polarization of electron clouds intensifies as the strength of magnetic field outside grows.
At the same time, deformations in hydrogen bonds go up with a larger amount of molecules,
which have shifted from the equilibrium state in the lattice points out to fill the voids.
As a result, the density of water builds up.
Naturally, the magnetic field deforms, first and foremost, weaker and "long" bonds.
A relative number of strong bonds between water molecules increase. The kinetic energy
of water molecule oscillations near temporary equilibrium at magnetic treatment does not
change (constant temperature). A rise in the relative amount of strong bonds between molecules
causes reduction of ionic water product. However, the structure formed during motion in
magnetic field cannot be stable. On exiting the scope of magnetic field, this structure
tends to regain its former condition that shows a minimum of energy and a maximum of hydrogen
bonds between molecules in specific environment.
Distillated water has equal molecules and, consequently, observed differences of physical
properties prior to and following magnetic treatment are quite insignificant and depend
weakly OJH the magnetic field strength. Adding salts and rising charged ions upsets the
water structure to a greater extent as the solution concentration thickens. In this case,
the cation force fields pull the electron pairs away from the nearest water molecule oxygen,
which results in an additional layer of eight electrons around the cations. In other words,
free electric levels in the cations are filled making the latter more or less bonded with
water molecules, which reside next to the ion (close hydration). The structure of water
molecules is tampered with not only in the adjacent layers but also in those next to the
hydrated ion owing to polarization.
Water structure changes set off by addition of dissolved substances (impurities) can be
of different degree and are dependent upon the value and nature of charge distribution
in ions (particles), their sizes, configuration and other reasons. Impurities enter the
voids of the water hexagonal cage with stabilizing or destroying effects subject to the
size of additives. That is why both the structure and properties of water dispersed systems
hinge upon the nature of dispersed phase, concentration, temperature, etc.
When magnetic field is applied from outside, water dispersed systems have precession of
individual shells of the particles present in the water. It also initiates polarization
of electron clouds in water molecules. However, unlike pure water with nearly same precession
in identical atoms because of equality of all molecules, identical atoms do not precede
at the same interval in solutions. This is caused by diversified polarization of molecules
by ion electric fields. There is also a different shift of electric shells of water molecules
that envelop the ions.
By varying the density of electron clouds of both ions and water molecules, magnetic field
alters the structure of water dispersed systems, interaction energy between ions and water
molecules around the ions, close hydration and molecular polarization in the layers abutting
on the ions (remote hydration). By and large, magnetic field changes the structure of water-dispersed
system to a certain degree.
Hence it follows that outward magnetic field has a particular impact on the ion hydration.
The latter is the major factor that determines the condition of phase separation boundaries
and structural transformations in a water dispersed system.
Magnetic field is known to create the asymmetry of hydrated shells due to its effects
on water molecules situated around the ion (near and far). Likewise, magnetic field weakens
the bonds between certain ions with subsequent bonding amplification of others. These changes
result in conditions for ionic associates or crystal embryos. The reversal of magnetic flux
and, consequently, modified direction of ion movements greatly facilitate the formation
of ion pairs and more sophisticated aggregates. This can be attributed to a higher probability
of attracting particles to close with one another.
The theory of magnetic field impact on technological processes for water treatment falls
into two main chapters: crystallization at magnetic water preparation and impurity coagulation
in water systems.
Crystallization is the formation of crystals when a substance enters a transition phase
from less stable thermodynamic state into more steadfast condition.
Equal chemical potentials are the principal consideration for thermodynamic phase equilibrium:
xk = xc, (3)
where,
xk - substance potential in crystalline condition;
xc - same substance potential in solution.
Equilibrium departure is the thermodynamic driving force of crystallization. When xc - xk > 0,
there is a crystal formation and growth. For xc - xk < 0, decrystallization occurs.
A number of crystalline aggregates formed per unit of volume/time shall be computed with
the following equation:
 |
, (4) |
given that,
- density of atoms in a crystal;
- a number of particles in embryo's surface layer;
Z - probability of adding one particle to the crystal embryo per unit of time;
n - a number of particles in embryo's surface layer;
A - height of potential barrier to be cleared by the system for formation of viable embryo;
K - Boltzmann's constant;
T - absolute temperature.
For spherical embryo:
 |
, (5) |
given that,
- specific volume per one particle in a crystal;
- specific free energy of separation surface.
Solution supersaturation is a prerequisite for crystallization. A crystallization embryo
is the outcome of phase transformations.
The following requirements are to be matched to secure spontaneous crystallization in a
supersaturated solution:
1. Local enhanced concentration of substance molecules or ions with little kinetic energy.
2. The order of molecules or ions in compliance with their positions in the crystal lattice
of a crystallized substance.
Given appropriate conditions, it may be expected that molecules or ions clash and set up
short chains or flat molecular layers. Once the attractive force exceeds the one of repulsion,
a crystal embryo is generated as an elementary particle of solids. The stability of a particle
is directly related to its size. For the size in excess of the critical one, the expenditure
of energy for the particle to grow would be at the lowest and in the process of constant
enlargement. In case of the size less than the critical dimensions, destruction is most
likely to take place. As a rule, the following pattern is observed: the more supersaturation,
the less activity involved in generation of a critical embryo, the smaller embryo size and
faster rates of formation. The speed of embryo birth is an exponential function of supersaturation
degree, which vanishes at:
 |
, (6) |
The crystallization rate is positively affected by exposure to microgroups of a new phase,
which accelerate their growth to the size of stable embryos. The embryo birth and crystallization
degree also depend on electric interaction between particles when the work required for
embryo formation can be significantly reduced.
Magnetic field causes formation of crystal microembryos in supersaturated aqueous solutions
and, therefore, influences immensely the nature of crystallization. In this particular
case, the embryos are more plentiful in number and are of smaller sizes than those in the
solutions untreated by magnetic field. Furthermore, magnetic field will shorten a magnetic
period of crystallization and will allow for an earlier isolation of solid phase. These
changes are predominantly linked to the direct impact of magnetic field on impurity ions.
The forces acting on the ions of unlike charges are opposite in direction and will induce
opposite ion motions when the aqueous solution is in transit of magnetic field.
The radius of ion movement around the force lines of magnetic field is subject to the ion
weight and the Lorentz force. At the same time, the radius of ion orbit is dependent upon
the magnetic field strength and the velocity of water solution passing through it.
In some cases, the radius is small enough to set off ion fluctuation. For instance, at
the magnetic field strength H = 80 kA/m and the flow rate 1-3 m/s the circumference radius
of calcium and sulphate ions are ~0/17 and ~0.04 mcm, respectively.
Despite negligible action of the Lorentz force, there is quite a considerable change in
the nature of ion movement whereas the fluctuation of ion concentration caused by the latter
is fairly noticeable. The distribution of ion concentration along the cross-section of the
flow perpendicular to magnetic force lines can be defined by the equation:
 |
, (7) |
given that,
C - concentration of ions;
- electric conductivity of solution;
Bo - magnetic field induction;
k - constant;
- mean velocity of solution movement;
Ha - Hartman number;

- viscosity of solution;
z - coordinate of the field direction;
a - flow half-width.
The edges of magnetic field present the highest probability for ion associations. It happens
due to severe nonuniformity of magnetic field in its marginal areas, which favours the
wave formation and the travel of ions in the direction of wave propagation. In the meantime,
there will be electric field oscillations in the boundary conjugates that are likely to
lead to additional fluctuations of ion concentration.
Direct effects of magnetic field on impurity ions in the water cause changes in the structure
of the water system proper.
In particular, magnetic field facilitates an activation hurdle and makes it easier to yield
calcium hexaqua complexes [Ca(OH2O)5]2+ and large meta-stable
complexes {[Ca(H20)5]20H20}2+.
Stabilization of clustered water structures by a calcium hexaqua complex with application
of magnetic field promotes the formation of extra crystallization centres in the water.
Short of hexaqua complex instability, its existence is rather long. The degree of order
of water structures influenced by magnetic field reduces remote ion hydration and, hence,
has a favourable impact on adsorption, coagulation, etc.
Coagulation may proceed much faster if there is a hard surface in the solution since the
energy required for crystal growth is much less than that needed for the birth of embryo
in the solution. Crystallization takes place on the crystal surface of any given or isomorphous
substance as long as the surface is capable of adsorbing the molecules or ions present in
the solution. Initially, there is an adsorptive layer, which gradually builds up and, ultimately,
turns into a layer of the crystalline substance.
Silica particles (for readily soluble salts) and ferrous compounds, which occur in the
water as colloids are used to seed crystallization in the water when magnetic treatment
is applied. Colloidal'particles of ferromagnetic iron oxides, such as magnetites, present
in the water may coagulate by the action of both magnetic attraction and pandemotor forces
that speed up mutual attraction of the particles. Newly bom particles of the size in excess
of crystal particles will adsorb molecules or ions from the solution and serve as a basis
for crystallization.
Colloidal centers may be activated by magnetic field with subsequent effects on the growth
kinetics of hardness salt crystals. It has been found now that this phenomenon is a polyextreme
function of magnetic field strength and an extreme function of water flow rate. Besides,
it has also been established that after magnetic treatment of calcium bicarbonate solution,
the formation of crystallization centers is more active than under usual crystallization
conditions.
Coagulation is the adherence of particles to one another in dispersed systems and, especially,
colloidal dispersion. This process reduces particles of a dispersed system and increases
their weight. Coagulation happens under the action of molecular forces on collision of
particles as a result of Brownian motion or some exterior factors. Coagulation may proceed
in the form of aggregates shaped by particle coalescence and aggregate flake-like sedimentation
or gel, a solid coagulation structure. The rate of coagulation may be calculated by the equation:
dn / dt = K · n2, (8)
given that,
n - a number of particles per volume unit;
K - coagulation constant.
The coagulation constant of spherical particles of various values is defined by the formula:
 |
, (9) |
given that,
r1, r2 - radius of coagulating particles;
A - number factor depending on the properties of particle surface;
L - length of particle's free run;
k - Boltzmann's constant;
T - absolute temperature.
The equation analysis shows that K grows significantly as the particle radius ratio goes up.
This is why the particles vanish rapidly in heavily polydispersed medium.
The coalescence of particles suspended in the water hinges upon the rate of hydration and
the value ofelectrokinetic potential on the surface of particles.
The coagulation of particles depends immensely on the wetting changes of their hard surface,
which are caused by magnetic field.
Magnetic treatment of water affects its wetting capacity of solid surfaces owing to changed
interaction patterns of water molecules as it has been mentioned before. This "pushes"
the water molecules off the surface. The benefits of water magnetic treatment are also
attributive to altered adsorption of individual ions on the surface. Therefore, the surface
charge undergoes changes too.
Improved wetting of hard surfaces after magnetic treatment of water enhances coagulation
of suspended particles and increases aggregate instability of suspensions.
The findings of amplified aggregate suspension instability resulted from magnetic treatment
are in perfect harmony with the data on adhesion enhancement of solid particles in condensed
systems (sediments).
The formation of easy-to-precipitate floes with developed surfaces within the shortest
possible time is of special interest to the water treatment practice. Such flakes ensure
quick separation of heterogeneous systems. One of the commonly used technological methods
to intensify the coagulation for water treatment is injection of chemical agents such as
active silicic acid into the clarified water. However, in many cases it entails considerable
consumption of the reactant. At the same time, the coagulant activity may be remarkably
strengthened when treating the water solution of coagulant by magnetic field. In this case,
it can be inferred from the mechanism of magnetic field impact on aqueous solutions that
ionic salt associations are raised in the coagulant solution due to weakened ion hydration
and some other factors caused by the positioning of outside magnetic field. Ionic associates
existing in the aqueous solution may work as coagulation centres.
Ferromagnetic particles (iron ions) always present in different numbers in the treated
water can have a certain influence on crystallization during magnetic water treatment.
The research has shown that during magnetic treatment of water, aggregation of ferromagnetic
particles emerges and accelerates the crystallization. In addition, the agglomerates of
ferromagnetic particles get a coating of calcium carbonate, which can also become a crystallization
centre.
Any method of water treatment pursues the general object of isolating insoluble contaminants
through coalescence and fusion. The sedimentation of species is regarded as a mass process
that changes in time.
Qualitative and quantitative indicators of sedimentation are greatly determined by the
process kinetics, which imply the nature of velocity changes and the mechanism for separation
of particles in time.
Fig. 2. |
With a considerably lengthy sedimentation time, the separation zones do not vanish completely.
This can be attributed to statistical factors and, primarily, collisions of particles,
flow discontinuity along them, etc. Hence, the pattern for fraction distribution of various
density is of statistical nature.
Wastewater is a relatively rough suspension, which contains fine and colloidal species.
The water contains dissolved electrolytes and, therefore, suspended fine particles carry
same electric charges that repel one another, Fine colloidal particles suspended in the
water are on the constant move and resemble the Brownian motion.
Several zones emerge some time later following the start of solid sedimentation in the
wastewater (Fig. 2).
The lower part has the sediments of large particles that settle in the first place at the
highest rate of precipitation. |
Zone 4 houses a stratum of thickened sediments with particles situated at the closest
range to one another, which stops any further sedimentation. The pressure of the above-lying
strata continuously compresses this section. It should be noted that part of water is gradually
squeezed upwards, which makes it possible to consolidate the given layer.
Zone 3 is a transition sector. Here the particles are steadily thickened in a downward
direction. Zone 2 has the water with fine-dispersed suspensions. This water is very similar
to the source wastewater in terms of composition without large species, which have settled
before. Finally, Zone 1 contains clarified water.
According to the above-mentioned information, compounds and ions present in the water have
certain magnetic properties characterized by magnetic susceptibility that defines the capacity
of ions and compounds to change their magnetic moment once magnetic field is applied from
outside. Augmentation of magnetic susceptibility will enhance the magnetization of particles,
induced moment and will, ultimately, better interaction between the particles. Such a process
intensifies the coagulation of particles in Zone 3, which will consequently consolidate
the species in Zone 4 and press additional clarified water out to Zone 1.
Operational experience of magnetic systems at various sewage plants has shown that the
quantity of quickly settling particles (Im/s and above) during magnetic treatment nearly
doubles. Likewise, the concentration of sediments in the suspended layer advances by 1.2-1.5
times. This will allow the convenience of increasing the capacity of sewage facilities.
2. Feasibility Studies for Adaptation of Magnetic Technologies at
IndahWater Pilot Plants in Malaysia
According to the information submitted by IndahWater, it is understood that all Malaysian
sewage plants fall into 4 categories:
1. Communal Septic Tanks (CST).
2. Imhoff Tanks (IT).
3. Oxidation Ponds with Pump Station (OPPS).
4. Extended Aeration Plants (EA).
Based on the available papers, it can be concluded that the diversity of sewage plants
in Malaysia calls for individual technical solutions to customize and adapt magnetic
systems to the existing facilities.
2.1. Communal Septic Tank
CST is a two-chamber settler with horizontal hydraulic flow. In the first chamber solids
from the incoming sewage settle to the bottom and form a "sludge blanket". This necessitates
magnetic treatment of the sewage water as early as at the first stage. The magnetic application
will intensify the separation process of a heterogeneous system such as the wastewater.
The partially clarified sewage proceeds to the second chamber for further sedimentation
where it also should be exposed to magnetic treatment. This will facilitate coalescence
and flocculation of the particles present in the water and will shorten the formation period
of large flakes, which precipitate with ease. Finally, dissolved solids will also settle
due to accelerated crystallization.
Thus, the magnetic techniques will secure a higher purity treatment of the wastewater,
which will inevitably lower both the biological oxygen demand and total dissolved solids
by 50-60% and 35-40%, respectively.
However, installation of magnetic systems online at the inlet to the CST is not expedient,
for the sewage water entering the CST does not go through mechanical treatment. Therefore,
it will be necessary to frequently remove the systems for cleaning, which will considerably
push up the operational expenses and depreciate the operational safety of the CST. In the
light of these challenges, the following options are the most acceptable for magnetic
treatment of the incoming CST wastewater:
1. Installation of magnetic systems on the centralized water supply pipeline inlet of a
residential house to treat the flow in passing (Fig. 3).
2. Installation of strap-on magnetic systems on the sewage outlet pipe of every residential
house (Fig. 3).
Implementation of the first scheme will produce the results that are presented below:
the operational lifetime of housing pipelines is extended by 2-3 times due to significant
reduction of deposit build-ups,
a corrosive action of the sewage water on the iron slides down by 30-50%. That will prolong
the service life time of housing pipelines,
the probability of clogging sewer pipes declines because of better solubility of the
magnetized water,
collection of fine fractions improves by 15-25%,
the rate of sludge sedimentation in the second CST chamber accelerates by 25%,
the rate of suspension settlement inside the CST goes up by 1.4-2.6 times
there is a 28-60% reduction of the suspended solids in the water on the CST outlet.
Almost the same advantages except for the first three will be obtained when carrying out
the activities related to the second option.
To sum up, the first choice is the most attractive one for a complex approach towards the
sewage problem.
Fig. 3. |
2.2. Imhoff Tank
The IT design provides for installation of a slot magnetic system at IT entrance (Fig. 4).
The following benefits can be secured:
the rate of solid sedimentation accelerates by 1.5-2 times,
collection of fine fractions improves by an average of 20%,
dissolved solids in the clarified water decrease by 15-25%,
biological oxygen demand goes down by 10-15%,
sludge digestion time reduces by 30%,
the probability of blocking the tank filter drops nearly two-fold.
2.3. Oxidation Pond with Pump Station
According to the charts attached to your technical papers, the sewage water undergoes
mechanical treatment and then is pumped to the sedimentation cell via the Parshall flume.
Partially clarified water moves to a system that comprises oxidation ponds to reduce the
organic matter and pathogenic bacteria. However, the efficiency of such a pattern for
wastewater treatment is essentially dependent upon climatic surroundings and weather conditions.
To lessen the dependency, it is necessary to diminish the organics that proceed with the
water to the ponds. Towards this end, magnetic aeration of the water flow to the Parshall
flume is required, on the one hand, and special magnetic field needs to be applied to the
water flow passing through a narrow cross-section of the flume, on the other (Fig. 5).
Magnetic aeration of the water stream will substantially enhance floatation and once combined
with magnetic treatment of the water in the flume will greatly improve the isolation of
organic substances from the water in the sedimentation cell. The complex treatment is also
likely to immensely reduce the pathogens in the ponds.
Any further reduction of the organic matter comes about in the first pond by way of aerobic
fermentation. Fermentation is known to imply chemical reactions fuelled by certain microorganisms
including bacteria with their vital role in the process. The bacteria affect impurities,
which work as a nutritional medium. Synthesized bacteria sustain chemical reactions and
serve as catalysts for them. Thus, the fermentation process is based on building a bacterial
culture. The growth of bacteria slows down once the conditions turn unfavourable. One of
the main reasons for growth inhibition or cessation is accumulation of toxic metabolic
products or environmental changes. Magnetic treatment alters the water structure and,
therefore, maintains best conditions for the removal of hydrogen sulphide and CO2 from
the water. This will appreciably curtail the digestion time for the organic matter.
Heading from this, the suggested technical solution will secure the following results:
the rate of solid sedimentation accelerates by 1.5-2 times,
fermentation period oforganics dwindles roughly by 30%,
dissolved solids in the water go down by an average of 20%,
biological oxygen demand lowers by 10-15%,
consolidation of sediments and the dry substance output advances by 5-6%,
pathogens decline approximately by 10 times.
Application of magnetic technologies at oxidation ponds with pump stations makes it possible
to increase the productive throughput by 40%.
2.4. Extended Aeration Plant
An extended aeration plant is a typical sewage facility to treat wastewater and consists
of a primary treatment section, an aeration tank, a sludge-settling tank with sludge recirculation
system, an aerobic digestion tank and a sludge holding tank.
To achieve the ultimate goal, i.e. reduction of dissolved solids in the treated sewage
water as well as the biological oxygen demand, it is necessary to install magnetic systems
at the following points (Fig. 6):
1. Before aeration tank
To intensify floatation through consolidation of air bubbles in the magnetic field with
subsequent particle coalescence.
2. Before sludge settling tank
To additionally enhance destabilization of the water dispersed system, which will speed
up flocculation and, therefore, almost halve the sedimentation time with a subsequent 5-6%
increase in the dry matter output.
3. Before aerobic digestion tank
To quicken the growth of bacterial culture, which will shorten the fermentation time nearly
by 1.4 times.
4. Before sludge holding tank
To intensify the phase separation or, namely, accelerate the sludge dewatering process.
Taking into account the above-mentioned improvements, complex installation of our systems
will allow the convenience of the benefits as specified below:
reduction of dissolved solids by 15-17%,
a drop in the biological oxygen demand by 8-10%,
an increase in the capacity by 30-65%.
The proposed adaptation of magnetic systems will entail one-time payment with no additional
electricity expenses. Another important thing about the systems is that they are maintenance-free.
3. Magnetic Systems for Water Treatment at IndahWater Sewage Plants
A thorough analysis of the Malaysian sewage plants based on your engineering specifications
has shown that the Communal Septic Tank is the hardest part for magnetic treatment of the
wastewater for the reason of technical implementation. Nonetheless, a complex approach,
as we have mentioned before, which includes installation of magnetic systems on the central
water supply pipe of residential houses will make it possible to solve the main problem
and will substantially extend the operational lifetime ofexisting pipelines.
Below is given an outer tracing of the three proposed magnetic devices. All the units for
the aforesaid purpose will have a similar design with flanges, which can be made to fit
the diameters at installation points (Fig. 7).
The table below includes the specification details of the three magnetic systems.
| # |
Description |
Unit |
System#1 |
System#2 |
System#3 |
| 1 |
Unit code |
- |
Ut-1 |
Ut-2 |
Ut-3 |
| 2 |
Flange inside diameter |
mm |
250 |
100 |
50 |
| 3 |
Unit length |
mm |
500-700 |
500-700 |
500-700 |
| 4 |
Pressure limit |
bar |
6 |
6 |
6 |
| 5 |
Flow capacity |
m3/hr |
180 |
40 |
28 |
| 6 |
Temperature limit |
°C |
90 |
90 |
90 |
The detailed sketches of magnetic systems suggested for installation at the CST, Imhoff tank,
oxidation pond and extended aeration plant are shown in Fig. 8, 9, 10, 11.
| # |
Place of Installation |
Qty. |
A, mm |
B, mm |
C, mm |
D, mm |
| 1 |
After Pump Station (with flange) |
2 |
500 |
50 |
500 |
250 |
| 2 |
After Aeration Tank (with flange) |
2 |
500 |
50 |
500 |
250 |
| 3 |
After Settling Tank |
1 |
120 |
40 |
500 |
112.5 |
| 4 |
After Sludge Digester Tank |
1 |
350 |
50 |
500 |
175 |
4. Warranty
Magnetic Technologies L.L.C. guarantees to provide full-service and necessary replacement
of equipment due to technical faults for the duration of 18 months from the date of commissioning.
The probability of trouble-free operation is 0.999973.
No side or negative effects are associated with magnetic treatment of water.
5. Monitoring System
Both parties should undertake operational efficiency monitoring of the systems according
to the following procedure.
1. Make at least 20 tests of TDS (mg/l) and BOD (mg/1) at the discharge point of each sewage
facility prior to installation of magnetic systems.
2. Define average values of the measured parameters.
3. Compile a joint report on the results obtained.
4. Follow Step 1 and Step 2 after installation of magnetic systems.
5. Compute the operational efficiency of magnetic systems by the formula:
E = (K0- Km) x 100% / K0
given that,
E - operational efficiency of magnetic systems,
Ko - an average value of TDS or BOD before installation of
magnetic systems,
Km - an average value of TDS or BOD after installation of magnetic systems,
In case of significant fluctuations in weather conditions before and after installation
of magnetic systems the formula-computed value shall be divided by the empirical factor of O.85.
6. File a joint evaluation report on operational efficiency of magnetic systems.
6. Offer for Installation of Magnetic Systems
6.1. Magnetic Systems for Residential Houses and Industrial Premises
| # |
Particulars |
Price, USD |
| 1 |
QUADRO- 3/4" |
110.00 |
| 2 |
QUADRO-1" |
110.00 |
| 3 |
QUADRO-1.5" |
192.00 |
| 4 |
QUADRO-2" |
685.00 |
| 5 |
QUADRO-3" |
1,370.00 |
| 6 |
QUADRO-4" |
4,110.00 |
| 7 |
QUADRO-6" |
5,205.00 |
| 8 |
QUADRO-8" |
7,671.00 |
| 9 |
QUADRO-10" |
8,767.00 |
| 10 |
QUADRO-12" |
9,589.00 |
| 11 |
QUADRO-14" |
13,425.00 |
6.2. Communal Septic Tank (PJA 006)
Details of equipment
1 (one) UT device (option 1) - necessary female flanges, nuts, bolts and brackets
1 (one) specially designed device (option 2)
Installation - by your technical staff under combined supervision
Cost of equipment - USD 15,000-20,000
6.3 Imhoff Tank (KLR 004)
Details of equipment
1 (one) special magnetic system - necessary fastening pieces
Installation - by your technical staff under combined supervision
Cost of equipment - USD 25,000
6.4. Oxidation Pond (KLR 035)
Details of equipment
1 (one) special device with injector - necessary fastening pieces
Installation - by your technical staff under combined supervision
Cost of equipment - USD 45,000
6.5 Extended Aeration Plant (HLT 034)
Details of equipment
4 (four) magnetic systems - necessary fastening pieces
Installation - by your technical staff under combined supervision
Cost of equipment - USD 250,000
7. Conclusion
The technical proposal presented herein includes brief information on enhancement of natural
and wastewater treatment and describes the mechanism of magnetic field effects on the condition
of water dispersed systems. This will enable the customer to visualize near and long-term outlook.
A self-contained design of individual systems ensures highly reliable functioning with
the trouble-free operation probability being 0.999973. The feasibility study for adaptation
of magnetic systems and guaranteed designs serve as an indication of viability and capacity
of the given proposal to make IndahWater the first major enterprise in Malaysia to capitalize
on the latest magnetic technologies.
Our experience and expertise in implementation of similar projects is underpinned by efficient
functioning of our systems at sewage plants in various regions of the erstwhile Soviet
Union and by the results of experiments carried out at the sewage plants in Dubai, United
Arab Emirates and Cairo, Egypt. There is a multitude of sewage facilities in the C.I.S.
that have availed themselves of magnetic systems. This is just to name a few:
1. Sewage Plant in Kharkov, Ukraine.
2. Sewage Plant at the Phosphorite Factory in Bryansk, Russia.
3. Heat Power Station in Polotsk, Belarus.
4. Heat Power Station in Togliatti, Russia.
5. Sewage Plant in Kramatorsk, Ukraine.
6. Sewage Plant in Cherkassy, Ukraine.
7. Sewage Plant in Dnepropetrovsk (Lomovsk district), Ukraine.
8. Sewage Plant in Aulsk Ukraine.
9. Sewage Plant in Belaya Tserkov, Ukraine.
8. Recommendations of Magnetic Technologies L.L.C. Commission of Experts
Taking into consideration the particularities of sewage plants in your country such as
a great number, low technological level and a scattered nature of sparsely populated areas,
we believe that our proposal embodies the most expedient one from the engineering, economical
and medical standpoint. It involves installation of magnetic systems on all main pipelines,
which feed drinking and industrial water to dwelling houses and industrial enterprises alike.
Our equipment will dramatically change the ecological situation at large and will significantly
reduce the population morbidity rate. So, it will help you solve the problems that you
are facing on an every day scale.
Furthermore, the method presented herein is the most economical and inexpensive without
peer among all the currently available solving models.
Attached are some decrees passed by the Healthcare Ministry of the former Soviet Union,
which dwell on the effects that magnetic water has on the human body.