Treatment systems optimization for the sewage water.
Alexandrescu, Aurora
1. INTRODUCTION
Investigations on organic and inorganic water pollutants have had a
significant impact on environmental sciences by providing reliable
knowledge on inputs and environmental exposure in such a way that risk
assessments can be performed. Especially important have been the
development of chemical analytical techniques, which allow qualitative
identifications and quantitative determinations of trace concentrations
in aqueous and solid samples. A large number of environmental
contaminants have been studied regarding their fate and behaviour in the
environment, (Bate, 2006). The paper describes the influence filtration
methods about water's quality. It is distinguished the capacity of
some polymer mixtures of different types to react on a lot of quality
parameters of water. It is presented a comparison between the retaining
efficiency of the organic substances and organic carbon after clarifying
step, respectively of filtration on quartz sand stratum. It is analysed
the reduction efficiency of organic filling case usage of polymers
mixture. The indicator's allowance depends of technology type used
in the treatment process, (Chapra et. al., 1997).
The application's advanced coagulation requires process
modifications for the water plants. These modifications can improve the
disinfection at pH reduced, but can make big slush quantities. The
experimental researches concerning the optimization of the
coagulation--flocculation process allowance following problems:
1. The influence of the water quality on the reagent type of
coagulation.
2. The regent type's influence concerning abeyances abstention efficiency and organic substances for different sources.
3. The improvement of the coagulation process with different
coagulants (through polymers). The coagulation tests are effectuated in
laboratory and pilot installations. The specific polymers for the
drinkable water's treatment and the polymers obtained through
irradiation with electrons and microwaves have been tested. Aluminium
sulphate is used like polymer admixture.
4. The pH's influence on the coagulation process. The
coagulation tests have used aluminium sulphate and ferric chloride.
The advanced coagulation represents the reduction process of the
natural organic substances in the water's treatment channel. It is
a correlation between the three-halo-methane and the total organic
carbon concentration from brute water. The coagulation adjuvants are
natural or synthesis substances used for the improvement of the
coagulation process's performance, (getting of big flakes). The
coagulation adjuvants doses may be established through
coagulation--flocculation tests and tests on slush. The spell between
the coagulant's injection and coagulation adjuvant's injection
is very important. It is efficient as the polymers to be injected after
what the micro-flocculation phase is fully. The water's composition
and the temperature influence this spell. It is considered a particle j
situated in the origin of co-ordinates system and liquid debit from a
sphere of [R.sub.j] = [R.sub.i]+ [R.sub.j] radius. Speed gradient is
equable. The collisions number [N.sub.i] with central particle j is,
(for [n.sub.i] particles of i dimension on volume unity):
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII]. (1)
Equation (1) may be written depending on the particles diameter
[d.sub.i] [d.sub.j] and the speed gradient dv / dz = [bar.G].
Smoluchowski equation for the kinetic stage supposes that each
collisions carries at flakes formation; the particles are destabilized.
If y is net electrostatics potential energy, then d[psi]/dr is
electrostatics force that acts on particles, at r distance against j
central particle. Equation (2) is bringing; the limit conditions are
following: n = [n.sub.o] for r = [infinity] and n = 0 for r = 2R. It is
obtained mathematical relation, ([D.sub.[infinity]] = [D.sub.i] +
[D.sub.j]):
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII]. (2)
2. EXPERIMENTAL RESULTS
The experimental determinations are effectuated at Chirita Iasi
water plant. The measures for the establishment of the optimum
coagulation conditions are make obvious through experimentation. Maximum
efficiency of coagulation's achievement is determined by the
substances and concentrations used. The powder active coal is necessary
to dose correct in the optimization process of the
coagulation--flocculation, because of the pesticides presence in water.
It is obtaining the biologically steady water. The water treatment with
elevated content of sulphide hydrogen requires an oxidation process for
the transformation in colloidal sulphur; it is removed the sulphur
through clarifying process, (Liu et al., 2009). The experimentation is
effectuated on ground water with ammonium and hydrogen sulphate content.
The oxidation is realized through the usage of sodium hypochlorite. It
is analysed the possibility of removal of the sulphides and the hydrogen
sulphate through oxidation and filtration with quartz sand, respectively
hyper filtration. It is following the improvement of the oxidised
water's clarifying process through coagulation process. The
coagulation process's efficiency grows through usage of
flocculants; it is obtained slush volumes lesser, (Suthers & Rissik,
2009).
It is analysed the water's quality from Prut river in the
Tutora section. It is found the following properties:
1. The water has big variations of turbulence and is feeble
colored.
2. pH is in the alkalescent domain (8,06 / 8,16) pH units; the
total alkalinity is (3 / 3,5) mechiv/l.
3. The mineralization indicators (fixed residue and conductivity)
have values adequate to the mineralised average water; the
mineralization is given by the bicarbonates and the calcium sulphates.
4. The concentration of organic substances is established with
potassium permanganate in the interval (10 / 26) mg/l K Mn O4. The
concentration of organic substances is established with potassium
bi-chromium in the interval (12 / 15) mg/l O2. These values may conduct
at difficulties in the water's treatment.
The pesticides concentration from water has excelled many times (5
/ 10) times the accepted concentration for drinkable water, (Hatzinger
et al., 2009). It is used a treatment channel with following processes:
1. Oxidation with Cl[O.sub.2] and ozone. Advanced coagulation with
ferric chlorides (14,5 mg/l) and brute water acidifying with 2,5 % HCl
solution, (18,5 mg/l).
2. Clarifying in clarifying tank with concentrated dynamical
stratum at hydraulic attempts [i.sub.h] = 4 m/h. Castigation pH with
lime water, (dozes of 28 mg/l).
3. Quick filtration on quartz sand stratum. The seeming filtration
speed is [V.sub.f] = 6 m/h. Post--oxidation with ozone (1 mg O3/l) after
quick filtration on sand. Filtration on granular active coal with
seeming filtration speed [v.sub.f] =5 m/h and time t = 8 min. Final
disinfection with sodium hypochlorite, (dozes chlorine 1 mg/l).
It is tested water sources with aluminium sulphate and ferrous
chloride at (6 / 6,5) pH. It is ascertained the reduction of turbulence
and organic substances' oxidation. The usage of the ferrous
chloride reduces organic loading, particularly at oxidable hard organic
substances. The coagulation--flocculation tests make obvious the
water's aggressiveness growth through treatment. The castigations
with lime water eliminate the aggressiveness effect of water. Also grow
up the total organic carbon quantity with (30 / 40) %. After organic
substance' removal may be corrected pH. It is necessary lime dozes
between (8 / 10) mg CaO/l.
Figure 1 present the concentration's variation of total
organic carbon depending on pH for lime water treatment from Chirita
treatment station. The polymers conduct at different efficiency all
over: turbulence and organic loading. It is used polymers mixtures for
coagulation--flocculation treatment in laboratory. The best behaviour
has been the mixture c. Polymer optimum dose is 0,2 mg/l, (figure 2).
The experimentation in laboratory has used simple polymers and polymers
mixtures. Some polymers mixtures have acted simultaneous about several
quality parameters of water.
[FIGURE 1 OMITTED]
[FIGURE 2 OMITTED]
3. CONCLUSIONS
The studies concerning the water's treatment in Chirita
treatment station make obvious the following conclusions:
1. Te water source present treatment difficulties because of
elevated concentration of organic substances; concentration of total
organic carbon is (10 / 18) mg C/l. Removal maximum efficiency of the
organic loading through advanced coagulation is obtained with ferric
chloride (5 / 7) mg [Fe.sup.3+]/l and reduced pH (6 / 6,5). It is
necessary to use powder active coal for the coagulation--flocculation
optimum process. The water's treatment with ozone and granular
active coal establish good qualities, in the limit imposed by the
standard.
2. Sulphide hydrogen may be eliminated with 100 % efficiency using
filtration and oxidation with chloride. The filtration process on sand
has not good efficiency; it is not drinkable water. It is necessary the
coagulation--flocculation and clarifying process. It is recommended the
clarifying tank with (4 / 5) m/h and sedimentation time of 1 h. The
nitrogen may be eliminated through treatment with chlorine. The filtered
water on diaphragm has the standard qualities.
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