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IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 288
COMPARATIVE STUDY ON PERFORMANCE OF COAGULANTS IN
WATER TREATMENT
B.G. Mahendra1
, Madhusudhan C2
1
Associate Professor, 2
M.Tech Scholar, Department of Civil Engineering, Poojya Doddappa Appa College of
Engineering, Gulbarga-585102, Karnataka
bgm_pda@yahoo.co.in, masc1942@gmail.com
Abstract
The study on the performance of different coagulants in water treatment was carried out using coagulants such as alum(C1), Poly
aluminium chloride(PAC)(C2) and sodium aluminate(C3). The performance was studied with respect to turbidity removal,
concentration of residual aluminium and comparative cost of coagulants for treatment of Bhima river water. The performances of
these coagulants were studied separately as well as mixture of two coagulants in equal proportions. C1 and C2 were mixed to get
coagulant mixture (CM1), C1 and C3 were mixed to get CM2, C2 and C3 were mixed to get CM3. The study reviews that the
coagulants C1 and CM3 were found to be more efficient with 100% removal of turbidity at turbidities up to 50 NTU. For higher
turbidities above 50 NTU, the coagulants C1, C2 and CM1 are found to be more efficient with 100% turbidity removal. The
concentration of residual aluminium is found to be less in CM1 and C2. For turbidities of 200 NTU and 400 NTU with optimum
dosages, the concentrations were 0.02mg/L and 0.04mg/L for CM1 respectively.
Keywords: Coagulants, turbidity, residual aluminium.
---------------------------------------------------------------------***------------------------------------------------------------------------
1. INTRODUCTION
The primary source of water is precipitation, which may be
available in the form of surface water and ground water.
Surface water sources available on the ground are streams,
rivers, lakes etc. These sources should have adequate flow of
water to be considered as a reliable source of water supply for
a town or city. Surface waters generally contain suspended
and colloidal solids from land erosion, decaying vegetation,
micro-organisms etc. Coarser materials, such as sand and silt,
can be eliminated to a considerable extent by plain
sedimentation, but finer particles of colloidal must be
chemically coagulated to produce larger floc that is removable
by subsequent settling and filtration. This treatment of water is
very important as polluted water is the main cause for many
diseases and may be even worse in spreading an epidemic.
Coagulation is the first process of treatment given to the water
in which the chemical compounds called as coagulants are
added. The chemistry of coagulation/flocculation consists of
three processes - flash mix, coagulation, and flocculation as
explained below:-
Flash mixing: - In the flash mixer, coagulant chemicals are
added to the water and the water is mixed quickly and
violently. The purpose of this step is to evenly distribute the
chemicals through the water. Flash mixing typically lasts a
minute or less. If the water is mixed for less than thirty
seconds, then the chemicals will not be properly mixed into
the water. However, if the water is mixed for more than sixty
seconds, then the mixer blades will shear the newly forming
floc back into small particles.
Coagulation: - After flash mixing, coagulation occurs. During
coagulation, the coagulant chemicals neutralize the electrical
charges of the fine particles in the water, allowing the particles
to come closer together and form large clumps.
Flocculation: - The final step is flocculation. During
flocculation, a process of gentle mixing brings the fine
particles formed by coagulation into contact with each other.
Flocculation typically lasts for about thirty to forty-five
minutes. The flocculation basin often has a number of
compartments with decreasing mixing speeds as the water
advances through the basin. This compartmentalized chamber
allows increasingly large floc to form without being broken
apart by the mixing blades.
1.1 Objectives of the Study
This study has been carried out in the environmental
engineering laboratory, civil engineering department of P. D.
A college of engineering, Gulbarga, from September-2012 to
November-2012 with the following objectives:-
(i) To study the characteristics of Bhima river water.
(ii) To determine the optimum dosage for each
coagulant.
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 289
(iii)To study the performance of each coagulant with
its optimum dosage and to compare the performance
of each coagulant with respect to turbidity removal,
residual aluminium and cost of coagulant for
treatment
(iv)To study the efficiency of treatment with the
combination of two coagulants mixed in equal
proportions.
2. MATERIALS AND METHODOLOGY
The water samples were collected from Bhima river near the
intake structure which is located near the village Saradgi,
approximately 16 kms from Gulbarga. The water samples
were tested for the characteristics considered as important in
coagulation process. Grab sampling technique was adopted to
collect the water samples. The materials or aluminium based
coagulants used in this study are :-
1) Alum (aluminium sulfate) [Al2(So4)3.18H2O] (C1)
2) Poly aluminium chloride (PAC)[Al12Cl12(OH)24] (C2)
3) Sodium aluminate (NaAlO2) (C3)
The below given parameters are considered for studying the
performance of coagulants:-
1) Optimum dosage(Turbidity removal)
2) Optimum pH
3) Residual aluminium and
4) Cost.
1) Optimum Dosage: Jar tester is used for this test in
optimizing the amount of dosage required. Six number of jars
were placed and different concentrations of coagulants were
added to each beaker. 500ml±5ml were taken in each beaker
of 1L capacity. The dosing was done without much time
difference between the beakers. The paddles of the rotor were
maintained at same height for all the beakers. After starting,
the flocculator were rotated at a greater speed of 100 rpm for
about 2 minutes and were brought down to about 30 rpm and
was maintained for 20 minutes. The rotor was stopped and the
settling was observed after 20 minutes. Flocs size were
observed with naked eye and for turbidity measurement, the
sample was pipette out keeping the pipette approximately 2
cms below the surface of sample, then measured on
nephelometer.
Coagulant solution: A coagulant solution was prepared by
weighing each coagulant to 10 grams and diluting it to 1 litre
with distilled water, so that 1ml of coagulant solution contains
10mg of coagulant. For a mixture of two coagulants, each
coagulant is weighed to 5 grams and mixed together and
diluted to 1 litre using distilled water.
2) The wholesome water used for drinking and domestic
purpose should have a pH in the range of 6.5 to 8.5, which is
also the allowable limit. The pH of the sample was adjusted
from 5 to 10 with an interval of 1.0, and was placed in 6
beakers. From jar tests, dosage concentration which imparted
0(zero) turbidity was noted and the same is used with varying
pH for each jar. The jar test is repeated and the turbidity is
measured and least turbidity yielding pH is noted and is
considered the optimum pH for the type of coagulant added.
This test was carried on water of turbidity 200 NTU with its
respective optimum dosage concentration for each coagulant
as in table – 3.
3) Residual aluminium: The test was carried on water samples
of 200 NTU and 400 NTU with optimum dosage yielding least
turbidity respectively.With Eriochrome cyanine R dye, dilute
aluminum solutions buffered to a pH of 6.0 produce a red to
pink complex that exhibits maximum absorption at 535 nm.
To compensate for colour and turbidity, the aluminum in one
portion of sample is complexed with EDTA to provide a
blank. The interference of iron and manganese, two elements
commonly found in water when aluminum is present, is
eliminated by ascorbic acid.
4) Cost: The cost of treatment for each coagulant is based on
the quantity of coagulant required to treat 1 million litre of
water with turbidity of 200 NTU and 400 NTU.
3. RESULTS AND DISCUSSIONS
The characteristics of water sample such as pH, total solids,
alkalinity and turbidity were tested and are given in table – 1.
Table1. Characteristics of water samples collected near the intake structure.
Sample no.
Characteristics
pH Total solids, mg/L Alkalinity, mg/L Turbidity, NTU
1 6.92 410 28 135
2 7.09 396 30 132
3 7.00 453 26 141
4 7.16 512 34 159
5 7.29 498 34 155
6 7.42 560 35 168
7 7.31 489 35 156
8 7.52 518 35 162
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 290
9 7.39 546 33 165
10 7.48 540 32 165
11 7.35 512 33 160
12 7.43 521 32 160
Mean 7.28 496.25 32.25 154.83
The water sample collected from the river was tested on the
same day of collection so as to get consistency in the
characteristics of the sample. The optimum dosage of
coagulant for different turbidities was studied using the jar test
apparatus. The turbidity of the clear water after jar tests were
found out with the help of nephelometer. The results of water
samples having turbidities 50 NTU, 100 NTU, 200 NTU
and 400 NTU with their efficiency of turbidity removal and
cost of coagulant are tabulated in tables – 2. Optimum dosage
results are shown in figures – 1 to 4.
Table2 Optimum dosage and cost of coagulants for treating 1 million litres of river water
Coagulant
50 NTU 100 NTU 200 NTU 400 NTU
Qty
in
Kgs
Cost
in
Rs
E
in
%
Qty
in
Kgs
Cost
in
Rs
E
in
%
Qty
in
Kgs
Cost
in
Rs
E
in
%
Qty
in
Kgs
Cost
in
Rs
E
in
%
C1 60 1458 100 120 2916 100 240 5832 100 380 9234 100
C2 40 5400 100 100 13500 100 200 27000 100 340 45900 100
C3 100 11880 98 280 33264 100 460 54648 98 740 87912 99
CM1 40 3186 100 60 4779 100 140 11151 100 260 20709 100
CM2 50 3577 100 160 11448 98 340 24327 100 580 41499 100
CM3 40 2862 100 100 12675 100 240 30456 100 400 50760 100
Fig1. Showing the optimum dosage of Fig2 Showing the optimum dosage of
Coagulants for turbidity of 50 NTU Coagulants for turbidity of 100 NTU
0
10
20
30
40
50
0
10
20
30
40
50
60
70
80
90
100
110
Turbidity,NTU
Coagulant dosage, mg/L
C1
C2
C3
CM1
CM2
CM3
0
10
20
30
40
50
60
70
80
90
100
0 40 80 120 160 200 240 280
Turbidity,NTU
Coagulant dosage, mg/L
C1
C2
C3
CM1
CM2
CM3
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 291
Fig3. Showing the optimum dosage of Fig4 Showing the optimum dosage of
coagulants for turbidity of 200 NTU. coagulants for turbidity of 400 NTU.
Table3. Optimum pH for a turbidity of 200 NTU.
pH
C1
Dosage–240
mg/L
C2
Dosage–420
mg/L
C3
Dosage–460
mg/L
CM1
Dosage–140
mg/L
CM2
Dosage–340
mg/L
CM3
Dosage–240
mg/L
5 01 00 01 00 12 12
6 00 00 04 00 06 04
7 00 00 08 00 01 03
8 00 00 08 00 00 03
9 04 02 09 00 00 02
10 05 02 09 02 01 02
0
50
100
150
200
250 0
140
180
220
260
300
340
380
420
460
500
540
0
50
100
150
200
250
300
350
400
0 260 320 380 440 500 560 620 680 740
Turbidity,NTU
Coagulant dosage, mg/L
C1
C2
C3
CM1
CM2
CM3
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 292
Fig5. Showing the turbidity vs pH results for a turbidity of
200 NTU.
Residual aluminium: The test was carried on water samples of
200 NTU and 400 NTU with optimum dosage yielding least
turbidity. The concentrations of residual aluminium for
optimum dosages is given in table – 4 and shown in figure - 6.
Table4. Residual aluminium concentration with optimum
dosages
Coagulants
Turbidity – 200 NTU Turbidity – 400 NTU
Dosage
mg/L
pH
Al
mg/L
Dosage
mg/L
pH
Al
mg/L
C1 240 7.0 0.07 380 7.0 0.09
C2 200 7.0 0.03 340 7.0 0.05
C3 460 5.0 0.18 740 5.0 0.24
CM1 140 7.0 0.02 260 7.0 0.04
CM2 340 8.0 0.12 580 8.0 0.18
CM3 240 9.0 0.11 400 9.0 0.12
Fig6. Showing the residual aluminium concentration for
turbidity of 200 and 400 NTU
Coagulant CM1 is having the least aluminium concentration in
treated water when coagulated at optimum dosage
concentration for turbidities of 200 and 400 NTU. The
residual aluminium concentration was 0.02 mg/L and 0.04
mg/L with CM1 for turbidities of 200 and 400 NTU
respectively.
Cost: The cost of the alum(C1) is far more lesser than poly
aluminium chloride(C2) and sodium aluminate(C3). The cost
of coagulants is given in the table – 5. The cost per Kg of
coagulant, for CM1, CM2 and CM3 were computed and were
found to be still higher than C1. The quantity and cost of
coagulant for treating 1 million litres(ML) of river water is
summarized in table – 2 and from this summary we can see
that even with least dosage the cost of treatment is high for
coagulants C2, C3, CM2, CM3 and CM1 to that of C1.
Table5. Cost of coagulants per unit weight
Coagulants
Cost per Kg in
Rupees
Alum(C1) 24.3
Poly aluminium
chloride(C2)
135.0
Sodium aluminate(C3) 118.8
Alum + poly aluminium
chloride(CM1)
79.65
Alum + Sodium
aluminate(CM2)
71.55
Poly aluminium chloride +
Sodium aluminate(CM3)
126.9
0
2
4
6
8
10
12
14
5 6 7 8 9 10
Turbidity,NTU
pH
Alum
PAC
SA
Alum+PAC
Alum+SA
PAC+SA
0
0.05
0.1
0.15
0.2
0.25
0.3
C1 C2 C3 CM1CM2CM3
Residualaluminium,mg/L
Coagulants
200 NTU
400 NTU
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 293
CONCLUSIONS
On analyzing the results based on the laboratory experiments
conducted, the following conclusions are drawn.
1) The characteristics of water sample collected from
Bhima river were found to be pH – 7.28, total solids
– 496.25 mg/L, alkalinity – 32.25 mg/L and turbidity
– 155 NTU.
2) Coagulant CM1 is found to be good coagulant for all
the turbidity values with least dosage to remove
100% turbidity.
3) CM1 has the wider range of pH suitability and works
satisfactorily over a pH range of 5.0 to 9.0 over other
coagulants considered for the study.
4) The residual aluminium concentration in treated
water is less when CM1 is used, ie 0.02 and 0.04
mg/L for turbidities 200 and 400 NTU respectively
with optimum dosages.
5) The cost per unit weight of CM1 is less than both C2
and C3, but more than C1. The cost of coagulant
required for treating 1 million litres of water is least
for C1 even with its higher dosage requirement over
CM1.
REFERENCES
[1] APHA, AWWA, Standard Methods for Examination of
Water and Wastewater, 19th
Edition. Prepared and
Published by American Public Health Association,
American Water Works Association, Water Pollution
Control Federation (1995)
[2] Drinking water standards, Bureau of Indian Standards,
IS 10500-1991.
[3] FPSDW- (Federal-Provincial Sub-committee on
Drinking water). 2001. Summary of guidelines for
Canadian drinking water quality.
[4] U.S.EPA- (United States Environmental Protection
Agency). 1999. Enhanced coagulation and enhanced
precipitative softening guidance manual.EPA 815-R-
99-012, 237 p.
[5] WHO (2004). Guidelines for drinking-water quality,
3rd ed., World Health Organization, Geneva.

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Comparative study on performance of coagulants in water treatment

  • 1. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 288 COMPARATIVE STUDY ON PERFORMANCE OF COAGULANTS IN WATER TREATMENT B.G. Mahendra1 , Madhusudhan C2 1 Associate Professor, 2 M.Tech Scholar, Department of Civil Engineering, Poojya Doddappa Appa College of Engineering, Gulbarga-585102, Karnataka bgm_pda@yahoo.co.in, masc1942@gmail.com Abstract The study on the performance of different coagulants in water treatment was carried out using coagulants such as alum(C1), Poly aluminium chloride(PAC)(C2) and sodium aluminate(C3). The performance was studied with respect to turbidity removal, concentration of residual aluminium and comparative cost of coagulants for treatment of Bhima river water. The performances of these coagulants were studied separately as well as mixture of two coagulants in equal proportions. C1 and C2 were mixed to get coagulant mixture (CM1), C1 and C3 were mixed to get CM2, C2 and C3 were mixed to get CM3. The study reviews that the coagulants C1 and CM3 were found to be more efficient with 100% removal of turbidity at turbidities up to 50 NTU. For higher turbidities above 50 NTU, the coagulants C1, C2 and CM1 are found to be more efficient with 100% turbidity removal. The concentration of residual aluminium is found to be less in CM1 and C2. For turbidities of 200 NTU and 400 NTU with optimum dosages, the concentrations were 0.02mg/L and 0.04mg/L for CM1 respectively. Keywords: Coagulants, turbidity, residual aluminium. ---------------------------------------------------------------------***------------------------------------------------------------------------ 1. INTRODUCTION The primary source of water is precipitation, which may be available in the form of surface water and ground water. Surface water sources available on the ground are streams, rivers, lakes etc. These sources should have adequate flow of water to be considered as a reliable source of water supply for a town or city. Surface waters generally contain suspended and colloidal solids from land erosion, decaying vegetation, micro-organisms etc. Coarser materials, such as sand and silt, can be eliminated to a considerable extent by plain sedimentation, but finer particles of colloidal must be chemically coagulated to produce larger floc that is removable by subsequent settling and filtration. This treatment of water is very important as polluted water is the main cause for many diseases and may be even worse in spreading an epidemic. Coagulation is the first process of treatment given to the water in which the chemical compounds called as coagulants are added. The chemistry of coagulation/flocculation consists of three processes - flash mix, coagulation, and flocculation as explained below:- Flash mixing: - In the flash mixer, coagulant chemicals are added to the water and the water is mixed quickly and violently. The purpose of this step is to evenly distribute the chemicals through the water. Flash mixing typically lasts a minute or less. If the water is mixed for less than thirty seconds, then the chemicals will not be properly mixed into the water. However, if the water is mixed for more than sixty seconds, then the mixer blades will shear the newly forming floc back into small particles. Coagulation: - After flash mixing, coagulation occurs. During coagulation, the coagulant chemicals neutralize the electrical charges of the fine particles in the water, allowing the particles to come closer together and form large clumps. Flocculation: - The final step is flocculation. During flocculation, a process of gentle mixing brings the fine particles formed by coagulation into contact with each other. Flocculation typically lasts for about thirty to forty-five minutes. The flocculation basin often has a number of compartments with decreasing mixing speeds as the water advances through the basin. This compartmentalized chamber allows increasingly large floc to form without being broken apart by the mixing blades. 1.1 Objectives of the Study This study has been carried out in the environmental engineering laboratory, civil engineering department of P. D. A college of engineering, Gulbarga, from September-2012 to November-2012 with the following objectives:- (i) To study the characteristics of Bhima river water. (ii) To determine the optimum dosage for each coagulant.
  • 2. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 289 (iii)To study the performance of each coagulant with its optimum dosage and to compare the performance of each coagulant with respect to turbidity removal, residual aluminium and cost of coagulant for treatment (iv)To study the efficiency of treatment with the combination of two coagulants mixed in equal proportions. 2. MATERIALS AND METHODOLOGY The water samples were collected from Bhima river near the intake structure which is located near the village Saradgi, approximately 16 kms from Gulbarga. The water samples were tested for the characteristics considered as important in coagulation process. Grab sampling technique was adopted to collect the water samples. The materials or aluminium based coagulants used in this study are :- 1) Alum (aluminium sulfate) [Al2(So4)3.18H2O] (C1) 2) Poly aluminium chloride (PAC)[Al12Cl12(OH)24] (C2) 3) Sodium aluminate (NaAlO2) (C3) The below given parameters are considered for studying the performance of coagulants:- 1) Optimum dosage(Turbidity removal) 2) Optimum pH 3) Residual aluminium and 4) Cost. 1) Optimum Dosage: Jar tester is used for this test in optimizing the amount of dosage required. Six number of jars were placed and different concentrations of coagulants were added to each beaker. 500ml±5ml were taken in each beaker of 1L capacity. The dosing was done without much time difference between the beakers. The paddles of the rotor were maintained at same height for all the beakers. After starting, the flocculator were rotated at a greater speed of 100 rpm for about 2 minutes and were brought down to about 30 rpm and was maintained for 20 minutes. The rotor was stopped and the settling was observed after 20 minutes. Flocs size were observed with naked eye and for turbidity measurement, the sample was pipette out keeping the pipette approximately 2 cms below the surface of sample, then measured on nephelometer. Coagulant solution: A coagulant solution was prepared by weighing each coagulant to 10 grams and diluting it to 1 litre with distilled water, so that 1ml of coagulant solution contains 10mg of coagulant. For a mixture of two coagulants, each coagulant is weighed to 5 grams and mixed together and diluted to 1 litre using distilled water. 2) The wholesome water used for drinking and domestic purpose should have a pH in the range of 6.5 to 8.5, which is also the allowable limit. The pH of the sample was adjusted from 5 to 10 with an interval of 1.0, and was placed in 6 beakers. From jar tests, dosage concentration which imparted 0(zero) turbidity was noted and the same is used with varying pH for each jar. The jar test is repeated and the turbidity is measured and least turbidity yielding pH is noted and is considered the optimum pH for the type of coagulant added. This test was carried on water of turbidity 200 NTU with its respective optimum dosage concentration for each coagulant as in table – 3. 3) Residual aluminium: The test was carried on water samples of 200 NTU and 400 NTU with optimum dosage yielding least turbidity respectively.With Eriochrome cyanine R dye, dilute aluminum solutions buffered to a pH of 6.0 produce a red to pink complex that exhibits maximum absorption at 535 nm. To compensate for colour and turbidity, the aluminum in one portion of sample is complexed with EDTA to provide a blank. The interference of iron and manganese, two elements commonly found in water when aluminum is present, is eliminated by ascorbic acid. 4) Cost: The cost of treatment for each coagulant is based on the quantity of coagulant required to treat 1 million litre of water with turbidity of 200 NTU and 400 NTU. 3. RESULTS AND DISCUSSIONS The characteristics of water sample such as pH, total solids, alkalinity and turbidity were tested and are given in table – 1. Table1. Characteristics of water samples collected near the intake structure. Sample no. Characteristics pH Total solids, mg/L Alkalinity, mg/L Turbidity, NTU 1 6.92 410 28 135 2 7.09 396 30 132 3 7.00 453 26 141 4 7.16 512 34 159 5 7.29 498 34 155 6 7.42 560 35 168 7 7.31 489 35 156 8 7.52 518 35 162
  • 3. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 290 9 7.39 546 33 165 10 7.48 540 32 165 11 7.35 512 33 160 12 7.43 521 32 160 Mean 7.28 496.25 32.25 154.83 The water sample collected from the river was tested on the same day of collection so as to get consistency in the characteristics of the sample. The optimum dosage of coagulant for different turbidities was studied using the jar test apparatus. The turbidity of the clear water after jar tests were found out with the help of nephelometer. The results of water samples having turbidities 50 NTU, 100 NTU, 200 NTU and 400 NTU with their efficiency of turbidity removal and cost of coagulant are tabulated in tables – 2. Optimum dosage results are shown in figures – 1 to 4. Table2 Optimum dosage and cost of coagulants for treating 1 million litres of river water Coagulant 50 NTU 100 NTU 200 NTU 400 NTU Qty in Kgs Cost in Rs E in % Qty in Kgs Cost in Rs E in % Qty in Kgs Cost in Rs E in % Qty in Kgs Cost in Rs E in % C1 60 1458 100 120 2916 100 240 5832 100 380 9234 100 C2 40 5400 100 100 13500 100 200 27000 100 340 45900 100 C3 100 11880 98 280 33264 100 460 54648 98 740 87912 99 CM1 40 3186 100 60 4779 100 140 11151 100 260 20709 100 CM2 50 3577 100 160 11448 98 340 24327 100 580 41499 100 CM3 40 2862 100 100 12675 100 240 30456 100 400 50760 100 Fig1. Showing the optimum dosage of Fig2 Showing the optimum dosage of Coagulants for turbidity of 50 NTU Coagulants for turbidity of 100 NTU 0 10 20 30 40 50 0 10 20 30 40 50 60 70 80 90 100 110 Turbidity,NTU Coagulant dosage, mg/L C1 C2 C3 CM1 CM2 CM3 0 10 20 30 40 50 60 70 80 90 100 0 40 80 120 160 200 240 280 Turbidity,NTU Coagulant dosage, mg/L C1 C2 C3 CM1 CM2 CM3
  • 4. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 291 Fig3. Showing the optimum dosage of Fig4 Showing the optimum dosage of coagulants for turbidity of 200 NTU. coagulants for turbidity of 400 NTU. Table3. Optimum pH for a turbidity of 200 NTU. pH C1 Dosage–240 mg/L C2 Dosage–420 mg/L C3 Dosage–460 mg/L CM1 Dosage–140 mg/L CM2 Dosage–340 mg/L CM3 Dosage–240 mg/L 5 01 00 01 00 12 12 6 00 00 04 00 06 04 7 00 00 08 00 01 03 8 00 00 08 00 00 03 9 04 02 09 00 00 02 10 05 02 09 02 01 02 0 50 100 150 200 250 0 140 180 220 260 300 340 380 420 460 500 540 0 50 100 150 200 250 300 350 400 0 260 320 380 440 500 560 620 680 740 Turbidity,NTU Coagulant dosage, mg/L C1 C2 C3 CM1 CM2 CM3
  • 5. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 292 Fig5. Showing the turbidity vs pH results for a turbidity of 200 NTU. Residual aluminium: The test was carried on water samples of 200 NTU and 400 NTU with optimum dosage yielding least turbidity. The concentrations of residual aluminium for optimum dosages is given in table – 4 and shown in figure - 6. Table4. Residual aluminium concentration with optimum dosages Coagulants Turbidity – 200 NTU Turbidity – 400 NTU Dosage mg/L pH Al mg/L Dosage mg/L pH Al mg/L C1 240 7.0 0.07 380 7.0 0.09 C2 200 7.0 0.03 340 7.0 0.05 C3 460 5.0 0.18 740 5.0 0.24 CM1 140 7.0 0.02 260 7.0 0.04 CM2 340 8.0 0.12 580 8.0 0.18 CM3 240 9.0 0.11 400 9.0 0.12 Fig6. Showing the residual aluminium concentration for turbidity of 200 and 400 NTU Coagulant CM1 is having the least aluminium concentration in treated water when coagulated at optimum dosage concentration for turbidities of 200 and 400 NTU. The residual aluminium concentration was 0.02 mg/L and 0.04 mg/L with CM1 for turbidities of 200 and 400 NTU respectively. Cost: The cost of the alum(C1) is far more lesser than poly aluminium chloride(C2) and sodium aluminate(C3). The cost of coagulants is given in the table – 5. The cost per Kg of coagulant, for CM1, CM2 and CM3 were computed and were found to be still higher than C1. The quantity and cost of coagulant for treating 1 million litres(ML) of river water is summarized in table – 2 and from this summary we can see that even with least dosage the cost of treatment is high for coagulants C2, C3, CM2, CM3 and CM1 to that of C1. Table5. Cost of coagulants per unit weight Coagulants Cost per Kg in Rupees Alum(C1) 24.3 Poly aluminium chloride(C2) 135.0 Sodium aluminate(C3) 118.8 Alum + poly aluminium chloride(CM1) 79.65 Alum + Sodium aluminate(CM2) 71.55 Poly aluminium chloride + Sodium aluminate(CM3) 126.9 0 2 4 6 8 10 12 14 5 6 7 8 9 10 Turbidity,NTU pH Alum PAC SA Alum+PAC Alum+SA PAC+SA 0 0.05 0.1 0.15 0.2 0.25 0.3 C1 C2 C3 CM1CM2CM3 Residualaluminium,mg/L Coagulants 200 NTU 400 NTU
  • 6. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ IC-RICE Conference Issue | Nov-2013, Available @ http://www.ijret.org 293 CONCLUSIONS On analyzing the results based on the laboratory experiments conducted, the following conclusions are drawn. 1) The characteristics of water sample collected from Bhima river were found to be pH – 7.28, total solids – 496.25 mg/L, alkalinity – 32.25 mg/L and turbidity – 155 NTU. 2) Coagulant CM1 is found to be good coagulant for all the turbidity values with least dosage to remove 100% turbidity. 3) CM1 has the wider range of pH suitability and works satisfactorily over a pH range of 5.0 to 9.0 over other coagulants considered for the study. 4) The residual aluminium concentration in treated water is less when CM1 is used, ie 0.02 and 0.04 mg/L for turbidities 200 and 400 NTU respectively with optimum dosages. 5) The cost per unit weight of CM1 is less than both C2 and C3, but more than C1. The cost of coagulant required for treating 1 million litres of water is least for C1 even with its higher dosage requirement over CM1. REFERENCES [1] APHA, AWWA, Standard Methods for Examination of Water and Wastewater, 19th Edition. Prepared and Published by American Public Health Association, American Water Works Association, Water Pollution Control Federation (1995) [2] Drinking water standards, Bureau of Indian Standards, IS 10500-1991. [3] FPSDW- (Federal-Provincial Sub-committee on Drinking water). 2001. Summary of guidelines for Canadian drinking water quality. [4] U.S.EPA- (United States Environmental Protection Agency). 1999. Enhanced coagulation and enhanced precipitative softening guidance manual.EPA 815-R- 99-012, 237 p. [5] WHO (2004). Guidelines for drinking-water quality, 3rd ed., World Health Organization, Geneva.