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Effect of Water Quality Improvement
in Raw Water Source on WaterTreatment Cost: A Case Study of
West Tarum Canal in Java
Aug 22, 2011
Ibnu Samsi, Myong Jin Yu
UNIVERSITY OF SEOUL
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WTC System and Water Quality Monitoring Points
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West Tarum Canal (WTC)Cibeet, Cikarang and Bekasi River intercepted by WTC.Erosion by deforestration, and discharge of untreated domestic andindustrial wastewater in the basins of three rivers.Deterioration of WTC water quality.
Water Uses of WTCRaw water supply to Water Treatment Plants (16.3m3/sec to Jakarta)IrrigationIndustrial Uses
River Water Classification CLASS I(Gov. Regulation No. 82/2001 concerning water quality management)
Present Water Quality of WTCOut of Class IV based on some parameters, BOD, DO, COD, SS,Fecal Coliform
Introduction
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Parameters Units CLASS I CLASS IV
Temperature C Dev. 3 Dev. 5
TDS mg/L 1000 2000
SS mg/L 50 400
Turbidity NTU -
pH mg/L 6-9 5-9
BOD mg/L 2 12
COD mg/L 10 100
DO mg/L 6 0NH3-N mg/L 0.5 -
NO3-N mg/L 10 20
Fe mg/L 0.3 -
Mn mg/L 0.1 -
Key Water Parameters for WTC
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Turbidity
The most important quality parameter affecting coagulant dose in water
treatment
WHO sets maximum level 5 NTU, 1 NTU for successful disinfection
Less than 0.1 NTU applied to filtered water for removal of Giardia andCryptosporidium
Raw water turbidity ranged from 3 to 28,239 NTU at Buaran WTP
which takes raw water downstream of WTC
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Water Quality Levels at WTC and Crossing Rivers
100908070605040302010099989796959493
30
25
20
15
10
5
0
Year
B
O
D
m
g
/
L
1 Curug
11 Cibeet
12 Cikarang13 Bekasi
9 BTb.51
BOD5levels at the West Tarum Canal and crossing riversduring the period 1993-2010
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Turbidity levels at the West Tarum Canal and crossing riversduring the period 1993-2010
100908070605040302010099989796959493
16000
14000
12000
10000
8000
6000
4000
2000
0
Year
T
u
r
b
i
d
i
y
N
T
U
1 Curug
11 Cibeet
12 Cikarng
13 Bekasi
9 BTb.51
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Raw water turbidity
20000100006000300010005001005010
160
140
120
100
80
60
40
20
0
Turbidity NTU
F
e
q
u
e
n
c
y
000000229
1817
2932
282323
3334
28
34
42
80
115117122122
148141
118
78
110
129
101
57
26
100000
Daily average
3000020000100006000300010005001005010
140
120
100
80
60
40
20
0
T u r b i d i t y NT U
r
e
q
u
e
n
y
113
17
29
37
1617
24
30
16
292526
36
2024
34
53
7574
106
80
112
98
123
135
109
86
107109
90
64
11
1100000
Dai ly max imum
20000100006000300010005001005010
200
150
100
50
0
Turbidity NTU
F
e
q
u
e
n
c
y
0000000000011341
101322
28
4441
60
81
127
153
180
157
171
130
116
102
167
6876
58
13001
Daily minimum
Raw water turbidity frequencies atBuaran WTP
during the period 2006-2010
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Yearly frequencies of raw water turbidity at Buaran WTP
Turbidity, NTUFrequency of
daily average
Frequency of
daily maximum
0 ~ 300 298 253
300 ~ 1000 32 47
1000 ~3000 27 27
3000 ~ 10000 8 23
10000 ~ 14
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BOD5and turbidity along WTC will be comparedin the following conditions.
Present
After Bekasi siphon constructionAfter Bekasi and Cikarang siphon constructionAfter Bekasi and Cibeet siphon constructionAfter Bekasi, Cikarang and Cibeet siphon construction
Results and discussion
Effects of separation of three rivers on water quality of WTC
Bekasi siphon most effective in reducing both BOD5and turbidityCikarang siphon more effective in BOD5 reduction.Cibeet siphon more effective in turbidity reduction.
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Effects of siphons on water qualities at the Buaran WTP intakeusing water quality data during the period 1993-2010
Alternatives
BOD
at Buaran(mg/L)
BOD
reduction(%)
Turbidity
at Buaran(NTU)
Turbidity
reduction(%)
Present 8.22 822.9
Bekasi siphon 6.53 20.5 624.7 24.1
Bekasi &
Cikarang siphon5.70 30.7 504.4 38.7
Bekasi & Cibeet
siphon 6.2 25.0 455.3 44.7
Bekasi, Cikarang
& Cibeet siphon5.26 36.0 304.5 63.0
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Turbidity frequency change at Buaran WTPafter the construction of siphons
Turbidity
range, NTU
Present
frequency
Frequency
after Bekasi
siphon
Frequency
after Bekasi
&Cikarang
siphon
Frequency
after Bekasi
&Cibeet
siphon
Frequency
after Bekasi,
Cikarang &
Cibeet siphon
0 ~ 300 298 314 324 328 340
300 ~ 1000 32 24 20 18 15
1000 ~3000 27 20 17 15 10
3000 ~ 10000 8 6 5 4 0
Improvement of raw water turbidity by separation of three rivers
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Chemicals used for turbidity removal
Chemicals used at the Buaran WTP
Chemical Component Use Unit price
Alum (Liquid) Aluminum sulphate Coagulation $200-400 per ton
PAC Polyaluminium chloride Coagulation $300-320 per ton
Sudfloc A Aluminum chlorohydrate Coagulation $750-800 per tonLT20 Polyacrylamide Coagulation aid $4.99 per kg
LT7994Polydiallyldimethylammonium Chloride
Coagulation aid $4.99 per kg
Lime Calcium hydroxide pH adjustment $90-200 per ton
Chlorine Liquid chlorine Disinfection $100-300 per ton
Daily average, maximum and minimum turbidity.Chemical doses such as alum, PAC, Sudfloc A, LT 20,LT7994, lime and chlorine every two hours.
S O S O
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Relation between daily average turbidityremoved and chemicals used
In general one kind of coagulant such as Alum or PAC is used inmoderately turbid raw water.Extremely high turbidity in high frequency makes purificationprocesses extremely difficult.Therefore, combination of three kinds of coagulant is used tostrengthen the effects of each ones, and either of two kinds of
polyelectrolyte is applied to make dense floc.Turbidity removal was related to the combined action of Alum, PAC,Sudofloc A and polyelectrolytes as follows:
Average turbidity = - 411 + 2.65 Alum + 0.67 PAC + 12.4 Sudofloc A+ 1919 Total polymer
The R2measure for the model is 0.617.
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Water treatment cost saving by separation of three rivers
An empirical approach was tried to develop a model that relates chemicalcost per unit of treated water to raw water quality.Water quality parameters such as turbidity, pH, organic matter and colorof raw water which are available and considered to influence coagulationprocess were included in regression equations.
Costs/1000m3
for all the chemicals was related to the raw water turbiditywith R2 of 0.197 as follows.
Cost/1000m3= 23.2 + 0.00464 Daily average turbidity
The R
2
was not increased much more by including more parameters.
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Chemical cost reductions at the water treatment plants using raw waterfrom WTC for water quality management alternatives (in US $)
Yearly chemical cost Yearly chemical cost reduction byapplying alternatives
Alternatives Buaran WTPAll the WTPs using
WTC raw waterBuaran WTP
All the WTPs using
WTC raw water
Present 4,402,139 13,686,650
Bekasi siphon 4,340,099 13,493,763 62,040 192,886
Bekasi &
Cikarang siphon4,302,515 13,376,911 99,624 309,739
Bekasi & Cibeetsiphon 4,287,070 13,328,889 115,069 357,760
Bekasi, Cikarang
& Cibeet siphon4,202,042 13,064,529 200,097 622,120
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Conclusions
Water quality improvement in terms of turbidity and BOD in thedownstream of WTC was evaluated with application of alternatives insiphon constructions.Then yearly savings in chemicals cost were derived applying chemicalcost per unit of water treated estimated in the wide range of raw waterturbidity at Buaran WTP.
These savings in chemicals would be only part of cost savings in watertreatment. Other savings in labor, electricity and maintenance from less useof chemicals and disposal of less sludge should be included for completeanalysis.There is difficulty in assessing management alternatives by only limited
general water quality parameters such as BOD and turbidity which comefrom organic pollution and sediment. Load assessment for industrialsources will be necessary in crossing river basins to know the possibility inrelease of harmful pollutants into the raw water to WTPs.
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