Journal of Environmental Treatment Techniques 2015, Volume 3, Issue 2, Pages: 170-174
170
Optimization of Coagulation/Flocculation for Treatment of
Wastewater
Abdolreza Karbassi, Maryam Pazoki
Department of Environment, University of Tehran, Tehran, Iran
Received: 19/04/2015 Accepted: 08/06/2015 Published: 30/06/2015
Abstract
One of the industrial areas in the south of Iran is Bandar Imam Petrochemical Economic Zone which has a lot of
petrochemical complex, Farabi Petrochemical complex is one of those places. Coagulation/flocculation could be a typical
methodology in water and wastewater treatment that a number of chemicals are added to assist the coagulation/flocculation and
causes to the sedimentation. In this paper, the sampling and measurement of characteristics wastewater containing turbidity, pH,
COD, TDS and etc. were done, also Efficiency of coagulant was assessed in terms of the COD, TDS and turbidity also the
optimum concentration to determine the coagulant and the pH effluent were investigated.The results show that the optimum
coagulants for decreasing organic matters of wastewater, the amount of coagulant is 10mm per liter of wastewater. With this
amount can be reduced by more than 50% of COD.
Keywords: Wastewater, effluent, Farabi Petrochemical complex, coagulant, jar test
1 Introduction
1
Industrial wastewater containing organic material
which enters to the groundwater or surface water is an
environmental concern. Due to characterization of these
pollutants such as non-biodegradable, high toxicity,
cumulative and carcinogenic effects are considered.
Discharge of effluents containing organic material is not
only harmful to aquatic life and plants, but also, is very
dangerous due to ecosystem changes [1].
Due to the increasing applications of petrochemical
products, destructive and negative effects on the
environment caused by the production of wastewater, solid
waste and gas emissions to the environment should be
considered.
Coagulation/flocculation could be a typical methodology in
water and wastewater treatment [2, 3, 4& 5] that a number
of chemicals are added to assist the
coagulation/flocculation and causes to the sedimentation.
Mentioned chemical materials are sodium hydroxide to
regulate the pH range, metallic ions and commercial
anionic or cationic-based poly-electrolytes (PEs) [6].
Coagulation process was found to be economical, easy
to work and uses less energy than various treatment
methods. Coagulation is extensively utilized in several
water treatment plants and has been found to be desirable in
the treatment of wastewaters from petroleum refineries and
industrial treatment plant [7, 8].
In recent years, due to vast oil and gas resources in the
country and and the government's economic policies, the
petrochemical industry has developed considerable, and
Corresponding author: Maryam Pazoki, Department of
Environment, University of Tehran, Tehran, Iran.
E-mail: mpazoki@ut.ac.ir
Recent research has strongly implies that the Persian Gulf
is seriously polluted with toxic metals and oil.
In recent years, in many parts of the country, using
wastewater for irrigation of farmlands in most cases due to
lack of water and increasing of wastewater is inevitable [9].
The management of wastewater and leachate from landfill
for irrigation or using energy leads to costs reduction. [10,
11] Also, it would increase agricultural production,
especially in dry climates and less water situation. With
respect to the notes, the development of green space is one
of the advantages of the effluent [12].
Considering shortage of water in arid and semi-arid
areas, reusing of unconventional water including municipal
and industrial wastewater and at the same time in
compliance with environmental considerations, is
necessary. For reusing of wastewater in different parts,
quality of wastewater effluent and standards should be
considered [13]. Presence of heavy metals in wastewater
treatment and the accumulation of these metals, especially
cadmium and lead in soil, are considered as important
environmental issues [14].
In the present study, at first the quantity of the
wastewater after each stage and the amount of overall
wastewater was analyzed. Efficiency of coagulant was
assessed in terms of the COD, TDS and turbidity also the
optimum concentration to determine the coagulant and the
pH effluent were investigated.
2 Materials and Methods
In this study, firstly identifying of Farabi
petrochemicals production process, consumables chemicals
and research for identifying the amount of wastewater
production at each stage and whole process was
investigated. Then, the sampling and measurement
characteristics of wastewater are done that containing pH,
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J. Environ. Treat. Tech.
ISSN: 2309-1185
Journal of Environmental Treatment Techniques 2015, Volume 3, Issue 2, Pages: 170-174
171
COD, TDS, … and the effectiveness of coagulant test (poly
aluminum chloride) and jar test was studied to determine
the optimum concentration of coagulant and suitable pH
range for the final wastewater. It should be mentioned that,
the tests were carried out according to the APHA standard
[15]. All tests were repeated three times and the mean
values are showed in this paper.
2-1- specifications of the region under study
2-1-1- Farabi petrochemical facility specifications
Farabi petrochemicals department with an area of 20
acres on the northwest side of the Persian Gulf, port of
Imam Khomeini and in the vicinity of Imam Petrochemical
port, Razi and at petrochemical special economic zone are
located.
Now, in this department, wastewater without any
settling was entered in Khor Mousa River and then Persian
Gulf. According to the carcinogenic of food and substances
productive and since the fish, birds, plant tissue and finally
human are in danger so it is necessary for wastewater
settling and disposal of organic materials. Figure 1 shows
map of khor mousa and Farabi complex and Figure 2 shows
Wastewater treatment process diagram.
2-2- Characteristics of wastewater
Characteristics of total wastewater have been measured.
Wastewater flow was 720 m
3
/day and temperature of
wastewater was 250 C. table 1 shows characteristics of
total wastewater.
Fig.1- Khor Mousa and Farabi complex
Table 1- Characteristics of wastewater
Fecal Coliform (Mpv/100 ml)
Ec
s/cm
pH
Total Hardness
(CaCO
3
) mg/l
TDS
mg/l
BOD
5
mg/l
COD
mg/l
1100
3878
6.8
700
2000
800
2677
2-3- Sampling
The effluent samples were collected from Farabi
Petrochemical wastewater discharge to the Khor Mousa
rever.
Sampling and measurements of various characteristics of
wastewater were conducted in according to the standard
methods for the examination of treated water and
wastewater [15].
2-4- Jar tests
The jar test was used to optimize the addition of
coagulants and flocculants and poly aluminum chloride
coagulant were utilized in different dose. For coagulation
test, 200 rpm was used for mixing in five minutes and for
flocculation, slow mixing rate (40 rpm) was used for five
minutes also settling time was 30 minutes. Two series of jar
tests were taken accordance with the standard test methods
[16].
3 Results and Discussion
In this section the results of water quality and quantity
of the wastewater and effectiveness of the coagulant (poly
aluminum chloride) were provided then the jar test were
done to determine the optimum concentration of coagulant
and a suitable pH range for maximum efficiency.
3-1- Results of quality and quantity of wastewater
The following chart compares the volume of
wastewater produced and COD effluent compared to the
output in the different processes.
Figure 3 shows that highest amount of organic material
is related to the washing process. Esterification, recycling
and dewatering stages have an organic load between 3000-
4000 mg/l.
Journal of Environmental Treatment Techniques 2015, Volume 3, Issue 2, Pages: 170-174
172
Figure 2: Wastewater treatment process diagram
Figure 3: comparing of effluent COD in different processes
According to Figure 4, the maximum volume of
wastewater production are form resin restoration, road
washing, backwashing of sand filters and steam traps
respectively.
3-2- Effect of coagulants on wastewater
Table 2 shows the results of the effect of coagulants on
the removal of COD and turbidity. As can be seen, removal
percentage of COD and turbidity was 38% and 99%
respectively, which both test results were acceptable.
3-3- Jar test results
Sampling (6 samples every 2 hours, 1 liter for each time)
was done from the second pond of treatment plant.
COD and TDS of the raw wastewater were 1870 and 3290
mg/l also in pH of 6.4, turbidity was 970 NTU. Jar test No.
1 shows the optimum pH in a fixed dose of coagulant.
According to the table 2, the best result for COD removal is
occurred in pH of 9. Jar test number 3: shows the optimum
dose of coagulant in a fixed pH. According to the table 4
the best dose of coagulant is 10ml. Jar test No. 3 shows the
optimum pH in the fixed optimum dose of coagulant with a
higher pH.
0
2000
4000
6000
8000
10000
12000
14000
16000
18000
20000
COD (mg/l)
Process
Esterification
Alkaline wash
Alcohol recovery
Washing
Dewatering
DOP
PA
Sand filters for cooling towers
Sand filter for water treatment
Resin restoration
Road washing
Steam Traps
Journal of Environmental Treatment Techniques 2015, Volume 3, Issue 2, Pages: 170-174
173
Figure 4: comparing of wastewater production volume (liters per hour) in the effluent of processes
Table 2: Results of coagulants tests on wastewater
Sample
pH
Turbidity NTU
EC (µs/cm)
TDS (mg/l)
T(°C)
COD (mg/l)
TSS (mg/l)
Control
8.5
461
4875
2830
29.5
1060
1540
6 cc coagulants
7.55
3
5158
3010
29.8
673
-
10 cc coagulants
7.06
4.6
5565
3260
29.1
684
-
Table 3- Jar test results fixed dose of coagulant sample temperature: 15 C°
Sample
Coagulants
mg
primary
pH
Turbidity
NTU
TDS
mg/l
Final pH
COD
mg/l
Reduction% COD
Sludge volume
ratio
1
10
6
160
4160
4
1270
32
Normal
2
10
7
240
4260
4.1
1235
34
Normal
3
10
7.5
213
2200
4.1
1310
30
Normal
4
10
9
93
3310
4.4
810
57
High
Table 4- Jar tests result- fixed pH, sample temperature: 15 C°
Sample
Coagulants
mg
Coagulants
(%)
primary
pH
Turbidity
NTU
TDS
mg/l
Final
pH
COD
mg/l
Reduction
(%) COD
Sludge
volume ratio
1
2
0.01
9
21
3820
6.69
1640
13
Normal
2
5
0.02
9
26
3260
5.25
1120
40
High
3
10
0.05
9
105
3240
4.34
910
51
High
4
15
0.07
9
167
3390
4.14
1120
40
Normal
Table 5: Jar test results - optimum dose of coagulant - sample temperature 15 C°
Sample
Coagulants
mg
pH
primary
Turbidity
NTU
TDS
mg/l
pH
Final
COD
mg/l
Removal
percentage
Volume ratio of
sludge
1
10
8
210
2240
4.1
1320
29
Normal
2
10
9
90
3298
4.4
821
56
Normal
3
10
10
120
3100
4.5
952
49
High
4
10
11
138
3207
4.7
998
45
High
According to the table 5 the best range of pH for maximum
COD removal is 9. According to the results obtained in the
three jar test, it can be said that the experimental error was
less than 10%.
4 Conclusions
At analyzing of output characteristics of wastewater
over a period of 6 months, was determined that in most
cases, organic pollution is far more than the designed
(COD=2677mg/l), so serious attempt should be made to the
0
5
10
15
20
25
30
35
40
45
50
wastewater production volume (l/h)
Process
Esterification
Alkaline wash
Alcohol recovery
Washing
Dewatering
DOP
PA
Sand filters for cooling towers
Sand filter for water treatment
Resin restoration
Road washing
Steam Traps
Journal of Environmental Treatment Techniques 2015, Volume 3, Issue 2, Pages: 170-174
174
wastewater settling. Because the system of DOP production
is a batch system and because the current volume of
wastewater storage tank (90m3), every day at least 8 times
wastewater is discharged in to the Khor. And a simple
sampling can’t determine the characteristics of outcome
wastewater so composite sampling is required. In this
study, the effect of chemical coagulation by poly-aluminum
chloride coagulants of on wastewater as pre-settling was
tested in the laboratory. According to the current test results
indicate that the optimum coagulants for decreasing organic
matters of wastewater, the amount of coagulant is 10mm
per liter of wastewater. With this amount can be reduced by
more than 50% of COD. According to the wastewater
production rate at the maximum (currently) 700 cubic
meters per day, in this case for pre-settling 7000 liters of
coagulant 2% or 1000 liters of coagulant 14% should be
consumed.
References
1 Kowalska I., Kabsch-Korbutowicz, M., Majewska-
Nowak, K., Pietraszek, M., Removal of Detergents
from Industrial Wastewater in Ultrafiltration Process,
Environment Protection Engineering, Vol.31, No. 3-4,
pp. 207-219, 2005.
2 Ching-Jey K., Gary A., Curtis B., Factors affecting
coagulation with aluminum sulfate-I,Water Res. 22
(1988) 853862.
3 Franceschi M., Girou A., Carro-Diaz A.M., Maurette
M.T., Puech-Costes E., Optimisation of the
coagulationflocculation process of raw water by
optimal design method,Water Res. 36 (2002) 3561
3572.
4 Tatsi A.A., Zouboulis A.I., Matis K.A., Samara P.,
Coagulationflocculation pretreatment of sanitary
landfill leachates, Chemosphere 53 (2003) 737744.
5 Al-Mutairi N.Z., Hamoda M.F., Al-Ghusain I.,
Coagulant selection and sludge conditioning in a
slaughterhouse wastewater treatment plant, Bioresour.
Technol. 95 (2004) 115119.
6 Satterfield Z., Jar Testing: Technical Brief of National
Environmental Service Center, vol. 5, 2005, pp. 24.
7 Santo C.E., Vilar J.P., Botelho M.S., Bhatnagar A.,
Kumar E., Boaventura A.R., Optimization of
coagulationflocculation and flotation parameters for
the treatment of a petroleum refinery effluent from a
Portuguese plant, Chem. Eng. J. 183 (2012) 117123.
8 Verma S., Prasad B., Mishra I.M., Pretreatment of
petrochemical wastewater by coagulation and
flocculation and the sludge characteristics, J. Hazard.
Mater. 178 (2010) 10551064.
9 Mohammadi, P., Sepahi, M., Mehrdadi, N., Liaghat, A.,
Adl, M., Ehteshami, M., Ashrafi, A., Ghodusi, F., and
Zarnokaii, M. R. (2002). “Review of standards and
expperiments of appilcation of wastewater in
irrigation.”Iran National Organization of Irrigation
and Drinage, pp 45.
10 Pazoki M., Abdoli M.A., Karbasi A.R., Mehrdadi N.,
Yaghmaeian k., 2012. Removal of Nitrogen and
Phosphorous from Municipal Landfill Leachate
Through Land Treatment, World Applied Sciences
Journal 20 (4): 512-519, 2012
11 Abdoli, M.A., Karbassi, A.R., Samiee-Zafarghandi, R.,
Rashidi, Zh., Gitipour, S. and Pazoki M.,
(2012).Electricity Generation from Leachate Treatment
Plant, Int. J. Environ. Res., 6(2):493-498.
12 Pazoki M., Abdoli M.A., Karbasi A.R., Mehrdadi N.,
Yaghmaeian k., 2014. Attenuation of Municipal landfill
Leachate through Land treatment, Journal of
Environmental Health Science & Engineering, 12:12
13 Chen, Z. S., S. L. Lo and H. C. Wu (1994). Summary
analysis and assessment of rural soils contaminated
with Cd in Taoyuan. Project of Scientific Technology
Advisor Group (STAG), executive
Yuan.Taipei,Taiwan .
14 Cid, B. P., M. de J. Gonzalez and E. F.Gomez (2002).
Analyst, 126:1304-1311.
15 American Public Health Association (APHA), Standard
methods for the examination of water and wastewater.
22th. Ed., Washington D. C., 2012
16 ASTM, Standard Practice for CoagulationFlocculation
Jar Test of Water, D2035- 08, in: Annual Book of
ASTM Standards, Vol. 11.02, 2008.