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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4472
Study on Increasing The Efficiency of The Existing Sequential Batch
Reactor of St.Joseph Engineering College
Mr Dheeraj1, Ms Mohita1, Mr Musthakeem Mohammed1, Mr Kiran Kumar Raikar1 and
Mr Ajeeth B 2
1UG Students, Department of Civil Engineering, SJEC, Mangaluru
2 Assistant Professor, Department of Civil Engineering, SJEC, Mangaluru
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - The present study was carried out to evaluate
the efficiency of SBR of St. Joseph Engineering College.
Wastewater samples were collected in dailybasisandanalysis
of various water parameters were performed. Such as COD,
BOD, pH, Specific conductivity, Turbidity and hardness.
Increase in aeration time resulted in decrease in the values of
the water parameters. Usage of tubesettlers with algae
resulted in better water quality. Our study on characteristics
of wastewater resulted in reduction of aerationtime8hoursto
5 hours.
Key Words: SBR; Tubesettlers; Algae; Aeration
1.INTRODUCTION ( Size 11 , cambria font)
Sewage is 99% water carrying domestic wateroriginating in
kitchen, bathing, urine, washing clothes and night soil.
Sewage also contains water borne pathogenic organisms of
typhoid, jaundice, which originate from the night soil of the
already infected person.
Sewage treatment is normally carried out by aerobic and
anaerobic bacteria whereby there metabolize the organic
matter and multiply themselves and which are settled out
and disposed as sludge. Treated sewage as effluent can be
reused to contribute to conservation of water in areas
suffering from water scarcity. Direct discharge of sewage in
to nearby natural water body or underground body may be
one of the reason for water pollution.
To reduce pollution of the natural water body, treatment of
sewage water is compulsory. The treatment of sewage is
possible by various processes like Up-flow anaerobic sludge
blanket (UASB), Activated sludge process, Oxidation pond,
Trickling filter, Sequential batch reactor(SBR),Fluidizedbed
reactor, Membrane reactor, combi-treat technology etc. Out
of these Sequential batch reactor(SBR) and Activatedsludge
process(ASP) have many applications.
1.1 Sequential batch reactor process
A Sequential batch reactor is a treatment process that
consists of a sequence of steps that are carried out in the
same enclosed structure, called as tank reactor. The SBR
operation is based on “fill-and-draw” principle, consisting of
five steps ,namely-fill, react, settle, decant and Idle.
During fill phase the basin receives influent water where
influent brings food to the microbes in activated sludge,
creating an environment for biochemical reactions. During
react phase,no wastewater will enter the the reactor and
aeration units and mechanical mixing are switched on.
During settle phase activated sludge is allowed to settle
under inactive state.Clarified treated effluent is removed
from the tank in decant phase. The idle period is used when
the system is waiting for enough effluent to process.
2. LITERATURE REVIEW
As per the study of Devendra Dohare, Mahesh Kawale
(2014)on the biological treatment of wastewater using
activated sludge process and sequential batch reactor
process. In this paper they provided an overall information
regarding activated sludge process and sequential batch
process. When compared to other processes these two
processes are considered to be widely used.Theefficiencyof
the SBR is considered to be greater than that of ASP as it isof
low cost and consumes less space for both continues and
intermittent flow, thus SBR is preferred in selection of
technology for biological treatment of wastewater.
The oxygen dissolving capacityofSBRishigherthanASPand
it tends to provide higher Fecal Coliform removal efficiency.
Expansion of SBR is much more flexible than that of ASP,as
the Quality of Effluents is better in case of SBR hence the
quality standards of the water body are maintainedin which
the effluents are to be discharged. Hence it proves SBR to be
most economical and highly efficient which resultsinhaving
maximum probability in the selection process of technology
for Biological Treatment of Wastewater.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4473
As per the work of Jency Nadayil, Devu Mohan et al(2015)
aeration can be an effective method in treating domestic
waste water, laboratory tests were conducted on the
domestic wastewater and various parameterslike COD,BOD
and Turbidity were performed to study the effectofaeration
in domestic wastewater. This paper mainly focuses on how
the variation of various constituents takes place due to
aeration. Diffused fine bubble aeration was conducted in a
circular tank at flow rates of 4 L/minute,3 L/minute & 1.5
L/minute at time periods of 72 hours, 48 hours & 24 hours
using aerators and the values of percentage reduction in
COD, BOD and Turbidity were obtained. It was found that
percentage removal of constituents increased as flowrateof
aeration increased. Hence it was obtained that at a flow rate
of 4 L/min at time period of 72 hours optimum removal of
Turbidity, COD, BOD were found to be removed by and
37.72% , 95.71%, 95.88% respectively.
As per the work of Uzma Showkat&IshtiyaqAhmedNajar
(2018) study was conducted to evaluate the performance of
sewage treatment plant of 16.1MLD based on the SBR
technology. Laboratory Tests were conducted to analyse the
14 different water parameters. Such as COD, pH ,Electric
Conductivity, Magnesium, sodium,Potassium,Calcium,BOD,
TSS, TDS, Ortho-Phosphate, Total Phosphorus & Nitrate
Nitrogen were performed, It revealed that the SBR based
treatment removed the unacceptable physiochemical
properties of wastewaterbeforedischargingitintothewater
body, But reduction of total dissolvedsolids,total suspended
solids and ortho-phosphate was low. Thus effluents might
result in adverse effects on the receiving water body, as the
waterbody may be already facing pollution load. Hence it is
necessary to have continuous monitoringoverthetreatment
process by concerned authorities to ensure best measures
with respect to the treatment and discharge of wastewater
to the receiving waterbody.
As per Prof. Ing. Alberto Bertucco’s (2013) thesis on
Treating urban wastewaters with Microalgae: Batch and
continuous flow experiments and preliminary process
design. The possibilityofcombining existingactivatedsludge
method with cultivation of microalgae was addressed.
Growth of microalgae i.e. Chlorella Prothothecoides was
tested in un-sterilized urban waste waters was tested by
batch experiments which were carried out at different
temperature conditions in order to replicate variation of
annual temperature of influent wastewater of the treatment
plant. During this process of temperature screening it was
found that high dependence of growth rate of Chlorella
Prothothecoides was constant on temperature variation.
Further, the microalgae consortium from the wastewater
was detected, and was grown in batch mode in order to
distinguish its strain composition for future developments
and researches.An examinationofChlorella Prothothecoides
growth capacity in diluted sample of synthetic human urine
was performed ,but the results failed due to the incorrect
composition synthetic human urine.
Continuous flow experiments were performed using a flat
panel photobioreactor both under a simulated daylight and
by providing constant illumination, during these
experiments the production of biomass and depletion of
nutrients were observed and results were merged with the
data received from the thesis work done previously. Finally,
proposal was given for the three waste water treatment
processes merged with microalgae production and were
analysed by a preliminary process design approach.
3. METHODOLOGY
Preparation of model of sequential batch reactor(SBR) .
 A small working model of SBR is constructed using
acrylic sheet, silicon gum etc.
 The SBR model is fabricated using transparent
Acrylic sheets with square cross section.
Collection of sample from sewage treatment plant.
 The wastewater sample is collected from the
collection tank of the sewage treatment plant every
day and various laboratorical experimentsaredone
to determine characteristic.
Analysis of characteristics of wastewater before
treating.
 The characteristics such as BOD, COD, pH etc. are
tested for the sample collected from wastewater
collection pit.
Treatment of sample by SBR model.
 The collected water is poured to SBR model i.e. fill
phase.
 Air diffusers are made to operate for certain time
limit(aeration begins) i.e react phase.
 After aeration, restphasefollows.Heresludgestarts
settling down, leaving behind clear water.
 Now the clear water is extractedfromtheoutletsi.e
decant phase.
 Repetition of the same procedure.
Treatment using tubesettlers with algae.
 Algae from the neighbouring area is obtained.
 Tubesettlers are introduced in order to create a
controlled environment for the growth of algae
 Algae obtained is grown within the tube settlers
such that their chance of spreading is minimum
 The tubesettlers are laid within the SBR model
before aeration.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4474
Analysis of effluent characteristics of treated
wastewater.
 The treated water from SBR model is collected and
various tests like COD, BOD, pH etc. are conducted.
Details of the Existing SBR
 SBR is of 3lakh capacity with 2 partition, each of 1.5
lakh capacity.
 Aeration time-8 to 10 hours.
 Settling time-30 to 40 mins
 Acclimatization products are chlorine and lime
stone.
 Filtration bed consists of carbon filter and sand.
 Source of waste water:
 Boys and girls hostel have 124 and 97 washrooms.
 There are 3 main blocks having 25 washrooms.
 Bethania hall and dispensary has 20 washrooms.
Tubesettler
The tube settler’s channel collects solids into compact mass
which promotes the solids to slide down the tube channel.
Fig -1: Tubesettlers
4. RESULTS
pH Test :
Turbidity:
Specific Conductivity:
Initial
reading
After
1hr
After
2hr
After
3hr
After
4hr
After
5hr
After
6hr
0.526 0.482 0.432 0.421 0.418 0.385 0.364
Initial
reading
After
1hr
After
2hr
After
3hr
After
4hr
After
5hr
After
6hr
7.25 6.83 6.60 6.68 6.71 7.79 7.85
Initial
reading
After
1hr
After
2hr
After
3hr
After
4hr
After
5hr
After
6hr
120 111 94 78 75 73 46
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4475
Hardness Test:
Initial
reading
After
1hr
After
2hr
After
3hr
After
3hr
After
4hr
After
5hr
116 100 104 102 102 86 82
COD :
Initial
reading
After
1hr
After
2hr
After
3hr
After
4hr
After
5hr
After
6hr
380 320 240 160 152 137 128
BOD :
Initial
reading
After
1hr
After
2hr
After
3hr
After
4hr
After
5hr
After
6hr
190 176 165 154 147 142 137
5. CONCLUSIONS
 As per our study on characteristics of wastewater,
we can conclude that aeration time required can be
reduced from 8hours to 5 hours
 Quality of the water can be maintained by usage of
tubesettlers with algae.
ACKNOWLEDGEMENT
This paper expresses our gratitude to our institution and
management for providing us with good infrastructure,
qualified staff, whose guidance was of immense, help in
completion of this paper successfully. Without their
encouragement and guidance this project would not have
materialized.
REFERENCES
[1] Metcalf & Eddy, Inc. Wastewater Engineering:
Treatment, Disposal, Reuse.4th edition.
[2] Devendra Dohare,MaheshKawale(2014),Biological
Treatment of Wastewater Using Activated Sludge
Process and Sequential Batch ReactorProcess,ISSN:
2277-9655,Scientific Journal Impact Factor: 3.449
ISRA), Impact Factor: 2.114
[3] Jency Nadayil, Devu Mohan et al(2015), A Study on
effect of aeration on domestic wastewater(IJIRI)vol
3, issue 2, pp: (10-15) ISSN 2348-1218
[4] Uzma Showkat, Ishtiyaq Ahmed Najar, Study on the
efficiency of the sequential batch reactor-based on
sewage treatment plant, Applied Water Science.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4476
[5] Prof. Ing. Alberto Bertucco (2013) Treating urban
wastewaters withMicroalgae:Batchandcontinuous
flow experiments and preliminary process design,
University of Padua, Department of Civil,
Construction and Environmental Engineering
[6] Siddhartha V. Pawar, Pooja D. Taralgatti,
International Journal of Science, Engineering and
Technology Research (IJSETR) Volume 6, Issue 12,
December 2017, ISSN: 2278 -7798
[7] Garg S.K, Khanna, 2010: edition publisher:
Environmental Engineering

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IRJET- Study on Increasing the Efficiency of the Existing Sequential Batch Reactor of St.Joseph Engineering College

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4472 Study on Increasing The Efficiency of The Existing Sequential Batch Reactor of St.Joseph Engineering College Mr Dheeraj1, Ms Mohita1, Mr Musthakeem Mohammed1, Mr Kiran Kumar Raikar1 and Mr Ajeeth B 2 1UG Students, Department of Civil Engineering, SJEC, Mangaluru 2 Assistant Professor, Department of Civil Engineering, SJEC, Mangaluru ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - The present study was carried out to evaluate the efficiency of SBR of St. Joseph Engineering College. Wastewater samples were collected in dailybasisandanalysis of various water parameters were performed. Such as COD, BOD, pH, Specific conductivity, Turbidity and hardness. Increase in aeration time resulted in decrease in the values of the water parameters. Usage of tubesettlers with algae resulted in better water quality. Our study on characteristics of wastewater resulted in reduction of aerationtime8hoursto 5 hours. Key Words: SBR; Tubesettlers; Algae; Aeration 1.INTRODUCTION ( Size 11 , cambria font) Sewage is 99% water carrying domestic wateroriginating in kitchen, bathing, urine, washing clothes and night soil. Sewage also contains water borne pathogenic organisms of typhoid, jaundice, which originate from the night soil of the already infected person. Sewage treatment is normally carried out by aerobic and anaerobic bacteria whereby there metabolize the organic matter and multiply themselves and which are settled out and disposed as sludge. Treated sewage as effluent can be reused to contribute to conservation of water in areas suffering from water scarcity. Direct discharge of sewage in to nearby natural water body or underground body may be one of the reason for water pollution. To reduce pollution of the natural water body, treatment of sewage water is compulsory. The treatment of sewage is possible by various processes like Up-flow anaerobic sludge blanket (UASB), Activated sludge process, Oxidation pond, Trickling filter, Sequential batch reactor(SBR),Fluidizedbed reactor, Membrane reactor, combi-treat technology etc. Out of these Sequential batch reactor(SBR) and Activatedsludge process(ASP) have many applications. 1.1 Sequential batch reactor process A Sequential batch reactor is a treatment process that consists of a sequence of steps that are carried out in the same enclosed structure, called as tank reactor. The SBR operation is based on “fill-and-draw” principle, consisting of five steps ,namely-fill, react, settle, decant and Idle. During fill phase the basin receives influent water where influent brings food to the microbes in activated sludge, creating an environment for biochemical reactions. During react phase,no wastewater will enter the the reactor and aeration units and mechanical mixing are switched on. During settle phase activated sludge is allowed to settle under inactive state.Clarified treated effluent is removed from the tank in decant phase. The idle period is used when the system is waiting for enough effluent to process. 2. LITERATURE REVIEW As per the study of Devendra Dohare, Mahesh Kawale (2014)on the biological treatment of wastewater using activated sludge process and sequential batch reactor process. In this paper they provided an overall information regarding activated sludge process and sequential batch process. When compared to other processes these two processes are considered to be widely used.Theefficiencyof the SBR is considered to be greater than that of ASP as it isof low cost and consumes less space for both continues and intermittent flow, thus SBR is preferred in selection of technology for biological treatment of wastewater. The oxygen dissolving capacityofSBRishigherthanASPand it tends to provide higher Fecal Coliform removal efficiency. Expansion of SBR is much more flexible than that of ASP,as the Quality of Effluents is better in case of SBR hence the quality standards of the water body are maintainedin which the effluents are to be discharged. Hence it proves SBR to be most economical and highly efficient which resultsinhaving maximum probability in the selection process of technology for Biological Treatment of Wastewater.
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4473 As per the work of Jency Nadayil, Devu Mohan et al(2015) aeration can be an effective method in treating domestic waste water, laboratory tests were conducted on the domestic wastewater and various parameterslike COD,BOD and Turbidity were performed to study the effectofaeration in domestic wastewater. This paper mainly focuses on how the variation of various constituents takes place due to aeration. Diffused fine bubble aeration was conducted in a circular tank at flow rates of 4 L/minute,3 L/minute & 1.5 L/minute at time periods of 72 hours, 48 hours & 24 hours using aerators and the values of percentage reduction in COD, BOD and Turbidity were obtained. It was found that percentage removal of constituents increased as flowrateof aeration increased. Hence it was obtained that at a flow rate of 4 L/min at time period of 72 hours optimum removal of Turbidity, COD, BOD were found to be removed by and 37.72% , 95.71%, 95.88% respectively. As per the work of Uzma Showkat&IshtiyaqAhmedNajar (2018) study was conducted to evaluate the performance of sewage treatment plant of 16.1MLD based on the SBR technology. Laboratory Tests were conducted to analyse the 14 different water parameters. Such as COD, pH ,Electric Conductivity, Magnesium, sodium,Potassium,Calcium,BOD, TSS, TDS, Ortho-Phosphate, Total Phosphorus & Nitrate Nitrogen were performed, It revealed that the SBR based treatment removed the unacceptable physiochemical properties of wastewaterbeforedischargingitintothewater body, But reduction of total dissolvedsolids,total suspended solids and ortho-phosphate was low. Thus effluents might result in adverse effects on the receiving water body, as the waterbody may be already facing pollution load. Hence it is necessary to have continuous monitoringoverthetreatment process by concerned authorities to ensure best measures with respect to the treatment and discharge of wastewater to the receiving waterbody. As per Prof. Ing. Alberto Bertucco’s (2013) thesis on Treating urban wastewaters with Microalgae: Batch and continuous flow experiments and preliminary process design. The possibilityofcombining existingactivatedsludge method with cultivation of microalgae was addressed. Growth of microalgae i.e. Chlorella Prothothecoides was tested in un-sterilized urban waste waters was tested by batch experiments which were carried out at different temperature conditions in order to replicate variation of annual temperature of influent wastewater of the treatment plant. During this process of temperature screening it was found that high dependence of growth rate of Chlorella Prothothecoides was constant on temperature variation. Further, the microalgae consortium from the wastewater was detected, and was grown in batch mode in order to distinguish its strain composition for future developments and researches.An examinationofChlorella Prothothecoides growth capacity in diluted sample of synthetic human urine was performed ,but the results failed due to the incorrect composition synthetic human urine. Continuous flow experiments were performed using a flat panel photobioreactor both under a simulated daylight and by providing constant illumination, during these experiments the production of biomass and depletion of nutrients were observed and results were merged with the data received from the thesis work done previously. Finally, proposal was given for the three waste water treatment processes merged with microalgae production and were analysed by a preliminary process design approach. 3. METHODOLOGY Preparation of model of sequential batch reactor(SBR) .  A small working model of SBR is constructed using acrylic sheet, silicon gum etc.  The SBR model is fabricated using transparent Acrylic sheets with square cross section. Collection of sample from sewage treatment plant.  The wastewater sample is collected from the collection tank of the sewage treatment plant every day and various laboratorical experimentsaredone to determine characteristic. Analysis of characteristics of wastewater before treating.  The characteristics such as BOD, COD, pH etc. are tested for the sample collected from wastewater collection pit. Treatment of sample by SBR model.  The collected water is poured to SBR model i.e. fill phase.  Air diffusers are made to operate for certain time limit(aeration begins) i.e react phase.  After aeration, restphasefollows.Heresludgestarts settling down, leaving behind clear water.  Now the clear water is extractedfromtheoutletsi.e decant phase.  Repetition of the same procedure. Treatment using tubesettlers with algae.  Algae from the neighbouring area is obtained.  Tubesettlers are introduced in order to create a controlled environment for the growth of algae  Algae obtained is grown within the tube settlers such that their chance of spreading is minimum  The tubesettlers are laid within the SBR model before aeration.
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4474 Analysis of effluent characteristics of treated wastewater.  The treated water from SBR model is collected and various tests like COD, BOD, pH etc. are conducted. Details of the Existing SBR  SBR is of 3lakh capacity with 2 partition, each of 1.5 lakh capacity.  Aeration time-8 to 10 hours.  Settling time-30 to 40 mins  Acclimatization products are chlorine and lime stone.  Filtration bed consists of carbon filter and sand.  Source of waste water:  Boys and girls hostel have 124 and 97 washrooms.  There are 3 main blocks having 25 washrooms.  Bethania hall and dispensary has 20 washrooms. Tubesettler The tube settler’s channel collects solids into compact mass which promotes the solids to slide down the tube channel. Fig -1: Tubesettlers 4. RESULTS pH Test : Turbidity: Specific Conductivity: Initial reading After 1hr After 2hr After 3hr After 4hr After 5hr After 6hr 0.526 0.482 0.432 0.421 0.418 0.385 0.364 Initial reading After 1hr After 2hr After 3hr After 4hr After 5hr After 6hr 7.25 6.83 6.60 6.68 6.71 7.79 7.85 Initial reading After 1hr After 2hr After 3hr After 4hr After 5hr After 6hr 120 111 94 78 75 73 46
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4475 Hardness Test: Initial reading After 1hr After 2hr After 3hr After 3hr After 4hr After 5hr 116 100 104 102 102 86 82 COD : Initial reading After 1hr After 2hr After 3hr After 4hr After 5hr After 6hr 380 320 240 160 152 137 128 BOD : Initial reading After 1hr After 2hr After 3hr After 4hr After 5hr After 6hr 190 176 165 154 147 142 137 5. CONCLUSIONS  As per our study on characteristics of wastewater, we can conclude that aeration time required can be reduced from 8hours to 5 hours  Quality of the water can be maintained by usage of tubesettlers with algae. ACKNOWLEDGEMENT This paper expresses our gratitude to our institution and management for providing us with good infrastructure, qualified staff, whose guidance was of immense, help in completion of this paper successfully. Without their encouragement and guidance this project would not have materialized. REFERENCES [1] Metcalf & Eddy, Inc. Wastewater Engineering: Treatment, Disposal, Reuse.4th edition. [2] Devendra Dohare,MaheshKawale(2014),Biological Treatment of Wastewater Using Activated Sludge Process and Sequential Batch ReactorProcess,ISSN: 2277-9655,Scientific Journal Impact Factor: 3.449 ISRA), Impact Factor: 2.114 [3] Jency Nadayil, Devu Mohan et al(2015), A Study on effect of aeration on domestic wastewater(IJIRI)vol 3, issue 2, pp: (10-15) ISSN 2348-1218 [4] Uzma Showkat, Ishtiyaq Ahmed Najar, Study on the efficiency of the sequential batch reactor-based on sewage treatment plant, Applied Water Science.
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 04 | Apr 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4476 [5] Prof. Ing. Alberto Bertucco (2013) Treating urban wastewaters withMicroalgae:Batchandcontinuous flow experiments and preliminary process design, University of Padua, Department of Civil, Construction and Environmental Engineering [6] Siddhartha V. Pawar, Pooja D. Taralgatti, International Journal of Science, Engineering and Technology Research (IJSETR) Volume 6, Issue 12, December 2017, ISSN: 2278 -7798 [7] Garg S.K, Khanna, 2010: edition publisher: Environmental Engineering