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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
EXPERIMENTAL STUDY COST EFFECTIVE WASTE WATER
TREATMENT FOR MICRO UNITS
Roopa.D1, Dineshkumar.A2, Dinesh.T3,Gowtham.B4,Krish navin.K5
1Assistant professor, civil department, gnanamani college of technology, tamilnadu, india
2B.E Student, civil department, gnanamani college of technology, tamilnadu, india
3B.E Student, civil department, gnanamani college of technology, tamilnadu, india
4B.E Student, civil department, gnanamani college of technology, tamilnadu, india
5B.E Student, civil department, gnanamani college of technology, tamilnadu, india
---------------------------------------------------------------------***---------------------------------------------------------------------
ABSTRACT: A cost effective single unit effluent
treatment plant for waste water may be developed to
purify the industrial waste water and sewage waste
water. Effluent sewage water is also used for reusing
and recycling purpose so has reduced depending on
waste water. The chemicals such as a poly aluminium
chloride are being used for treatment the micro units
application for a purification and water as a purification
agent. The remains will be conducted known its initial
various test form. Potential hydrogen (pH), suspended
solid test, biaxial oxygen demand, Chemical oxygen
demand, jar test apparatus, turbidity level. After the
addition Poly aluminium chloride dosage will me 1g, 2g,
4g, 6g adding in the sample water 100 ml. And the
sample water coagulant flocculent in waste water
treatment process in micro units
Key words : Sewage water ,Poly aluminium chlorides,
Industrial waste water,
Introduction to Wastewater Treatment
Industrial wastewater treatment is any process
that separates and removes contaminants from industrial
process waters, or effluent.
These contaminants include oils, dissolved heavy
metals, suspended solids and organic compounds. Either
the local municipality or the Federal Government regulates
the specific contaminants.A series of limits are set to
determine the suitability for discharge. These limits must
be met for the water to be legally discharged.If these limits
are not met, the water must be pre-treated before being
discharged, to remove the majority of the regulated
contaminants. Although we are technically providing pre-
treatment systems, we refer to them as treatment systems.
What makes Wastewater Engineers, Inc. different
from other companies offering similar systems? We have a
commitment to the industry. We specialize in this area, and
can provide common sense advice derived from years of
experience. We provide a written guarantee of our systems’
performance. We bring fluid management
expertise to our clientele, providing added benefits and
cost savings.
We provide complete, turn-key systems, which
handle the water from source to discharge. We provide
excellent service after the sale, and back our systems with
warranties up to 3 years. We have adopted a three-phase
approach to treating industrial wastewater. The three phases
are Pre-treatment, Chemical Treatment, and Post-
treatment. Free Oil And Soluble Oil Often, it is
necessary to remove gross oils from a waste stream prior
to chemical treatment. We supply traditional belt and
wheel skimmers and also an innovative honeycomb “on
the flow” coalesce, which can separate up to 97% of free
oils in the first pass. This range of “on the flow”
coalesces are called L-OR and OR series. Emulsified
oils and grease products require an emulsion breaker to
achieve the floating characteristics of free oils. Once
“popped” the oils may be easily skimmed or coalesced.
Material & methods:
Material:

Sulphuric acid



Sodium thiosulphate



Magnet sulphate



Alkaline iodide



Ferrous ammonium sulphate



Ferns sulphate



Potassium dichromate



Poly aluminium chloride

Methods:

pH scale(power of hydrogen)


BOD(bio chemical oxygen demand)

© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072

COD(chemical oxygen demand) AFTER ADDING PAC IN WATER

Suspended solids
TEST

Turbidity SEAWAGE AREIAL OUTLET
pH SCALE: pH is a scale of acidity from 0 to 14. It tells BOD 13.01 15.2 14.3
how acidic or alkaline a substance is. More acidic
solutions have lower pH. More alkaline solutions have COD 12.3 14.6 11.2
higher pH. Substances that aren't acidic or alkaline (that is,
neutral solutions) usually have a pH of 7. pH 7.3 7.65 11.7
BOD: Biochemical Oxygen Demand is an important
water quality parameter because it provides an index to TABLE 2(AFTER ADDING PAC)
assess the effect discharged wastewater will have on the
receiving environment. The higher the BOD value, the Turbidity amount of sewage, aerial & Outlet water have
greater the amount of organic matter or “food” available been tested by adding Poly aluminium chloride and noted
for oxygen consuming bacteria. in the following (TABLE 3)
COD: Chemical oxygen demand (COD) is a measure of Poly TURBIDITY
the capacity of water to consume oxygen during the
aluminium
decomposition of organic matter and the oxidation of
Sewage Aerial Outlet
inorganic chemicals such as Ammonia and nitrite. chloride
water water water
SUSPENDED SOLIDS: Suspended solids refer to
1g 42.3 124.6 84.5small solid particles which remain in suspension in water
as a colloid or due to the motion of the water. It is used as
one indicator of water quality. 2g 18.2 110.5 81.5
TURBIDITY: The definition of Turbidity is the 3g 19.7 109.5 85.7
cloudiness or haziness of a fluid caused by suspended
solids that are usually invisible to the naked eye. The 4g 23.7 109.6 92.4
measurement of Turbidity is an important test when trying
5g 28.5 108.4 93.3to determine the quality of water
RESULT& DISCUSSION 6g 35.6 120.7 94.6
This test result was before adding PAC in waste TABLE 3( TURBIDITY )
water value results in (TABLE 1).and after adding PAC
The above seen data (table 3) have been plotted has graph
test result was in (TABLE 2).
in the following
BEFORE ADDING PAC IN WATER
TEST SEAWAGE AREIAL OUTLET
BOD 35 43.4 56.7
COD 137 140.09 151.08
pH 8.4 6.7 13.7
Fig 1(GRAPH FOR TRBIDITY TEST)
TABLE: 1(BEFORE ADDIN PAC )
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
DISCUSSION:
We have gone through the BOD, COD, pH, & turbidity
test for sewage water, aerial water, outlet water. It
should be the result higher then permissible result.
before adding poly aluminium chloride has we could its
same producer for the same sewage water, aerial water,
outlet water but we added poly aluminium chloride for
the respective water it’s should the different result
which was lower than the perimeter limits.
RESULT& DISCUSSION:
We testing the industrial waste water before adding
poly aluminium chloride result were given in (Table 4)
PERIMETER BEFORE ADDING PAC IN
WATER
pH 8
Poly aluminium chloride TURBIDITY
1g 120.5
2g 135.6
3g 175.6
4g 202.6
5g 307.6
6g 105.8
TABLE 6 ( TURBIDITY)
BOD 4.517
COD 11.53
TABLE 4 (BEFORE ADDING PAC)
PERIMETER AFTER ADDING PAC IN
WATER
pH 7.78
BOD 5.57
COD 14.6
TABLE 5 (AFTER ADDING PAC)
Turbidity amount of industrial water have been tested by
adding Poly aluminium chloride and noted in the
following (TABLE 6)
Fig 2(GRAPH FOR TRBIDITY TEST)
DISCUSSION:
We have gone through the BOD, COD, pH, &
turbidity test for industrial waste water .It should be the
result lower than the permissible result. Before adding
poly aluminium chloride has we could its same producer
for the same industrial waste water but we added poly
aluminium chloride for the respective water it’s should
the small amount of different result which was lower than
the perimeter limits. The turbidity test was by
adding poly aluminium chloride was 1g, 2g, 3g ,4g ,5g ,6g
respectively given result value was very high
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 3
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
Conclusion:
Sewage water:
Tests which we are gone through have shown a
good turbidity value the sewage water, aerial water,
outlet water can we used for gardening purpose only.
Because of the irrelevant values of BOD, COD, pH in
respective water. Which cause of disuses to human.
Industrial waste water:
Tests which we are gone through have shown
very bad turbidity value the industrial waste water &
cant we used for gardening purpose and other purpose.
Because of the irrelevant values of BOD, COD, pH in
respective water. Which cause of disuses to human..
Soil fertility this very bad for our earth.
REFERENCES :
1. Shannon, M.A.; Bohn, P.W.; Elimelech, M.;
Georgiadis, J.G.; Marĩas, B.J.; Mayes, A.M. Science and
technology for water purification in the coming decades.
Nature 2008, 452, 301–310. [CrossRef] [PubMed]
2. Schlosser, C.; Strzepek, K.; Gao, X. The Future
of Global Water Stress: An Integrated Assessment. Earth’s
Future 2014, 2, 341–361. [CrossRef]
3. Cohen, B. Urban growth in developing
countries: A review of current trends and a caution
regarding existing forecasts. World Dev. 2004, 32, 23–
51. [CrossRef]
4.Machdar, I., Sekiguchi, Y., Sumino H., Ohashi
A. and H. Harada (2000) Combination of a
UASB Reactor and a Curtain-type DHS(Downflow
Hanging Sponge) Reactor as Costeffective
Sewage Treatment System for Developing Countries,
Water, Science &
Technology, 42 (3): 83-88.
5. Mann, D.D., J.C. DeBruyn and Q. Zhang
(2002). Design and evaluation of an open biofilter for
treatment of odour from swine barns during sub-zero
ambient temperatures. Canadian Biosystems
Engineering, 44: 21-26.
6. Mara, D. and S. Cairncross (1989).
Guidelines for the safe use of wastewater and excreta in
agriculture and aquaculture. Geneva: United Nations
Environmental Programme/World Health Organization.
7.Bridgewater, A.V., 2001. Thermal conversion
of biomass and waste: the status. Bio-
Energy Research Group, Aston University, Birmingham,
UK.
8.Demirbas_, A., 2004. Hydrogen-rich gas from
fruit shells via supercritical water
extraction. Int. J. Hydrogen Energy 29 (12), 1237–1243.
9.Furness, D.T., Hoggett, L.A., Judd, S.J., 20
Thermochemical treatment of sewage
10.sludge. Water Environ. J. 14 (1), 57–65.
Fytili, D., Zabaniotou, A., 2008. Utilization of sewage
sludge in EU application of
6 old and new methods – a review. Renew.
Sustain. Energy Rev. 12 (1), 116–
11.Gloyna, E.F., Li, L., McBrayer, R.N., 1994.
Engineering aspects of supercritical water oxidation.
Water Sci. Technol. 30 (9), 1–10.
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4

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IRJET- Experimental Study Cost Effective Waste Water Treatment for Micro Units

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 EXPERIMENTAL STUDY COST EFFECTIVE WASTE WATER TREATMENT FOR MICRO UNITS Roopa.D1, Dineshkumar.A2, Dinesh.T3,Gowtham.B4,Krish navin.K5 1Assistant professor, civil department, gnanamani college of technology, tamilnadu, india 2B.E Student, civil department, gnanamani college of technology, tamilnadu, india 3B.E Student, civil department, gnanamani college of technology, tamilnadu, india 4B.E Student, civil department, gnanamani college of technology, tamilnadu, india 5B.E Student, civil department, gnanamani college of technology, tamilnadu, india ---------------------------------------------------------------------***--------------------------------------------------------------------- ABSTRACT: A cost effective single unit effluent treatment plant for waste water may be developed to purify the industrial waste water and sewage waste water. Effluent sewage water is also used for reusing and recycling purpose so has reduced depending on waste water. The chemicals such as a poly aluminium chloride are being used for treatment the micro units application for a purification and water as a purification agent. The remains will be conducted known its initial various test form. Potential hydrogen (pH), suspended solid test, biaxial oxygen demand, Chemical oxygen demand, jar test apparatus, turbidity level. After the addition Poly aluminium chloride dosage will me 1g, 2g, 4g, 6g adding in the sample water 100 ml. And the sample water coagulant flocculent in waste water treatment process in micro units Key words : Sewage water ,Poly aluminium chlorides, Industrial waste water, Introduction to Wastewater Treatment Industrial wastewater treatment is any process that separates and removes contaminants from industrial process waters, or effluent. These contaminants include oils, dissolved heavy metals, suspended solids and organic compounds. Either the local municipality or the Federal Government regulates the specific contaminants.A series of limits are set to determine the suitability for discharge. These limits must be met for the water to be legally discharged.If these limits are not met, the water must be pre-treated before being discharged, to remove the majority of the regulated contaminants. Although we are technically providing pre- treatment systems, we refer to them as treatment systems. What makes Wastewater Engineers, Inc. different from other companies offering similar systems? We have a commitment to the industry. We specialize in this area, and can provide common sense advice derived from years of experience. We provide a written guarantee of our systems’ performance. We bring fluid management expertise to our clientele, providing added benefits and cost savings. We provide complete, turn-key systems, which handle the water from source to discharge. We provide excellent service after the sale, and back our systems with warranties up to 3 years. We have adopted a three-phase approach to treating industrial wastewater. The three phases are Pre-treatment, Chemical Treatment, and Post- treatment. Free Oil And Soluble Oil Often, it is necessary to remove gross oils from a waste stream prior to chemical treatment. We supply traditional belt and wheel skimmers and also an innovative honeycomb “on the flow” coalesce, which can separate up to 97% of free oils in the first pass. This range of “on the flow” coalesces are called L-OR and OR series. Emulsified oils and grease products require an emulsion breaker to achieve the floating characteristics of free oils. Once “popped” the oils may be easily skimmed or coalesced. Material & methods: Material:  Sulphuric acid    Sodium thiosulphate    Magnet sulphate    Alkaline iodide    Ferrous ammonium sulphate    Ferns sulphate    Potassium dichromate    Poly aluminium chloride  Methods:  pH scale(power of hydrogen)   BOD(bio chemical oxygen demand)  © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072  COD(chemical oxygen demand) AFTER ADDING PAC IN WATER  Suspended solids TEST  Turbidity SEAWAGE AREIAL OUTLET pH SCALE: pH is a scale of acidity from 0 to 14. It tells BOD 13.01 15.2 14.3 how acidic or alkaline a substance is. More acidic solutions have lower pH. More alkaline solutions have COD 12.3 14.6 11.2 higher pH. Substances that aren't acidic or alkaline (that is, neutral solutions) usually have a pH of 7. pH 7.3 7.65 11.7 BOD: Biochemical Oxygen Demand is an important water quality parameter because it provides an index to TABLE 2(AFTER ADDING PAC) assess the effect discharged wastewater will have on the receiving environment. The higher the BOD value, the Turbidity amount of sewage, aerial & Outlet water have greater the amount of organic matter or “food” available been tested by adding Poly aluminium chloride and noted for oxygen consuming bacteria. in the following (TABLE 3) COD: Chemical oxygen demand (COD) is a measure of Poly TURBIDITY the capacity of water to consume oxygen during the aluminium decomposition of organic matter and the oxidation of Sewage Aerial Outlet inorganic chemicals such as Ammonia and nitrite. chloride water water water SUSPENDED SOLIDS: Suspended solids refer to 1g 42.3 124.6 84.5small solid particles which remain in suspension in water as a colloid or due to the motion of the water. It is used as one indicator of water quality. 2g 18.2 110.5 81.5 TURBIDITY: The definition of Turbidity is the 3g 19.7 109.5 85.7 cloudiness or haziness of a fluid caused by suspended solids that are usually invisible to the naked eye. The 4g 23.7 109.6 92.4 measurement of Turbidity is an important test when trying 5g 28.5 108.4 93.3to determine the quality of water RESULT& DISCUSSION 6g 35.6 120.7 94.6 This test result was before adding PAC in waste TABLE 3( TURBIDITY ) water value results in (TABLE 1).and after adding PAC The above seen data (table 3) have been plotted has graph test result was in (TABLE 2). in the following BEFORE ADDING PAC IN WATER TEST SEAWAGE AREIAL OUTLET BOD 35 43.4 56.7 COD 137 140.09 151.08 pH 8.4 6.7 13.7 Fig 1(GRAPH FOR TRBIDITY TEST) TABLE: 1(BEFORE ADDIN PAC ) © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 DISCUSSION: We have gone through the BOD, COD, pH, & turbidity test for sewage water, aerial water, outlet water. It should be the result higher then permissible result. before adding poly aluminium chloride has we could its same producer for the same sewage water, aerial water, outlet water but we added poly aluminium chloride for the respective water it’s should the different result which was lower than the perimeter limits. RESULT& DISCUSSION: We testing the industrial waste water before adding poly aluminium chloride result were given in (Table 4) PERIMETER BEFORE ADDING PAC IN WATER pH 8 Poly aluminium chloride TURBIDITY 1g 120.5 2g 135.6 3g 175.6 4g 202.6 5g 307.6 6g 105.8 TABLE 6 ( TURBIDITY) BOD 4.517 COD 11.53 TABLE 4 (BEFORE ADDING PAC) PERIMETER AFTER ADDING PAC IN WATER pH 7.78 BOD 5.57 COD 14.6 TABLE 5 (AFTER ADDING PAC) Turbidity amount of industrial water have been tested by adding Poly aluminium chloride and noted in the following (TABLE 6) Fig 2(GRAPH FOR TRBIDITY TEST) DISCUSSION: We have gone through the BOD, COD, pH, & turbidity test for industrial waste water .It should be the result lower than the permissible result. Before adding poly aluminium chloride has we could its same producer for the same industrial waste water but we added poly aluminium chloride for the respective water it’s should the small amount of different result which was lower than the perimeter limits. The turbidity test was by adding poly aluminium chloride was 1g, 2g, 3g ,4g ,5g ,6g respectively given result value was very high © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 3
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 Conclusion: Sewage water: Tests which we are gone through have shown a good turbidity value the sewage water, aerial water, outlet water can we used for gardening purpose only. Because of the irrelevant values of BOD, COD, pH in respective water. Which cause of disuses to human. Industrial waste water: Tests which we are gone through have shown very bad turbidity value the industrial waste water & cant we used for gardening purpose and other purpose. Because of the irrelevant values of BOD, COD, pH in respective water. Which cause of disuses to human.. Soil fertility this very bad for our earth. REFERENCES : 1. Shannon, M.A.; Bohn, P.W.; Elimelech, M.; Georgiadis, J.G.; Marĩas, B.J.; Mayes, A.M. Science and technology for water purification in the coming decades. Nature 2008, 452, 301–310. [CrossRef] [PubMed] 2. Schlosser, C.; Strzepek, K.; Gao, X. The Future of Global Water Stress: An Integrated Assessment. Earth’s Future 2014, 2, 341–361. [CrossRef] 3. Cohen, B. Urban growth in developing countries: A review of current trends and a caution regarding existing forecasts. World Dev. 2004, 32, 23– 51. [CrossRef] 4.Machdar, I., Sekiguchi, Y., Sumino H., Ohashi A. and H. Harada (2000) Combination of a UASB Reactor and a Curtain-type DHS(Downflow Hanging Sponge) Reactor as Costeffective Sewage Treatment System for Developing Countries, Water, Science & Technology, 42 (3): 83-88. 5. Mann, D.D., J.C. DeBruyn and Q. Zhang (2002). Design and evaluation of an open biofilter for treatment of odour from swine barns during sub-zero ambient temperatures. Canadian Biosystems Engineering, 44: 21-26. 6. Mara, D. and S. Cairncross (1989). Guidelines for the safe use of wastewater and excreta in agriculture and aquaculture. Geneva: United Nations Environmental Programme/World Health Organization. 7.Bridgewater, A.V., 2001. Thermal conversion of biomass and waste: the status. Bio- Energy Research Group, Aston University, Birmingham, UK. 8.Demirbas_, A., 2004. Hydrogen-rich gas from fruit shells via supercritical water extraction. Int. J. Hydrogen Energy 29 (12), 1237–1243. 9.Furness, D.T., Hoggett, L.A., Judd, S.J., 20 Thermochemical treatment of sewage 10.sludge. Water Environ. J. 14 (1), 57–65. Fytili, D., Zabaniotou, A., 2008. Utilization of sewage sludge in EU application of 6 old and new methods – a review. Renew. Sustain. Energy Rev. 12 (1), 116– 11.Gloyna, E.F., Li, L., McBrayer, R.N., 1994. Engineering aspects of supercritical water oxidation. Water Sci. Technol. 30 (9), 1–10. © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4