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IWWA 51st Annual Convention Indore
TREATMENT of OILY WASTEWATER in CUTTING FLUID of a
METAL INDUSTRY in INDORE CITY
Sonal Garg Dr. D.J.Killedar Apurva Pandey
Asst. Professor Professor Former M.Tech student
CE-AMD CE-AMD CE-AMD
S.G.S.I.T.S S.G.S.I.T.S S.G.S.I.T.S
INDORE [M.P.] INDORE [M.P.] INDORE [M.P.]
INTRODUCTION
• Wastewater obtained from industries is generally much more polluted than
domestic or even commercial wastewater. Still several industries try to
discharge their effluents into our natural river streams through unauthorized
direct discharges.
• Such a tendency on the part of the industries may pollute the entire river water
to a great extent thereby making its purification almost an impossible task.
Sometimes the industries discharge their polluted wastewater into municipal
sewers thereby making the task of treating that municipal sewage a very
difficult and costly exercise.
• The industries are therefore generally prevented by legal laws from discharging
their untreated effluents. It therefore become necessary for the industries to treat
their wastewater in the individual treatment plant before discharging their
effluent either on land or lakes or rivers or in municipal sewers.
• Since, oil and grease present in oily wastewater consist of free oil, TSS and
TDS which are harmful for natural environment, so when untreated wastewater
is discharged into natural river or streams, it proves hazardous for aquatic life.
CUTTING FLUID
• Cutting fluid is a type of coolant and lubricant designed
specifically for metal working processes, such
as machining and stamping.
• There are various kinds of cutting fluids, which include
oils, oil-water emulsions, pastes, gels, aerosols (mists),
and air or other gases.
• They may be made from petroleum distillates, animal
fats, plant oils, water and air, or other raw ingredients.
Depending on context and on which type of cutting fluid
is being considered, it may be referred to as cutting
fluid, cutting oil, cutting compound, coolant, or lubricant.
• In order to protect our natural environment, oily wastewater
needs to be treated so as to minimize the concentration of
TDS, TSS and oil & grease present in it.
• The project has been taken to find ways to treat oily
wastewater present in cutting fluid economically by chemical
treatment.
• This study was done to determine the coagulant best suited for
chemical treatment of emulsified oil, it’s optimum pH and
optimum dosage for removal of TSS & TDS by jar test.
NEED OF STUDY
STUDY AREA
The field work was conducted at “BHARAT METAL ENGINEERS”
industry situated at Rambali Nagar industrial area near Scheme No. 51 at
Indore city.
METHODOLOGY ADOPTED
Treatability tests for removal of different parameters using coagulants by Jar
Test
Determination of optimum pH of raw wastewater by acidification
Preparation of different doses of coagulants
Selection of different coagulants
Determination of physico-chemical characteristics of raw effluent
Collection of sample
Characteristics of raw effluent of cutting fluid
S. No. Parameters Concentration
1 pH 8.5
2 COD 700 mg/l
3 TSS 6750 mg/l
4 TDS 32400 mg/l
5 Oil & Grease 173.20 mg/l
Selection of Coagulants
Coagulants
Alum
(Al2(SO4)3·18H2O)
Ferric Chloride
(FeCl3.6H2O)
Poly Aluminum
Chloride
(Aln(OH)m(Cl3)n-m)
Weight of coagulants add in 25 ml distilled water to make standard solution
S. No.
Standard solution
concentration
(in mg/L)
Alum
(in gm)
FeCl3
(in gm)
PAC
(in gm)
1 10 0.75 0.14 0.18
2 20 1.50 0.28 0.36
3 30 2.25 0.42 0.54
4 40 3.00 0.56 0.72
5 50 3.75 0.70 0.90
Preparations of different doses of coagulants
Determination of optimum pH of wastewater by
acidification
Check the concentration of oil & grease in bottom layer decanted water at
different pH values
Mixture separates in 2 layers
Oily material concentrates in upper layer Water separates on bottom layer
Place the sample in separating funnel & allow to settle
pH of sample was reduced from 8.5 to 2, 3, 4, 5, 6, 7 and
8 by adding appropriate amount of conc. HCl (Acid
allows the oil droplets to agglomerate)
100 ml of wastewater sample was collected
Oil and water separation was done by destabilizing cutting fluid emulsion and
separating it in two layers, one is water and other is oil material present by
addition of acid.
S. No. Parameters
Wastewater characteristics at different pH after acidification
pH=8.5 pH= 2 pH=3 pH=4 pH=5 pH =6 pH =7 pH= 8
1
Oil & Grease
(in mg/l)
173.20 60 62.60 58.6 74.3 68.2 72.7 75.8
2
TDS
(in mg/l)
32400 15900 24620 27600 31900 11450 26500 28690
3
TSS
(in mg/l)
6750 1400 1600 1300 1000 1100 1250 1500
4
COD
(in mg/l)
700 640 600 680 520 600 m 380 560
Treatability tests for removal of different physico-
chemical parameters using coagulants by Jar Test
Jar test method determines optimum dosage of coagulant (single/mixed),
coagulant aids for removal of TSS, TDS and oil & grease caused by colloidal
and non settleable particles followed by sedimentation under quiescent
condition.
RM:
100 rpm, 1 min
SM:
30 rpm, 20 min
RESULTS & DISSCUSSIONS
Comparative results of all coagulants for removal of
Oil & grease
Raw wastewater value = 173.20 mg/l
S. No.
Coagulant
Dosage
(in mg/l)
Oil &
Grease
(in mg/l)
%
Reduction
Oil &
Grease
(in mg/l)
%
Reduction
Oil &
Grease
(in mg/l)
%
Reduction
Alum FeCl3 PAC
1 10 134.71 22.22 84.14 72.22 25.67 85.18
2 20 121.93 29.6 57.84 66.6 48.15 72.2
3 30 141.16 18.5 67.37 61.1 19.39 88.8
4 40 115.33 33.4 83.31 51.9 22.46 87.03
5 50 121.58 29.8 80.19 53.7 32.08 81.48
Comparative Graph for % Removal of Oil & Grease by all coagulants at different
dosages
Comparative results of all coagulants for removal of
TSS
Raw Wastewater value = 6750 mg/l
S. No.
Coagulant
Dosage
(in mg/L)
TSS
(in mg/l)
%
Reduction
TSS
(in mg/l)
%
Reduction
TSS
(in mg/l)
%
Reduction
Alum FeCl3 PAC
1 10 3375 50 3152 53.6 2255 66.6
2 20 3152 53.3 2930 56.6 2025 70
3 30 2660 60.6 1667 75.3 722 89.3
4 40 2255 66.6 2045 69.7 1802 73.3
5 50 2700 60 2477 63.3 1985 70.6
Comparative Graph for % Removal of Total Suspended Solids by all coagulants at
different dosages
Comparative results of all coagulants for removal
of TDS
Raw Wastewater value = 32400 mg/l
S. No.
Coagulant
Dosage
(in mg/L)
TDS
(in mg/l)
%
Reduction
TDS
(in mg/l)
%
Reduction
TDS
(in mg/l)
%
Reduction
Alum FeCl3 PAC
1 10 20218 37.6 19861 38.7 18727 42.2
2 20 25758 20.5 23846 26.4 22388 30.9
3 30 26341 18.7 26471 18.3 22615 30.2
4 40 27378 15.5 25110 22.5 22162 31.6
5 50 29290 9.6 24980 22.9 23749 26.7
Comparative Graph for % Removal of Total Suspended Solids by all coagulants at
different dosages
Sample before treatment Sample after treatment
CONCLUSIONS
On the basis of study of some aspects of treatment of emulsion oil present in
cutting fluid by acidification and coagulation through chemical treatment, the
following conclusions can be drawn-
 In this study, it has been found that the ‘Acid cracking’ is a suitable method to
remove the maximum oil droplets at pH=4 from the effluent.
 The Oil & Grease concentration decreased drastically in the acidification
process as compared to the decrease in concentration of TSS & TDS.
 The coagulation process after acidification process applied in order to remove
contaminants from wastewater appeared very effective.
 The study shows that Poly aluminum chloride is very efficient in removal of
the TSS and TDS from oily wastewater as compared to other coagulants used.
 It was found that among three coagulants studied viz. Alum, FeCl3 and Poly
aluminum chloride, Poly aluminum chloride gave the best result and removed
maximum concentration of contaminates i.e. 89.6% TSS, 42.2% TDS and
88.8% Oil and grease.
THANK YOU

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Treatment of Industrial Oily Waste Water

  • 1. IWWA 51st Annual Convention Indore TREATMENT of OILY WASTEWATER in CUTTING FLUID of a METAL INDUSTRY in INDORE CITY Sonal Garg Dr. D.J.Killedar Apurva Pandey Asst. Professor Professor Former M.Tech student CE-AMD CE-AMD CE-AMD S.G.S.I.T.S S.G.S.I.T.S S.G.S.I.T.S INDORE [M.P.] INDORE [M.P.] INDORE [M.P.]
  • 2. INTRODUCTION • Wastewater obtained from industries is generally much more polluted than domestic or even commercial wastewater. Still several industries try to discharge their effluents into our natural river streams through unauthorized direct discharges. • Such a tendency on the part of the industries may pollute the entire river water to a great extent thereby making its purification almost an impossible task. Sometimes the industries discharge their polluted wastewater into municipal sewers thereby making the task of treating that municipal sewage a very difficult and costly exercise. • The industries are therefore generally prevented by legal laws from discharging their untreated effluents. It therefore become necessary for the industries to treat their wastewater in the individual treatment plant before discharging their effluent either on land or lakes or rivers or in municipal sewers. • Since, oil and grease present in oily wastewater consist of free oil, TSS and TDS which are harmful for natural environment, so when untreated wastewater is discharged into natural river or streams, it proves hazardous for aquatic life.
  • 3. CUTTING FLUID • Cutting fluid is a type of coolant and lubricant designed specifically for metal working processes, such as machining and stamping. • There are various kinds of cutting fluids, which include oils, oil-water emulsions, pastes, gels, aerosols (mists), and air or other gases. • They may be made from petroleum distillates, animal fats, plant oils, water and air, or other raw ingredients. Depending on context and on which type of cutting fluid is being considered, it may be referred to as cutting fluid, cutting oil, cutting compound, coolant, or lubricant.
  • 4. • In order to protect our natural environment, oily wastewater needs to be treated so as to minimize the concentration of TDS, TSS and oil & grease present in it. • The project has been taken to find ways to treat oily wastewater present in cutting fluid economically by chemical treatment. • This study was done to determine the coagulant best suited for chemical treatment of emulsified oil, it’s optimum pH and optimum dosage for removal of TSS & TDS by jar test. NEED OF STUDY
  • 5. STUDY AREA The field work was conducted at “BHARAT METAL ENGINEERS” industry situated at Rambali Nagar industrial area near Scheme No. 51 at Indore city.
  • 6. METHODOLOGY ADOPTED Treatability tests for removal of different parameters using coagulants by Jar Test Determination of optimum pH of raw wastewater by acidification Preparation of different doses of coagulants Selection of different coagulants Determination of physico-chemical characteristics of raw effluent Collection of sample
  • 7. Characteristics of raw effluent of cutting fluid S. No. Parameters Concentration 1 pH 8.5 2 COD 700 mg/l 3 TSS 6750 mg/l 4 TDS 32400 mg/l 5 Oil & Grease 173.20 mg/l
  • 8. Selection of Coagulants Coagulants Alum (Al2(SO4)3·18H2O) Ferric Chloride (FeCl3.6H2O) Poly Aluminum Chloride (Aln(OH)m(Cl3)n-m)
  • 9. Weight of coagulants add in 25 ml distilled water to make standard solution S. No. Standard solution concentration (in mg/L) Alum (in gm) FeCl3 (in gm) PAC (in gm) 1 10 0.75 0.14 0.18 2 20 1.50 0.28 0.36 3 30 2.25 0.42 0.54 4 40 3.00 0.56 0.72 5 50 3.75 0.70 0.90 Preparations of different doses of coagulants
  • 10. Determination of optimum pH of wastewater by acidification Check the concentration of oil & grease in bottom layer decanted water at different pH values Mixture separates in 2 layers Oily material concentrates in upper layer Water separates on bottom layer Place the sample in separating funnel & allow to settle pH of sample was reduced from 8.5 to 2, 3, 4, 5, 6, 7 and 8 by adding appropriate amount of conc. HCl (Acid allows the oil droplets to agglomerate) 100 ml of wastewater sample was collected Oil and water separation was done by destabilizing cutting fluid emulsion and separating it in two layers, one is water and other is oil material present by addition of acid.
  • 11. S. No. Parameters Wastewater characteristics at different pH after acidification pH=8.5 pH= 2 pH=3 pH=4 pH=5 pH =6 pH =7 pH= 8 1 Oil & Grease (in mg/l) 173.20 60 62.60 58.6 74.3 68.2 72.7 75.8 2 TDS (in mg/l) 32400 15900 24620 27600 31900 11450 26500 28690 3 TSS (in mg/l) 6750 1400 1600 1300 1000 1100 1250 1500 4 COD (in mg/l) 700 640 600 680 520 600 m 380 560
  • 12. Treatability tests for removal of different physico- chemical parameters using coagulants by Jar Test Jar test method determines optimum dosage of coagulant (single/mixed), coagulant aids for removal of TSS, TDS and oil & grease caused by colloidal and non settleable particles followed by sedimentation under quiescent condition. RM: 100 rpm, 1 min SM: 30 rpm, 20 min
  • 14. Comparative results of all coagulants for removal of Oil & grease Raw wastewater value = 173.20 mg/l S. No. Coagulant Dosage (in mg/l) Oil & Grease (in mg/l) % Reduction Oil & Grease (in mg/l) % Reduction Oil & Grease (in mg/l) % Reduction Alum FeCl3 PAC 1 10 134.71 22.22 84.14 72.22 25.67 85.18 2 20 121.93 29.6 57.84 66.6 48.15 72.2 3 30 141.16 18.5 67.37 61.1 19.39 88.8 4 40 115.33 33.4 83.31 51.9 22.46 87.03 5 50 121.58 29.8 80.19 53.7 32.08 81.48
  • 15. Comparative Graph for % Removal of Oil & Grease by all coagulants at different dosages
  • 16. Comparative results of all coagulants for removal of TSS Raw Wastewater value = 6750 mg/l S. No. Coagulant Dosage (in mg/L) TSS (in mg/l) % Reduction TSS (in mg/l) % Reduction TSS (in mg/l) % Reduction Alum FeCl3 PAC 1 10 3375 50 3152 53.6 2255 66.6 2 20 3152 53.3 2930 56.6 2025 70 3 30 2660 60.6 1667 75.3 722 89.3 4 40 2255 66.6 2045 69.7 1802 73.3 5 50 2700 60 2477 63.3 1985 70.6
  • 17. Comparative Graph for % Removal of Total Suspended Solids by all coagulants at different dosages
  • 18. Comparative results of all coagulants for removal of TDS Raw Wastewater value = 32400 mg/l S. No. Coagulant Dosage (in mg/L) TDS (in mg/l) % Reduction TDS (in mg/l) % Reduction TDS (in mg/l) % Reduction Alum FeCl3 PAC 1 10 20218 37.6 19861 38.7 18727 42.2 2 20 25758 20.5 23846 26.4 22388 30.9 3 30 26341 18.7 26471 18.3 22615 30.2 4 40 27378 15.5 25110 22.5 22162 31.6 5 50 29290 9.6 24980 22.9 23749 26.7
  • 19. Comparative Graph for % Removal of Total Suspended Solids by all coagulants at different dosages
  • 20. Sample before treatment Sample after treatment
  • 21. CONCLUSIONS On the basis of study of some aspects of treatment of emulsion oil present in cutting fluid by acidification and coagulation through chemical treatment, the following conclusions can be drawn-  In this study, it has been found that the ‘Acid cracking’ is a suitable method to remove the maximum oil droplets at pH=4 from the effluent.  The Oil & Grease concentration decreased drastically in the acidification process as compared to the decrease in concentration of TSS & TDS.  The coagulation process after acidification process applied in order to remove contaminants from wastewater appeared very effective.  The study shows that Poly aluminum chloride is very efficient in removal of the TSS and TDS from oily wastewater as compared to other coagulants used.  It was found that among three coagulants studied viz. Alum, FeCl3 and Poly aluminum chloride, Poly aluminum chloride gave the best result and removed maximum concentration of contaminates i.e. 89.6% TSS, 42.2% TDS and 88.8% Oil and grease.