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1
DEFLUORIDATION BY LOW
COST BIO-ADSORBENTS
2
 PRESENTED BY,
 NAYANA.D
 11144229
GUIDED BY ,
SIVA BALA P
ASST. PROFESSOR,CE
COLLEGE OF
ENGINEERING,PATHANAPURAM
CONTENTS
3
1. FLUORIDE-ILLEFFECTS,CONTAMINATION IN INDIA
2. METHODS OF DEFLUORIDATION
3. ADSORPTION-ADVANTAGES
4. LOW COST ADSORBENTS
5. CASE STUDY-MORINGA OLEIFERA A NATURAL BIO-
ADSORBENT
FLUORIDE
4
 Compound form of fluorine(F)
 SOURCES OF FLUORIDE
1.Ground water –Fluoride bearing rocks
&industrial discharges
2.Food products
3.Medicaments & cosmetics
The permissible limits of fluoride
concentration in drinking water
5
NAME OF ORGANISATION PERMISSIBLE LIMIT
Bureau of Indian standards(BIS) 0.6-1.2 mg/lit
World Health Organisation (WHO) 1-1.5 mg/lit
Indian Council of Medical
Research(ICMR)
1 mg/lit
6
FLUORIDE CONTAMINATION IN
GROUNDWATER
Excessive fluoride concentration reported in 28
developed and developing countries
India –
 19 states are affected by fluoride problem
 was first reported in 1937 in the state of U.P
 The desert-ridden water scarce state of
Rajasthan tops the affected states
7
 7
FIG :Fluorosis
prevalent states
MOST AFFECTED
STATES
RAJASTHAN
GUJARAT
ANDHARA
PREDESH
7
FLUORIDE-”A DOUBLE EDGED
SWORD”
8
ADEQUATE INTAKE
 prevent tooth decay and cavities
Maintenance of healthy bones
EXCESSIVE INTAKE
Dental fluorosis
Muscular –skeletal fluorosis
Damages pineal gland
Affects reproductive system and
intelligence
Thyroid disorder
Neurological damage
FLUORIDATION
DEFLUORIDATION
DEFLUORIDATION
9
Adjustment of level of fluoride in
drinking water to the optimal level
METHODS OF
DEFLUORIDATION
10
Precipitation methods
Ion exchange process
Membrane filtration process
Nano-filtration
Electro-coagulation
Adsorption
1. PRECIPITATION METHODS
11
Addition of chemicals (coagulants) and precipitation of
soluble salts of fluoride
Limestone,alum,lime,Poly Aluminium chloride,Poly
aluminium Hydroxy sulphate
Eg: Nalgonda Technique
Limitations-Time consuming, requires more
diligence, large dosage of aluminium sulphate,sludge
transfer issue
2.ION EXCHANGE PROCESS
12
 Materials
1.Bone
exchange of carbonate radicals with fluoride
2.Bone char
consists of calcium phosphate and carbonate
3.Ion exchange resins
anion exchangers-Eg. Polyanion(NCL)
cation exchangers-Eg.Carbion,Polystyrene
4.Activated alumina
consists of aluminium oxide (Al2O3).
3.MEMBRANE FILTRATION PROCESS
13
Reverse osmosis (RO)
the pressure is exerted on one side of the semi-permeable
membrane which forces the water across the membrane
leaving the pollutants behind
Electro dialysis
the membranes allow the ions to pass but not the water
4.NANO FILTRATION
14
 Nano filtration membranes have high retention of
charged particles.
 Requires less pressure and capital
 Limitations-
1.expensive
2.complicated
5.ELECTRO-COAGUlATION
15
Utilizes electricity and sacrificial anodes to form the
active coagulants
Advantages-less space, no chemical storage, no pH
adjustments
Disadvantages-expensive and complicated
LIMITATIONS
16
1. High operational cost
2. Maintenance cost
3. Low fluoride removal capacities
4. Lack of selectivity for fluoride
5. Undesirable effects on water quality
6. Generation of large volumes of sludge
7. Complicated procedures involved in the treatment.
ADSORPTION
17
Adsorption is the bond of molecules species from
bulk solution for a surface of a solid by physical or
chemical forces.
Applications in water treatment
1. Removal of taste and odour causing compounds
2. Synthetic organic chemicals(SOCs)
3. Colour forming organics
4. Disinfection by products(DBPs)
5. Heavy metals
18
Fig: Various adsorbents used for defluoridation
18
19
 3 phases of adsorption of fluoride.
1. diffusion or transport of fluoride ions to the external
surface of the adsorbent
2. adsorption of fluoride ions on to particle surfaces
3. the adsorbed fluoride ions probably exchange with
the structural elements inside adsorbent particles
ADVANTAGES OF ADSORPTION
20
1. High selectivity of adsorbents.
2. Low cost in installation and maintenance thus economic
compared to other methods of defluoridation
3. High efficiency, high productivity of fluoride removal and can
remove up to 90% of fluoride.
4. Easy post-treatment after adsorption.
5. Adsorption units are simple in their operation and design
Contn.............
21
6. Eco-friendly nature
7. Lack of sludge production
8. It is applicable in removal of fluoride even at low
concentration.
9. This method is also popular due to wide range of
availability of adsorbents.
10. Adsorption technique is efficient and can remove
ions over an extensive variety of pH to a lower
leftover concentration than precipitation
VARIOUS LOW COST ADSORBENTS
22
 Industrial, agricultural wastes ,natural plant
products used as adsorbents
23
Name of
adsorbent
pH Dosage
(g/L)
Contact
time
(hr)
Removal
percentag
e
Reference
Clay material 2 5 to 10 3 40-50 Ravikumar
and
Nazeebkhan(
2015)
Granular
activated
carbon and
sewage
sludge
neutral GAC-4
SS-3
3 Poundyl and
Sandhya
(2015)
Tea ash 6 0.8 1 51.3-77.6 Mondal.et.al.
,(2011)
Pumic 7 20 3 74.64 Malakootian
et.al.,(2011)
24
Neem leaves 2 10 1 90 Goswami(201
5)
Bark of
Babool
8 5 8 77.4 Mamdawan
Baggase Dust 6 1-20 5 84.4 Gupta.et.al.,
Rice husk 2-10 10 2 75 Deshmukh
et.al(2009)
Citrus
limonum(lem
on)leaf
2-8 1-10 2.4 70 V.Jomae.et.al
(2014)
Devadaru
leaf powder
7 7-8 3 77 Bharali
&Bhattachary
25
Eggshell powder 2-6 5 2 94 R Bhavnik&N
K Mondal
Chalk powder 2-7 2 2 86
Maize husk
fly ash
2 0.04 2 86 Jadhav A V
Neem stem
charcoal
5 .1-.6 3 94 Chakrabarty
&Sharma(201
2)
ADVANTAGES OF LOW COST
ADSORBENTS
26
1. Offers efficiency of 50-96%
2. Cheap and easily available compared to
conventional adsorbents
3. Need less maintenance and supervision
4. Used adsorbents can be used as filler material,thus
disposed easily and safely.
27
CASE STUDY:DEFLUORIDATION
BY MORINGA OLEIFERA-A
NATURAL ADSORBENT
28
Powdered seeds
Moringa oleifera seeds
Moringa oleifera plant
EXPERIMENT
29
1. Materials used
Moringa oleifera seed powder
1 N nitric acid
0.5 N sodium hydroxide
2. Experimental setup and procedure
The fluoride removal studies by adsorption were conducted in 250 ml
conical flask using 100 ml of synthetic water sample containing different
pH and initial concentrations of fluoride ion. In these conical flasks
adsorbent with varied dosage was added. Then the contact period was
given for different particle sizes. After giving a required contact time, the
contents of the flasks were filtered using Whatmann’s filter paper number
41. The filtrate was used for fluoride ion estimation using SPADNS method.
The above procedure was repeated for different pH, contact times,
adsorbent doses, particle sizes and different initial fluoride ion
concentrations
1.Optimum pH
30
Sl.No pH Acid washed
powder
Alkali washed
powder
%removal
efficiency
% removal
efficiency
1 1 39 -
2 2 31 31
3 4 24 37
4 6 20 41
5 8 13 49.5
6 10 12 51
2. Optimal contact time
31
 Adsorbent dosage = 2.5 gm/lit
 pH =8
Sr. No. Contact time 600 μ 212 μ
% removal
efficiency
%removal
efficiency
1 30 39 53
2 60 48 62
3 90 56 68
4 120 61 70
5 150 62 70
3. Optimal adsorbent dosage
32
pH = 8
Optimum contact time = 2.5 hrs (600µ)
= 2 hrs (212 µ)
Sr. No. Absorbent
dose
(mg)
600 μ 212 μ
% removal
efficiency
%removal
efficiency
1 100 47 48
2 200 58 62
3 300 61 67
4 400 68 76
OBSERVATIONS
33
1. The alkali treated Moringa Oleifera seed powder was
found better than acid treated Moringa Oleifera seed
powder for fluoride ion removal.
2. The removal by adsorption increases as the pH
value increases.
3. The removal by adsorption was found to be
optimum at adsorbent dose of 400 mg/lit.
4. The optimum contact times were 2 hrs and 2.5hrs
for 212 μ and 600 μ respectively.
CONCLUSION
34
Cost is of major consideration in developing
countries like India
Hence adsorption process using low cost adsorbents
that are abundant and easily available have been
investigated
35
SCOPE OF FUTURE WORK
The present study have to be extended for
1. Variety of other adsorbents
2. Different particle size
3. Mixture of adsorbents
4. Large scale applications
REFERENCE
36
1. Suman Mann, Dr.Anubha Mandal, Performance of Low-Cost Adsorbents for the Removal of fluoride
ions – An overview , International Journal of Engineering Science and Innovative Technology
(IJESIT) Volume 3, Issue 3, May 2014
2. Prerna Kumari ,Effective bio-adsorbents for removal of fluoride from water:a review,International
Journal of Advance Research in Science and Engineering,Vol.No.4,August 2015
3. C M Vivek Vardha and J Karthikeyan ,Removal of fluoride from water using low cost
materials,Fifteenth International Water Technology Conference,2011,Egypt
4. Suman Mann, Dr.Anubha Mandal, Performance of Low-Cost Adsorbents for the Removal of fluoride
ions – An overview, International Journal of Engineering Science and Innovative Technology (IJESIT)
Volume 3, Issue 3, May 2014
5. N. Gandhi, D. Sirisha, K.B. Chandra Shekar and Smita Asthana, Removal Of Fluoride From Water
And Waste Water By Using Low Cost Adsorbents, International Journal of ChemTech Research
CODEN( USA): IJCRGG ISSN : 0974-4290 Vol.4, No.4, pp 1646-1653, Oct-Dec 2012
37

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DEFLUORIDATION BY BIOADSORBENTS

  • 1. 1
  • 2. DEFLUORIDATION BY LOW COST BIO-ADSORBENTS 2  PRESENTED BY,  NAYANA.D  11144229 GUIDED BY , SIVA BALA P ASST. PROFESSOR,CE COLLEGE OF ENGINEERING,PATHANAPURAM
  • 3. CONTENTS 3 1. FLUORIDE-ILLEFFECTS,CONTAMINATION IN INDIA 2. METHODS OF DEFLUORIDATION 3. ADSORPTION-ADVANTAGES 4. LOW COST ADSORBENTS 5. CASE STUDY-MORINGA OLEIFERA A NATURAL BIO- ADSORBENT
  • 4. FLUORIDE 4  Compound form of fluorine(F)  SOURCES OF FLUORIDE 1.Ground water –Fluoride bearing rocks &industrial discharges 2.Food products 3.Medicaments & cosmetics
  • 5. The permissible limits of fluoride concentration in drinking water 5 NAME OF ORGANISATION PERMISSIBLE LIMIT Bureau of Indian standards(BIS) 0.6-1.2 mg/lit World Health Organisation (WHO) 1-1.5 mg/lit Indian Council of Medical Research(ICMR) 1 mg/lit
  • 6. 6 FLUORIDE CONTAMINATION IN GROUNDWATER Excessive fluoride concentration reported in 28 developed and developing countries India –  19 states are affected by fluoride problem  was first reported in 1937 in the state of U.P  The desert-ridden water scarce state of Rajasthan tops the affected states
  • 7. 7  7 FIG :Fluorosis prevalent states MOST AFFECTED STATES RAJASTHAN GUJARAT ANDHARA PREDESH 7
  • 8. FLUORIDE-”A DOUBLE EDGED SWORD” 8 ADEQUATE INTAKE  prevent tooth decay and cavities Maintenance of healthy bones EXCESSIVE INTAKE Dental fluorosis Muscular –skeletal fluorosis Damages pineal gland Affects reproductive system and intelligence Thyroid disorder Neurological damage FLUORIDATION DEFLUORIDATION
  • 9. DEFLUORIDATION 9 Adjustment of level of fluoride in drinking water to the optimal level
  • 10. METHODS OF DEFLUORIDATION 10 Precipitation methods Ion exchange process Membrane filtration process Nano-filtration Electro-coagulation Adsorption
  • 11. 1. PRECIPITATION METHODS 11 Addition of chemicals (coagulants) and precipitation of soluble salts of fluoride Limestone,alum,lime,Poly Aluminium chloride,Poly aluminium Hydroxy sulphate Eg: Nalgonda Technique Limitations-Time consuming, requires more diligence, large dosage of aluminium sulphate,sludge transfer issue
  • 12. 2.ION EXCHANGE PROCESS 12  Materials 1.Bone exchange of carbonate radicals with fluoride 2.Bone char consists of calcium phosphate and carbonate 3.Ion exchange resins anion exchangers-Eg. Polyanion(NCL) cation exchangers-Eg.Carbion,Polystyrene 4.Activated alumina consists of aluminium oxide (Al2O3).
  • 13. 3.MEMBRANE FILTRATION PROCESS 13 Reverse osmosis (RO) the pressure is exerted on one side of the semi-permeable membrane which forces the water across the membrane leaving the pollutants behind Electro dialysis the membranes allow the ions to pass but not the water
  • 14. 4.NANO FILTRATION 14  Nano filtration membranes have high retention of charged particles.  Requires less pressure and capital  Limitations- 1.expensive 2.complicated
  • 15. 5.ELECTRO-COAGUlATION 15 Utilizes electricity and sacrificial anodes to form the active coagulants Advantages-less space, no chemical storage, no pH adjustments Disadvantages-expensive and complicated
  • 16. LIMITATIONS 16 1. High operational cost 2. Maintenance cost 3. Low fluoride removal capacities 4. Lack of selectivity for fluoride 5. Undesirable effects on water quality 6. Generation of large volumes of sludge 7. Complicated procedures involved in the treatment.
  • 17. ADSORPTION 17 Adsorption is the bond of molecules species from bulk solution for a surface of a solid by physical or chemical forces. Applications in water treatment 1. Removal of taste and odour causing compounds 2. Synthetic organic chemicals(SOCs) 3. Colour forming organics 4. Disinfection by products(DBPs) 5. Heavy metals
  • 18. 18 Fig: Various adsorbents used for defluoridation 18
  • 19. 19  3 phases of adsorption of fluoride. 1. diffusion or transport of fluoride ions to the external surface of the adsorbent 2. adsorption of fluoride ions on to particle surfaces 3. the adsorbed fluoride ions probably exchange with the structural elements inside adsorbent particles
  • 20. ADVANTAGES OF ADSORPTION 20 1. High selectivity of adsorbents. 2. Low cost in installation and maintenance thus economic compared to other methods of defluoridation 3. High efficiency, high productivity of fluoride removal and can remove up to 90% of fluoride. 4. Easy post-treatment after adsorption. 5. Adsorption units are simple in their operation and design
  • 21. Contn............. 21 6. Eco-friendly nature 7. Lack of sludge production 8. It is applicable in removal of fluoride even at low concentration. 9. This method is also popular due to wide range of availability of adsorbents. 10. Adsorption technique is efficient and can remove ions over an extensive variety of pH to a lower leftover concentration than precipitation
  • 22. VARIOUS LOW COST ADSORBENTS 22  Industrial, agricultural wastes ,natural plant products used as adsorbents
  • 23. 23 Name of adsorbent pH Dosage (g/L) Contact time (hr) Removal percentag e Reference Clay material 2 5 to 10 3 40-50 Ravikumar and Nazeebkhan( 2015) Granular activated carbon and sewage sludge neutral GAC-4 SS-3 3 Poundyl and Sandhya (2015) Tea ash 6 0.8 1 51.3-77.6 Mondal.et.al. ,(2011) Pumic 7 20 3 74.64 Malakootian et.al.,(2011)
  • 24. 24 Neem leaves 2 10 1 90 Goswami(201 5) Bark of Babool 8 5 8 77.4 Mamdawan Baggase Dust 6 1-20 5 84.4 Gupta.et.al., Rice husk 2-10 10 2 75 Deshmukh et.al(2009) Citrus limonum(lem on)leaf 2-8 1-10 2.4 70 V.Jomae.et.al (2014) Devadaru leaf powder 7 7-8 3 77 Bharali &Bhattachary
  • 25. 25 Eggshell powder 2-6 5 2 94 R Bhavnik&N K Mondal Chalk powder 2-7 2 2 86 Maize husk fly ash 2 0.04 2 86 Jadhav A V Neem stem charcoal 5 .1-.6 3 94 Chakrabarty &Sharma(201 2)
  • 26. ADVANTAGES OF LOW COST ADSORBENTS 26 1. Offers efficiency of 50-96% 2. Cheap and easily available compared to conventional adsorbents 3. Need less maintenance and supervision 4. Used adsorbents can be used as filler material,thus disposed easily and safely.
  • 27. 27 CASE STUDY:DEFLUORIDATION BY MORINGA OLEIFERA-A NATURAL ADSORBENT
  • 28. 28 Powdered seeds Moringa oleifera seeds Moringa oleifera plant
  • 29. EXPERIMENT 29 1. Materials used Moringa oleifera seed powder 1 N nitric acid 0.5 N sodium hydroxide 2. Experimental setup and procedure The fluoride removal studies by adsorption were conducted in 250 ml conical flask using 100 ml of synthetic water sample containing different pH and initial concentrations of fluoride ion. In these conical flasks adsorbent with varied dosage was added. Then the contact period was given for different particle sizes. After giving a required contact time, the contents of the flasks were filtered using Whatmann’s filter paper number 41. The filtrate was used for fluoride ion estimation using SPADNS method. The above procedure was repeated for different pH, contact times, adsorbent doses, particle sizes and different initial fluoride ion concentrations
  • 30. 1.Optimum pH 30 Sl.No pH Acid washed powder Alkali washed powder %removal efficiency % removal efficiency 1 1 39 - 2 2 31 31 3 4 24 37 4 6 20 41 5 8 13 49.5 6 10 12 51
  • 31. 2. Optimal contact time 31  Adsorbent dosage = 2.5 gm/lit  pH =8 Sr. No. Contact time 600 μ 212 μ % removal efficiency %removal efficiency 1 30 39 53 2 60 48 62 3 90 56 68 4 120 61 70 5 150 62 70
  • 32. 3. Optimal adsorbent dosage 32 pH = 8 Optimum contact time = 2.5 hrs (600µ) = 2 hrs (212 µ) Sr. No. Absorbent dose (mg) 600 μ 212 μ % removal efficiency %removal efficiency 1 100 47 48 2 200 58 62 3 300 61 67 4 400 68 76
  • 33. OBSERVATIONS 33 1. The alkali treated Moringa Oleifera seed powder was found better than acid treated Moringa Oleifera seed powder for fluoride ion removal. 2. The removal by adsorption increases as the pH value increases. 3. The removal by adsorption was found to be optimum at adsorbent dose of 400 mg/lit. 4. The optimum contact times were 2 hrs and 2.5hrs for 212 μ and 600 μ respectively.
  • 34. CONCLUSION 34 Cost is of major consideration in developing countries like India Hence adsorption process using low cost adsorbents that are abundant and easily available have been investigated
  • 35. 35 SCOPE OF FUTURE WORK The present study have to be extended for 1. Variety of other adsorbents 2. Different particle size 3. Mixture of adsorbents 4. Large scale applications
  • 36. REFERENCE 36 1. Suman Mann, Dr.Anubha Mandal, Performance of Low-Cost Adsorbents for the Removal of fluoride ions – An overview , International Journal of Engineering Science and Innovative Technology (IJESIT) Volume 3, Issue 3, May 2014 2. Prerna Kumari ,Effective bio-adsorbents for removal of fluoride from water:a review,International Journal of Advance Research in Science and Engineering,Vol.No.4,August 2015 3. C M Vivek Vardha and J Karthikeyan ,Removal of fluoride from water using low cost materials,Fifteenth International Water Technology Conference,2011,Egypt 4. Suman Mann, Dr.Anubha Mandal, Performance of Low-Cost Adsorbents for the Removal of fluoride ions – An overview, International Journal of Engineering Science and Innovative Technology (IJESIT) Volume 3, Issue 3, May 2014 5. N. Gandhi, D. Sirisha, K.B. Chandra Shekar and Smita Asthana, Removal Of Fluoride From Water And Waste Water By Using Low Cost Adsorbents, International Journal of ChemTech Research CODEN( USA): IJCRGG ISSN : 0974-4290 Vol.4, No.4, pp 1646-1653, Oct-Dec 2012
  • 37. 37