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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1181
Removal of Fluoride From Drinking Water Using Tea Waste as
Adsorbent
Aparna K T1, Varsha Ashokan2
1M.Tech scholar in Environmental Engineering, Department of Civil Engineering, M. Dasan Institute of Technology,
Kozhikode, Kerala, India
2Assistant Professor, Department of Civil Engineering, M. Dasan Institute of Technology, Kozhikode, Kerala, India
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - Fluoride concentration above 1.5 ppm in
drinking water can cause serious health hazards. A low cost
and highly efficient adsorbent is prepared by using tea waste
and ability to remove fluoride from drinking water is tested.
Tea waste is cleaned and chemically treated with sulphuric
acid and formaldehyde which is then digested in alum. The
fluoride removal studies are donebyadsorptionmethodbytea
waste. The effect of contact time, pH andadsorbentdosageare
considered in batch study. For column study, a column with 50
mm diameter and height 60cm is used. The experiment is
conducted for varying bed depth of 3.5 cm, 5.4 cm, 8.9 cm and
flow rate of 5ml/min and 10ml/min. Regeneration study is
conducted by using sodium hydroxid and desorptionefficiency
of cycle 1 and cycle 2 is compared. The exhausted adsorbent is
regenerated upto two cycles.
Key Words: Fluoride, Adsorption, regeneration, column,
batch, removal.
1. INTRODUCTION
Groundwater is a renewable resource,yetthe world’ssupply
of groundwater is steadily decreasing especially in Asia and
North America [3]. Groundwater quality deterioration and
supply of safe drinking water is a major concern throughout
the world. Groundwater with high fluoride concentration
(>1.5 mg/L), according to WHO (2011), is affecting more
than 260 million people around the world [1].
Groundwater is one of the primary sources of water for
domestic and agriculture uses in Kerala. During the last two
decades, the groundwater scenario of Kerala has been
witnessing several changes [2].
2. MATERIALS AND METHODOLOGY
2.1 Adsorbent Used
Camellia sinensis is a species of evergreen shrubs from
which an aromatic bevarage called tea is made. It is
originated in borderlands of China and Northern Myanmar.
Recently the tea consumptionaroundthe worldisincreasing
which results in the production of tea leaf waste from the
industrial scale extraction of tea leaves to produce instant
tea and bottled tea drinks.
2.2 Adsorbent Preparation
In this study waste tea dust from the home is used to carry
out the experiment. The waste tea dust is collected and
washed properly to remove the milk and sugar. Then boiled
twice inorder to remove the colour. The tea waste is sun
dried to remove moisture. The dried tea waste is sieved to
get the particles having size 250µm-500µm. The oversized
particles are grounded by mortar and pestle and again
sieved.
For chemical treatment take 10 g of tea leaves and add 100
mL of 0.4 N H2SO4 and 20 ml of 30% formaldehyde. This
mixture is kept at a constant temperature of 50° C for 3
hours. Then tea leaves washed with distilled water to
remove the acid and formaldehyde. Then it is kept in hot air
oven to remove moisture. Tea leaves is then digested in 2%
alum solution. This is designated as tea leaves chemically
treated with sulphuric acid and formaldehyde.
2.3 Collection of Sample
The sample was collected from Palakkaddistrictandvarious
parameters such as pH, TDS, Total hardness, Electrical
conductivity, Alkalinity and Fluoride are tested.
2.4 Preparation of Fluoride Solution
The required sample solution is made up by diluting
Fluoride standard solution traceable to SRM (Standard
Reference Material) from NIST (National Institute of
Standards and Technology) NaF in H2O, made in Germany,
EMD Millipore Corporation.
2.5 SPADNS Spectrophotometric Method
SPADSNS spectrophotometric method is a commonly used
method for the determination of fluoride in drinking water.
This method involves the reaction of fluoride with a red
zirconium - dye solution. The basic principle of
spectrophotometric method is that each compound absorbs
or transmits light over a certain range of wavelength.
2.6 Batch Study
Batch study is conducted in order to study the effects of
various parameters like adsorbent size, adsorbent dosage,
Initial fluoride concentration, pH and contact time.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1182
And adsorbent dosage 3 g/l, 5 g/l, 7 g/l, 9g/l, 11 g/l, 13g/l,
15g/l, were considered. Initial fluoride concentrations
considered were 1 mg/l, 3 mg/l, 5 mg/l and 7 mg/l. Contact
time considered were 30, 60, 90, 120, 150 and 180 minutes.
2.7 Column Study
Inorder to investigate the practical aspect of application of
tea leaves for the removal of fluoride column study is
conducted by considering bed depth and flow rate as
parameters. The column experiment is carried out in a PVC
pipe of 50 mm diameter and 60 cm length and it is attached
to a flow control valve for adjusting the flow through
column. Bed depth of 3.5 cm, 5.4 cm and 8.9 cm are
considered. And flow rate of 5 ml/min and 10 ml/min are
considered.
2.8 Regeneration of Adsorbent
In the environmental aspect and economic aspect the
regeneration of adsorbent is important. Here regeneration
study is conducted using Sodium Hydroxide as regenerant.
After saturation of adsorbent the regenerant is passed
through the adsorbent bed and fluoride removal is checked.
The experimental setup used for regeneration was same
which was used for the break point analysis. The bed depth
of adsorbent used was 5.4 cm at a flow rate of 5 ml/min and
initial fluoride concentration of 3 mg/l.
3. RESULTS AND DISCUSSION
3.1 Testing of Raw Water
The collected sample of water is tested for various
parameters. The values had been compared with the
drinking water standards IS 10500:2012.
All the parameters excepthardnessandfluorideiswithin the
desirable limit as per Drinking water standards IS
10500:2012. The value of fluoride in the sample collected
from Palakkad district is 2.63 mg/l which is above the
desirable limit of 1 mg/l.
3.2 BATCH STUDY
In batch study Adsorbent size, Adsorbent dosage, initial
fluoride concentration pHandcontacttime wereconsidered,
the detailed results of these parameters are included in
following sections.
(i) Effect of Adsorbent size
The study of the effect of adsorbent size on fluoride removal
efficiency was carried out by using 150 µm, 300 µm, 600 µm
sized tea waste.
Chart – 1: Comparison on the effect of Adsorbent size on
the removal efficiency of Fluoride at different initial
fluoride concentrations of 1 mg/l, 3 mg/l and 5 mg/l and
adsorbent dosages of 3 g/l, 5 g/l and 7 g/l.
A maximum of 73 % removal was obtained for 150 µm sized
particles of adsorbent at an adsorbent dosage of 7 g/l and
initial fluoride concentration of 1 mg/l and 71.5 % is
obtained for 300µm sized adsorbent, but considering the
600 µm sized adsorbent the removal efficiency declines to
66.90 % at 3mg/l initial fluoride concentration.
(ii) Effect of Adsorbent Dosage
The study of the effect of adsorbent dosage on the fluoride
removal efficiency was carried out with a dosage of 3 g/l, 5
g/l, 7 g/l, 9 g/l, 11 g/l, 13 g/l, 15 g/l. The study is done by
keeping adsorbent size as 150 µm and varying initial
fluoride concentration as 3 mg/l, 5 mg/l and 7 mg/l.
Chart 2: - Effect of adsorbent dosage on Fluoride Removal
at different initial fluoride concentrations of 1 mg/l, 3
mg/l, 5 mg/l and 7 mg/l.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1183
A maximum efficiency of 76.54 % and 74.3 % was obtained
at 13 g/l adsorbent dosage, at initial fluorideconcentration3
mg/l and 5 mg/l. And 72.67 % was obtained at 7 mg/l initial
fluoride concentration.
(iii) Effect of Initial Fluoride Concentration and
Contact time
The study is conducted by varying theconcentrationsfrom1
mg/l, 3 mg/l, 5 mg/l and 7 mg/l, while keeping the
adsorbent size and dosage as 150 µm and 13 g/l.
The maximum removal efficiencyisobtainedat1mg/l initial
fluoride concentration. We can see that the percentage
removal has decreased with the increase in initial
concentration of fluoride.
Chart 3: - Effect of Initial Fluoride Concentration and
contact time on Fluoride Removal.
(iv) Effect of pH
The effect of pH on the extent of removal of the fluoride was
studied by varying the pH from 6.5, 7 and 8.5 while keeping
the adsorbent size and dosage as 150 µm and 13 g/l and
initial fluoride concentration 3 mg/l.
Chart 4: - Effect of pH
The maximum removal efficiency is obtained at a pH of 6.5
and there is no great variation in removal efficiency within
pH 6.5 to 8.5.
3.3 COLUMN STUDY
In column study we are mainly considering parameters such
as bed depth of adsorbent and flow rate.
(i) Effect of Bed Depth and Flow Rate
In this experiment the depth varies from 3.5 cm, 5.4 cm and
8.9 cm and the different flow rate choosen are 5 ml/min and
10 ml/min at time interval of 30, 90, 150 and 180 minutesat
pH 6.
Chart 5: - Effect of Bed Depth and Flow rate in fluoride
removal.
The maximum removal efficiency of 76.5 % is obtained at a
adsorbent bed depth of 5.4 cm and at a flow rate of 5 ml/min
after 150 minutes. But after 180 minutes there is a decrease
in the fluoride removal efficiency. Removal efficiency
decreased from 76.5 % to 76.41 %.
(ii)Break through Study
Inorder to find the breakthrough time of column we
conducted the study till the saturation of the column in the
first cycle.
Chart 6: - Breakthrough Curve of Original Adsorbent
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1184
A fluoride removal efficiency of 72.62 % obtained at 30
minutes and gradually increases to 75.56 % at 90 minutes
and 77.1 %removal at 150 minutes.
Chart 7: - Breakthrough Curve of Regenerated Adsorbent
3.4 REGENERATION STUDY
We need to check the possibility of regeneration before
throwing the adsorbent after it reaches the saturationpoint.
Sodium Hydroxide solution was used as regenerant.
After saturation of adsorbent column in cycle 1 is washed
with NaOH solution. Initially a fluoride removal of 66.4 %
occurs at 10 minutes, then gradually increases to 67.1 % in
30 minutes, 68.6 % in 50 minutes, 69.73 % in 70 minutes,
71.33 % in 90 minutes, 73.1 % in 110 minutes,74.9%in 130
minutes, then reduced to 74.6 % in 150 minutes and 72.8 %
in170 minutes.
In cycle 2 initially fluoride removal efficiencywas60.33 %in
10 minutes, then gradually increases to 62.51 % in 30
minutes, 63.7 % in 50 minutes, 64.11 % in 70 minutes, 65.4
% in 90 minutes, 67.5 % in110 minutes, 68.13 % in 130
minutes, then reduced to 67.12 % in 150 minutes, 65.3 % in
170 minutes.
Chart -8: Comparison of regeneration of Original
adsorbent and regenerated adsorbent
This study shows that the regeneration of adsorbent is
possible and a maximum fluoride removal of 74.9 % and
68.13 % is obtained in cycle 1 and cycle 2.
4. CONCLUSIONS
The adsorbent size used in this study are 150 µm, 300 µm
and 600 µm. The Adsorbent dosage are 3 g/l, 5 g/l, 7 g/l, 9
g/l, 11 g/l, 13 g/l and 15 g/l. The initial fluoride
concentration of 1mg/l, 3 mg/l, 5 mg/l, 7 mg/l. The time
varying from 30 minutes to 180 minutesascontacttime.The
effect of pH on fluoride removal efficiency was conducted by
varying pH from 6 to 8. Max removal efficiencywasobtained
for 150 µm adsorbent size and 13 g/l adsorbent dosage with
3 mg/l initial fluoride concentration at 150 minutes at pH 6.
In the column study the parameters mainlyconsideredwere
flow rate and Bed depth. Flow rate choosen for the column
study were 5 ml/min and 10 ml/min.Thebeddepthchoosen
were 3.5 cm, 5.4 cm and 8.9 cm. As the first cycle completed
a maximum fluoride removal efficiency of 77.1 % was
obtained at a bed depth of 5.4 cm and flow rate of 5 ml/min
in breakthrough analysis. And as the second cycle has
completed a maximum removal efficiency of 74.31 % was
also obtained at a bed depth of 5.4 cm and flow rate of 5
ml/min.
In regeneration study of cycle 1 the fluoride removal of 66.4
% was obtained at 10 minutes the gradually increased to
74.9 % at 130 minutes.
In cycle 2 the fluoride removal of 60.33 % was obtained at
10 minutes then gradually increased to 68.13 % at 130
minutes. After 130 minutes the removal efficiency reduced
to 67.12 % at 150 minutes and then declined to 65.3 % at
170 minutes.
From this sets of experiment, we can concludethattea waste
can be used as an adsorbent for removing fluoride from
water,as it shows great removal efficiency and regeneration
characteristics.
REFERENCES
[1] Amini, M., Mueller, K., Abbaspour, K. C., Rosenberg, T.,
Afyuni, M., Moller, K.N., Sarr, M., Johnson, C. A., (2008)
Statistical modeling of global geogenic fluoride
contamination in groundwaters, Environmental science
and technology, 42, 3662-3668.
[2] E. Shaji & Bindu, & Viju, J. & Thambi, D.S. (2007). High
fluoride in groundwater of Palghat District, Kerala.
Current Science. 92. 240-245.
[3] Gleeson, T., Wada, Y., Bierkens, M. F., Van Beek, L. P.,
(2012) Water balance of global aquifers revealed by
ground water footprint, Nature 488 (7410), 197-200.

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Removal of Fluoride From Drinking Water Using Tea Waste as Adsorbent

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1181 Removal of Fluoride From Drinking Water Using Tea Waste as Adsorbent Aparna K T1, Varsha Ashokan2 1M.Tech scholar in Environmental Engineering, Department of Civil Engineering, M. Dasan Institute of Technology, Kozhikode, Kerala, India 2Assistant Professor, Department of Civil Engineering, M. Dasan Institute of Technology, Kozhikode, Kerala, India ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - Fluoride concentration above 1.5 ppm in drinking water can cause serious health hazards. A low cost and highly efficient adsorbent is prepared by using tea waste and ability to remove fluoride from drinking water is tested. Tea waste is cleaned and chemically treated with sulphuric acid and formaldehyde which is then digested in alum. The fluoride removal studies are donebyadsorptionmethodbytea waste. The effect of contact time, pH andadsorbentdosageare considered in batch study. For column study, a column with 50 mm diameter and height 60cm is used. The experiment is conducted for varying bed depth of 3.5 cm, 5.4 cm, 8.9 cm and flow rate of 5ml/min and 10ml/min. Regeneration study is conducted by using sodium hydroxid and desorptionefficiency of cycle 1 and cycle 2 is compared. The exhausted adsorbent is regenerated upto two cycles. Key Words: Fluoride, Adsorption, regeneration, column, batch, removal. 1. INTRODUCTION Groundwater is a renewable resource,yetthe world’ssupply of groundwater is steadily decreasing especially in Asia and North America [3]. Groundwater quality deterioration and supply of safe drinking water is a major concern throughout the world. Groundwater with high fluoride concentration (>1.5 mg/L), according to WHO (2011), is affecting more than 260 million people around the world [1]. Groundwater is one of the primary sources of water for domestic and agriculture uses in Kerala. During the last two decades, the groundwater scenario of Kerala has been witnessing several changes [2]. 2. MATERIALS AND METHODOLOGY 2.1 Adsorbent Used Camellia sinensis is a species of evergreen shrubs from which an aromatic bevarage called tea is made. It is originated in borderlands of China and Northern Myanmar. Recently the tea consumptionaroundthe worldisincreasing which results in the production of tea leaf waste from the industrial scale extraction of tea leaves to produce instant tea and bottled tea drinks. 2.2 Adsorbent Preparation In this study waste tea dust from the home is used to carry out the experiment. The waste tea dust is collected and washed properly to remove the milk and sugar. Then boiled twice inorder to remove the colour. The tea waste is sun dried to remove moisture. The dried tea waste is sieved to get the particles having size 250µm-500µm. The oversized particles are grounded by mortar and pestle and again sieved. For chemical treatment take 10 g of tea leaves and add 100 mL of 0.4 N H2SO4 and 20 ml of 30% formaldehyde. This mixture is kept at a constant temperature of 50° C for 3 hours. Then tea leaves washed with distilled water to remove the acid and formaldehyde. Then it is kept in hot air oven to remove moisture. Tea leaves is then digested in 2% alum solution. This is designated as tea leaves chemically treated with sulphuric acid and formaldehyde. 2.3 Collection of Sample The sample was collected from Palakkaddistrictandvarious parameters such as pH, TDS, Total hardness, Electrical conductivity, Alkalinity and Fluoride are tested. 2.4 Preparation of Fluoride Solution The required sample solution is made up by diluting Fluoride standard solution traceable to SRM (Standard Reference Material) from NIST (National Institute of Standards and Technology) NaF in H2O, made in Germany, EMD Millipore Corporation. 2.5 SPADNS Spectrophotometric Method SPADSNS spectrophotometric method is a commonly used method for the determination of fluoride in drinking water. This method involves the reaction of fluoride with a red zirconium - dye solution. The basic principle of spectrophotometric method is that each compound absorbs or transmits light over a certain range of wavelength. 2.6 Batch Study Batch study is conducted in order to study the effects of various parameters like adsorbent size, adsorbent dosage, Initial fluoride concentration, pH and contact time.
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1182 And adsorbent dosage 3 g/l, 5 g/l, 7 g/l, 9g/l, 11 g/l, 13g/l, 15g/l, were considered. Initial fluoride concentrations considered were 1 mg/l, 3 mg/l, 5 mg/l and 7 mg/l. Contact time considered were 30, 60, 90, 120, 150 and 180 minutes. 2.7 Column Study Inorder to investigate the practical aspect of application of tea leaves for the removal of fluoride column study is conducted by considering bed depth and flow rate as parameters. The column experiment is carried out in a PVC pipe of 50 mm diameter and 60 cm length and it is attached to a flow control valve for adjusting the flow through column. Bed depth of 3.5 cm, 5.4 cm and 8.9 cm are considered. And flow rate of 5 ml/min and 10 ml/min are considered. 2.8 Regeneration of Adsorbent In the environmental aspect and economic aspect the regeneration of adsorbent is important. Here regeneration study is conducted using Sodium Hydroxide as regenerant. After saturation of adsorbent the regenerant is passed through the adsorbent bed and fluoride removal is checked. The experimental setup used for regeneration was same which was used for the break point analysis. The bed depth of adsorbent used was 5.4 cm at a flow rate of 5 ml/min and initial fluoride concentration of 3 mg/l. 3. RESULTS AND DISCUSSION 3.1 Testing of Raw Water The collected sample of water is tested for various parameters. The values had been compared with the drinking water standards IS 10500:2012. All the parameters excepthardnessandfluorideiswithin the desirable limit as per Drinking water standards IS 10500:2012. The value of fluoride in the sample collected from Palakkad district is 2.63 mg/l which is above the desirable limit of 1 mg/l. 3.2 BATCH STUDY In batch study Adsorbent size, Adsorbent dosage, initial fluoride concentration pHandcontacttime wereconsidered, the detailed results of these parameters are included in following sections. (i) Effect of Adsorbent size The study of the effect of adsorbent size on fluoride removal efficiency was carried out by using 150 µm, 300 µm, 600 µm sized tea waste. Chart – 1: Comparison on the effect of Adsorbent size on the removal efficiency of Fluoride at different initial fluoride concentrations of 1 mg/l, 3 mg/l and 5 mg/l and adsorbent dosages of 3 g/l, 5 g/l and 7 g/l. A maximum of 73 % removal was obtained for 150 µm sized particles of adsorbent at an adsorbent dosage of 7 g/l and initial fluoride concentration of 1 mg/l and 71.5 % is obtained for 300µm sized adsorbent, but considering the 600 µm sized adsorbent the removal efficiency declines to 66.90 % at 3mg/l initial fluoride concentration. (ii) Effect of Adsorbent Dosage The study of the effect of adsorbent dosage on the fluoride removal efficiency was carried out with a dosage of 3 g/l, 5 g/l, 7 g/l, 9 g/l, 11 g/l, 13 g/l, 15 g/l. The study is done by keeping adsorbent size as 150 µm and varying initial fluoride concentration as 3 mg/l, 5 mg/l and 7 mg/l. Chart 2: - Effect of adsorbent dosage on Fluoride Removal at different initial fluoride concentrations of 1 mg/l, 3 mg/l, 5 mg/l and 7 mg/l.
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1183 A maximum efficiency of 76.54 % and 74.3 % was obtained at 13 g/l adsorbent dosage, at initial fluorideconcentration3 mg/l and 5 mg/l. And 72.67 % was obtained at 7 mg/l initial fluoride concentration. (iii) Effect of Initial Fluoride Concentration and Contact time The study is conducted by varying theconcentrationsfrom1 mg/l, 3 mg/l, 5 mg/l and 7 mg/l, while keeping the adsorbent size and dosage as 150 µm and 13 g/l. The maximum removal efficiencyisobtainedat1mg/l initial fluoride concentration. We can see that the percentage removal has decreased with the increase in initial concentration of fluoride. Chart 3: - Effect of Initial Fluoride Concentration and contact time on Fluoride Removal. (iv) Effect of pH The effect of pH on the extent of removal of the fluoride was studied by varying the pH from 6.5, 7 and 8.5 while keeping the adsorbent size and dosage as 150 µm and 13 g/l and initial fluoride concentration 3 mg/l. Chart 4: - Effect of pH The maximum removal efficiency is obtained at a pH of 6.5 and there is no great variation in removal efficiency within pH 6.5 to 8.5. 3.3 COLUMN STUDY In column study we are mainly considering parameters such as bed depth of adsorbent and flow rate. (i) Effect of Bed Depth and Flow Rate In this experiment the depth varies from 3.5 cm, 5.4 cm and 8.9 cm and the different flow rate choosen are 5 ml/min and 10 ml/min at time interval of 30, 90, 150 and 180 minutesat pH 6. Chart 5: - Effect of Bed Depth and Flow rate in fluoride removal. The maximum removal efficiency of 76.5 % is obtained at a adsorbent bed depth of 5.4 cm and at a flow rate of 5 ml/min after 150 minutes. But after 180 minutes there is a decrease in the fluoride removal efficiency. Removal efficiency decreased from 76.5 % to 76.41 %. (ii)Break through Study Inorder to find the breakthrough time of column we conducted the study till the saturation of the column in the first cycle. Chart 6: - Breakthrough Curve of Original Adsorbent
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 05 | May 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 1184 A fluoride removal efficiency of 72.62 % obtained at 30 minutes and gradually increases to 75.56 % at 90 minutes and 77.1 %removal at 150 minutes. Chart 7: - Breakthrough Curve of Regenerated Adsorbent 3.4 REGENERATION STUDY We need to check the possibility of regeneration before throwing the adsorbent after it reaches the saturationpoint. Sodium Hydroxide solution was used as regenerant. After saturation of adsorbent column in cycle 1 is washed with NaOH solution. Initially a fluoride removal of 66.4 % occurs at 10 minutes, then gradually increases to 67.1 % in 30 minutes, 68.6 % in 50 minutes, 69.73 % in 70 minutes, 71.33 % in 90 minutes, 73.1 % in 110 minutes,74.9%in 130 minutes, then reduced to 74.6 % in 150 minutes and 72.8 % in170 minutes. In cycle 2 initially fluoride removal efficiencywas60.33 %in 10 minutes, then gradually increases to 62.51 % in 30 minutes, 63.7 % in 50 minutes, 64.11 % in 70 minutes, 65.4 % in 90 minutes, 67.5 % in110 minutes, 68.13 % in 130 minutes, then reduced to 67.12 % in 150 minutes, 65.3 % in 170 minutes. Chart -8: Comparison of regeneration of Original adsorbent and regenerated adsorbent This study shows that the regeneration of adsorbent is possible and a maximum fluoride removal of 74.9 % and 68.13 % is obtained in cycle 1 and cycle 2. 4. CONCLUSIONS The adsorbent size used in this study are 150 µm, 300 µm and 600 µm. The Adsorbent dosage are 3 g/l, 5 g/l, 7 g/l, 9 g/l, 11 g/l, 13 g/l and 15 g/l. The initial fluoride concentration of 1mg/l, 3 mg/l, 5 mg/l, 7 mg/l. The time varying from 30 minutes to 180 minutesascontacttime.The effect of pH on fluoride removal efficiency was conducted by varying pH from 6 to 8. Max removal efficiencywasobtained for 150 µm adsorbent size and 13 g/l adsorbent dosage with 3 mg/l initial fluoride concentration at 150 minutes at pH 6. In the column study the parameters mainlyconsideredwere flow rate and Bed depth. Flow rate choosen for the column study were 5 ml/min and 10 ml/min.Thebeddepthchoosen were 3.5 cm, 5.4 cm and 8.9 cm. As the first cycle completed a maximum fluoride removal efficiency of 77.1 % was obtained at a bed depth of 5.4 cm and flow rate of 5 ml/min in breakthrough analysis. And as the second cycle has completed a maximum removal efficiency of 74.31 % was also obtained at a bed depth of 5.4 cm and flow rate of 5 ml/min. In regeneration study of cycle 1 the fluoride removal of 66.4 % was obtained at 10 minutes the gradually increased to 74.9 % at 130 minutes. In cycle 2 the fluoride removal of 60.33 % was obtained at 10 minutes then gradually increased to 68.13 % at 130 minutes. After 130 minutes the removal efficiency reduced to 67.12 % at 150 minutes and then declined to 65.3 % at 170 minutes. From this sets of experiment, we can concludethattea waste can be used as an adsorbent for removing fluoride from water,as it shows great removal efficiency and regeneration characteristics. REFERENCES [1] Amini, M., Mueller, K., Abbaspour, K. C., Rosenberg, T., Afyuni, M., Moller, K.N., Sarr, M., Johnson, C. A., (2008) Statistical modeling of global geogenic fluoride contamination in groundwaters, Environmental science and technology, 42, 3662-3668. [2] E. Shaji & Bindu, & Viju, J. & Thambi, D.S. (2007). High fluoride in groundwater of Palghat District, Kerala. Current Science. 92. 240-245. [3] Gleeson, T., Wada, Y., Bierkens, M. F., Van Beek, L. P., (2012) Water balance of global aquifers revealed by ground water footprint, Nature 488 (7410), 197-200.