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Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and
                   Applications (IJERA) ISSN: 2248-9622 www.ijera.com
                          Vol. 2, Issue 4, July-August 2012, pp.334-338
        Removal Of Fluoride From Ground Water By Using Adsorbent
                  Bhagyashree M Mamilwar *, A.G.Bhole **, A.M.Sudame***
     *M.Tech Student IV Sem, Department of Civil Engineering, G.H.Raisoni College of Engineering, C.R.P.F Gate
                           No.3,Digdoah Hills, Hingna Road,RTMNU ,Nagpur 440016.(India)
       **Former Professor & Head of Civil Engineering,Vishwesaraya National Institute Of Technology Nagpur.
   ***Associate Professor, Department of Chemistry, G.H.Raisoni College of Engineering, C.R.P.F Gate No.3,Digdoah.
                                 Hills, Hingna Road,RTMNU, Nagpur 440016.(India)



ABSTRACT
         Presence of Fluoride in water is safe and               2.0 . Material and Method of study
 effective when used as directed, but it can be harmful          2.1 Material
 at high doses and at low concentration. In the present                    Adsorption of Fluoride was studied using bark of
 paper bark of babool as a adsorbent is used for                 babool as an Adsorbent. The bark is collected and grinded
 removal of fluoride from groundwater. Defluoridation            to a fine powder and sieved through the sieve of 150 µ size
 of groundwater using bark of babool as an adsorbent             and Washed by double distilled water in orbital shaking
 was studied in batch process. The effects of controlling        incubator at 300C, 150rpm for 24Hrs. After washing dried
 parameters like optimum dose ,contact time, pH,                 in oven under the temperature of 1000C for 24 hrs and kept
 temperature etc. were study. The result shows that              it in muffle furnace at 7000 C for 2 Hrs. After removing
 bark of babool of 5g/L accomplished a removal of                sample is again washed by double distilled water. Then the
 77.04% of Fluoride from a 5mg/L of Fluoride                     material was used as an adsorbent for the removal of
 concentration at normal pH of 8.0 requiring an                  Fluoride.
 equilibrium time of 8 hours. The experimental
 adsorption data fitted with Langmuir and Freundlich             2.2 Method Of Study
 adsorption isotherms. The pseudo-second-order                             The batch adsorption experiments were
 kinetic model fitted well as compared to pseudo first-          conducted to study.Fluoride stock solution was prepared
 order model. The effects of co-existing ions present in         by dissolving 221 mg anhydrous sodium fluoride in l litre
 groundwater were also studied. Comparison was made              of distilled water in volumetric flask. Initially 5 mg/L
 with simulated and field water.                                 fluoride concentration solution is taken for the study. The
                                                                 temperature range for the studies was from 20 ºC to 40 ºC.
                                                                 Batch studies were performed at the shaking rate of 150
Keywords - Adsorption, fluoride removal, Isotherm pH,            rpm. For each experimental run, 50 ml aqueous solution of
            Temperature.                                         the known 5mg/L fluoride concentration was taken in 100
                                                                 ml capacity plastic bottles containing 50 ml of fluoride
I. INTRODUCTION                                                  solution. These bottles were agitated at a constant shaking
          Water need is precious because it is the main          rate of 150 rpm in a temperature controlled orbital shaker
source of human as well as animals needs. Despite Earth’s        maintained at a constant temperature. The pH of the
appearance of watery abundance, less than 1% of the water        adsorbate solution was adjusted by using 0.1 N HCl or 0.1
on Earth is actually fresh and usable. Fluorine is widely        N NaOH aqueous solutions. To check whether the
spread in nature and is a common constituent of most soils       equilibrium has been attained, the samples were
and rocks, plants and animals. It is the 13th most abundant      withdrawn from the flasks at different time intervals.
element, averaging 650 mg/L in the earth crust                   Fluoride removal efficiency was found out by using Ion
[1].Exposure of living organisms to above normal                 Selective Electrode Method.
concentrations of fluoride may result in alteration of the
organism’s biochemistry and morphology,which restrict            3.0 Results & Discussions
the organism’s ability to maintain its ecological position
directly or indirectly. [2]. Global prevalence of fluorosis is   3.1 Effect of Adsorbent Dose
reported to be about 32% [3]. Some governments are not                    The effect of adsorbent dose studied at
yet fully aware of the fluoride problem or convinced of its      1,2.5,5,10,20 g/L From Fig.1 result shows that the
adverse impact on their populations. Efforts are therefore       optimum dose of adsorbent was found 5 g/L for fluoride
needed to support more research on the subject and               concentration of 5mg/L,which gives 77.04% fluoride ion
promote systematic policy responses by governments. [4].         removal efficiency was required to bring down the fluoride
The permissible limit of fluoride level is generally 1–          level between 1.0 – 1.5 mg/L as per WHO guidelines. An
1.5mg/L. In addition, WHO noted that mottling of teeth           adsorbent dose of 5 g/L was used for further study.
(i.e. dental fluorosis) is sometimes associated with fluoride
levels in drinking-water above 1.5 mg/L and crippling
skeletal fluorosis can ensue when fluoride levels exceed 10
mg/L.


                                                                                                            334 | P a g e
Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and
                   Applications (IJERA) ISSN: 2248-9622 www.ijera.com
                          Vol. 2, Issue 4, July-August 2012, pp.334-338
                                                               concentration in water was 1.12 mg/L which was within
                                                               permissible limit (1-1.5 mg/L ).After this the adsorption of
                                                               fluoride increased as the contact time increased but the
                                                               remaining concentration of fluoride range was below 1
                                                               mg/L . Hence 480 min. (8 hrs) was selected the time of
                                                               contact at 303K.




Fig.1: Fluoride Conc.– 5mg/L ,pH–8.0,Temp – 30OC,time
                  – 24 hrs, rpm – 150

3.2 Effect of pH
         To find pH effect the study was conducted from
pH 2 to12 in acidic and alkaline conditions respectively.
The graphical representation is shown in Fig.2 found that      Fig.3: Fluoride Conc.– 5mg/L , Dose of adsorbent– 5g/L,
the removal of fluoride was increased up to pH 8 and then                 pH – 8.0,Temp – 30OC, rpm – 150
decreases.Highest adsorption of fluoride was found to be
70.6% to 75.6 % in the pH range 6.0 and 8.0. It is seen that   3.4 Effect of Different Initial Concentration
the sorption of fluoride is good in the pH range 6.0-                     The effect of different initial concentration was
8.0.This may be due to neutralization of the negative          studied at 1,3,5,10,15 mg/L.From Fig.4 it shows that
charge at the surface of adsorbent material by greater         adsorption of fluoride decreased with the increased in
hydrogen concentration at lower pH values. In the acidic       adsorption concentration because capacity of adsorbent
pH range, the amount of fluoride adsorbed slightly             material get exhausted slowly with the increase in the
decreased and this can be due to the formation of weak         initial fluoride concentration.
hydrofluoric acid. In the alkaline condition pH range there
was sharply drop in adsorption which may be due to the
competition of the hydroxyl ions with the fluoride for
adsorption.




                                                               Fig. 4 : Dose of adsorbent – 5g/L, pH –8.0, Temp – 30OC,
                                                                            optimum time – 8 hrs, rpm– 150
 Fig.2: Fluoride Conc.– 5mg/L , Dose of adsorbent– 5g/L
         ,Temp – 30OC,time – 24 hrs, rpm – 150                 3.5 Effect of Co-Existing Ions
                                                                        Present of Co-existing ions in grounwater cause
3.3 Effect of Time of Contact                                  positive or adsversed effect on adsorption. The study was
         The graphical representation is shown in Fig.3 it     carried out on anions and cations (Mg ++, Fe ++, NO3 & SO4
shows that as the contact time increased the adsorption of     )
fluoride also increased. After 480 min. (8 hrs.) the
adsorption of fluoride was 77.6 % and remaining fluoride

                                                                                                           335 | P a g e
Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and
                   Applications (IJERA) ISSN: 2248-9622 www.ijera.com
                          Vol. 2, Issue 4, July-August 2012, pp.334-338
                         100
                          90
 % Removal of Fluoride



                          80
                          70
                          60
                          50                                Mg++
                          40
                          30
                          20
                          10
                           0
                               100      200        400      600
                                     Co-Existing Ion (mg/l)


 Fig. 5 : Fluoride Conc. – 5mg/L , Dose of adsorbent–              Fig. 8: Fluoride Conc. – 5mg/L , Dose of adsorbent –5g/L,
 5g/L, Temp – 30OC,optimum time – 8 hrs, rpm – 150                           Temp – 30OC, optimum time – 8 hrs rpm – 150

                                                                   3.6 ADSORPTION MODEL
                                                                            The adsorption of Fluoride can be mathematically
                                                                   expressed in terms of adsorption isotherms. Adsorption
                                                                   isotherm data are commonly fitted to the Langmuir model
                                                                   (equation 1) and the Freundlich model (equation 2).Study
                                                                   carried   on various dose of adsorbent and various
                                                                   temperature.
                                                                          Qm K ACe
                                                                   Qe                           ....................(1)
                                                                          1  K ACe
                                                                            Where,

                                                                              Qe       = Amount of adsorbate adsorbed per
                                                                                         unit amount of adsorbent at
                                                                                         equilibrium.
 Fig. 6 : Fluoride Conc. – 5mg/L , Dose of adsorbent –
 5g/L, Temp – 30OC, optimum time– 8 hrs, rpm – 150                            Qm       = Amount of adsorbate adsorbed per unit
                                                                                          amount of adsorbent required            for
                                                                                          monolayer adsorption.

                                                                             K A = Constant related to enthalpy of
                                                                                          adsorption.

                                                                                             Ce = Concentration of adsorbate
                                                                                   solution at equilibrium.

                                                                                   1
                                                                    Qe  K F Ce n                …................(2)

                                                                            where ,

                                                                            K F and n are the constants
  Fig. 7: Fluoride Conc. – 5mg/L, Dose of adsorbent
 5g/L,Temp – 30OC, optimum time – 8 hrs, rpm – 150                           Ce = the concentration of adsorbate solution               at
                                                                            equilibrium




                                                                                                                           336 | P a g e
Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and
                   Applications (IJERA) ISSN: 2248-9622 www.ijera.com
                          Vol. 2, Issue 4, July-August 2012, pp.334-338

                                                                             qmax
                                                                 Temp.                  b           r             R2
                                                                            (mg/g)


                                                                 293K       1.891       0.1509      0.5698        0.8722


                                                                 303K       4.17 3      0.1584      0.5580        0.9179


                                                                 313K       4.728       0.203       0.4961        0.9639

        Fig. 9: Fluoride Conc. – 5mg/L , rpm – 150
                                                                   Table 2:Freundlich adsorption isotherm parameters for
                                                                           fluoride adsorption by bark of babool

                                                                 3.7 Kinetic Adsorption Model
                                                                 It is apparent from the values of correlation coefficients
                                                                 that the pseudo-second-order kinetic model fitted well as
                                                                 compared to pseudo first-order model .




     Fig. 10: Langmuir Fit for Adsorption of Fluoride at
            293K, 303K and 313K




                                                                 Fig.12 :Pseudo-first kinetic model for fluoride removal by
                                                                                       bark of babool




Fig. 11: Freundlich Fit for Adsorption of Fluoride at
293K, 303K and 313K

 Temp      Kf ( mg/g)       n          1/n               R2

 293K         1.192       1.172        0.85             0.9701

 303K         2.847       1.046       0.955             0.8804

 313K         1.333       0.879       0.937             0.869

Table 1: Langmuir Adsorption isotherm parameters for             Fig.13:Pseudo-Second kinetic model for fluoride removal
fluoride adsorption by bark of babool                                              by bark of babool

                                                                 3.8 Comparison of Simulated and Field Water


                                                                                                             337 | P a g e
Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and
                   Applications (IJERA) ISSN: 2248-9622 www.ijera.com
                          Vol. 2, Issue 4, July-August 2012, pp.334-338
The adsorption experiments were study on simulated and
field water containing fluoride concentration of 5mg/L, at      [4]    Ensar Oguz,“Adsorption of fluoride on gas concrete
optimum pH-8.0, by adding optimum dose of adsorbent                    materials”, Journal of Hazardous Materials,
(5g/L) which was put inside the bottles in 50 ml. which                Vol.B117,(2005), 227–233.
operated at 150 rpm and with constant temperature 303K
up to 8hrs. (Time of equilibrium). From Fig.14 the              [5]    Mohanty.Auroprasad,National         institute    of
removal of fluoride was more in simulated water than the               Technology, Rourkela, “Developement of a Hybrid
fluoride present in field water. This may be due to the                Material for the removal of fluoride from water” 1-
presence of cat ions and anions present in field water.                6.

                                                                [6]    Patil S. S, “ Assessments of Concentration of
                                                                       Fluoride from Drinking Water in Yavatmal District
                                                                       in Vidarbha Region by Ion Selective Electrode
                                                                       Method” IE(I) Journal, Vol. 88,(2007), 1-3.

                                                                [7]    Valach R and Sedlacek F “Changes in the use of
                                                                       biologically  effective  fluorides  and    the
                                                                       consequences”. Cas Lek Cesk. Vol.129, (1990),
                                                                       769-777.

                                                                [8]    Raichur A.M, Basu M.J, “Adsorption of fluoride
                                                                       onto mixed rare earth oxides”, Sep. Purif. Technol.
                                                                       Vol.24, (2001), 121–127.

                                                                [9]    Agarwal, M., Rai, K., Shrivastav, R., Dass, S.
                                                                       “Defluoridation of water using amended clay”. J.
                                                                       Cleaner Produc.Vol.11, (2003), 439–444.

                                                                [10]   Ensar Oguz ,“Adsorption of fluoride on gas
                                                                       concrete materials”, Journal of Hazardous
                                                                       Materials, Vol.B117,(2005), 227–233.
      Fig.14:Fluoride Conc. – 5mg/L , Dose of adsorbent–
           5g/L, Temp – 30OC,time– 8 hrs, rpm – 150             [11]   Zhang V and Cao S R, “Coal Burning Induced
                                                                       Endemic     Fluorosis  in China. Fluoride”,
CONCLUSION                                                             Vol.29,(1996),207-211.
          From the present result it is concluded that bark
of babool as a adsorbent are promising materials for
Fluoride removal. These adsorbent material is locally
available but requires Pre-treatment to raw material before
using for removal of fluoride. Optimum dose of bark of
babool      was found 5g/L for removal of fluoride
concentration of 5 mg/L. Adsorption capacity was more in
the pH range of 6-8.Optimum time of contact was found 8
hrs. The removal increased with time and adsorbent dose,
but with higher initial concentration decreased with time
and adsorbent dose. The present study on defluoridation
using bark of babool shows that the equilibrium data fits
better to Langmuir isotherm as compared with Freundlich
isotherm.The pseudo-second-order kinetic model fitted
well as compared to pseudo first-order model .


REFERENCES
[1]      Maheshwari R.C.Meenakshi, “Fluoride in drinking
         water and its removal” Journal of Hazardous
         Materials, Vol.B137, (2006), 456–463.

[2]      Chaturvedi A.k., Yadava K.P, Pathak K.C, Singh
         V.N, “Defluoridation of water by adsorption on fly
         ash”, Defluoridation, Air Soil Pollut, 49,(1989).

[3]      Bhargava, D.S., Killedar, D.J., “Fluoride adsorption
         on fishbone charcoal through a moving media
         adsorber.” Vol.26, 1992, 781–788.
                                                                                                           338 | P a g e

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Ay24334338

  • 1. Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 2, Issue 4, July-August 2012, pp.334-338 Removal Of Fluoride From Ground Water By Using Adsorbent Bhagyashree M Mamilwar *, A.G.Bhole **, A.M.Sudame*** *M.Tech Student IV Sem, Department of Civil Engineering, G.H.Raisoni College of Engineering, C.R.P.F Gate No.3,Digdoah Hills, Hingna Road,RTMNU ,Nagpur 440016.(India) **Former Professor & Head of Civil Engineering,Vishwesaraya National Institute Of Technology Nagpur. ***Associate Professor, Department of Chemistry, G.H.Raisoni College of Engineering, C.R.P.F Gate No.3,Digdoah. Hills, Hingna Road,RTMNU, Nagpur 440016.(India) ABSTRACT Presence of Fluoride in water is safe and 2.0 . Material and Method of study effective when used as directed, but it can be harmful 2.1 Material at high doses and at low concentration. In the present Adsorption of Fluoride was studied using bark of paper bark of babool as a adsorbent is used for babool as an Adsorbent. The bark is collected and grinded removal of fluoride from groundwater. Defluoridation to a fine powder and sieved through the sieve of 150 µ size of groundwater using bark of babool as an adsorbent and Washed by double distilled water in orbital shaking was studied in batch process. The effects of controlling incubator at 300C, 150rpm for 24Hrs. After washing dried parameters like optimum dose ,contact time, pH, in oven under the temperature of 1000C for 24 hrs and kept temperature etc. were study. The result shows that it in muffle furnace at 7000 C for 2 Hrs. After removing bark of babool of 5g/L accomplished a removal of sample is again washed by double distilled water. Then the 77.04% of Fluoride from a 5mg/L of Fluoride material was used as an adsorbent for the removal of concentration at normal pH of 8.0 requiring an Fluoride. equilibrium time of 8 hours. The experimental adsorption data fitted with Langmuir and Freundlich 2.2 Method Of Study adsorption isotherms. The pseudo-second-order The batch adsorption experiments were kinetic model fitted well as compared to pseudo first- conducted to study.Fluoride stock solution was prepared order model. The effects of co-existing ions present in by dissolving 221 mg anhydrous sodium fluoride in l litre groundwater were also studied. Comparison was made of distilled water in volumetric flask. Initially 5 mg/L with simulated and field water. fluoride concentration solution is taken for the study. The temperature range for the studies was from 20 ºC to 40 ºC. Batch studies were performed at the shaking rate of 150 Keywords - Adsorption, fluoride removal, Isotherm pH, rpm. For each experimental run, 50 ml aqueous solution of Temperature. the known 5mg/L fluoride concentration was taken in 100 ml capacity plastic bottles containing 50 ml of fluoride I. INTRODUCTION solution. These bottles were agitated at a constant shaking Water need is precious because it is the main rate of 150 rpm in a temperature controlled orbital shaker source of human as well as animals needs. Despite Earth’s maintained at a constant temperature. The pH of the appearance of watery abundance, less than 1% of the water adsorbate solution was adjusted by using 0.1 N HCl or 0.1 on Earth is actually fresh and usable. Fluorine is widely N NaOH aqueous solutions. To check whether the spread in nature and is a common constituent of most soils equilibrium has been attained, the samples were and rocks, plants and animals. It is the 13th most abundant withdrawn from the flasks at different time intervals. element, averaging 650 mg/L in the earth crust Fluoride removal efficiency was found out by using Ion [1].Exposure of living organisms to above normal Selective Electrode Method. concentrations of fluoride may result in alteration of the organism’s biochemistry and morphology,which restrict 3.0 Results & Discussions the organism’s ability to maintain its ecological position directly or indirectly. [2]. Global prevalence of fluorosis is 3.1 Effect of Adsorbent Dose reported to be about 32% [3]. Some governments are not The effect of adsorbent dose studied at yet fully aware of the fluoride problem or convinced of its 1,2.5,5,10,20 g/L From Fig.1 result shows that the adverse impact on their populations. Efforts are therefore optimum dose of adsorbent was found 5 g/L for fluoride needed to support more research on the subject and concentration of 5mg/L,which gives 77.04% fluoride ion promote systematic policy responses by governments. [4]. removal efficiency was required to bring down the fluoride The permissible limit of fluoride level is generally 1– level between 1.0 – 1.5 mg/L as per WHO guidelines. An 1.5mg/L. In addition, WHO noted that mottling of teeth adsorbent dose of 5 g/L was used for further study. (i.e. dental fluorosis) is sometimes associated with fluoride levels in drinking-water above 1.5 mg/L and crippling skeletal fluorosis can ensue when fluoride levels exceed 10 mg/L. 334 | P a g e
  • 2. Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 2, Issue 4, July-August 2012, pp.334-338 concentration in water was 1.12 mg/L which was within permissible limit (1-1.5 mg/L ).After this the adsorption of fluoride increased as the contact time increased but the remaining concentration of fluoride range was below 1 mg/L . Hence 480 min. (8 hrs) was selected the time of contact at 303K. Fig.1: Fluoride Conc.– 5mg/L ,pH–8.0,Temp – 30OC,time – 24 hrs, rpm – 150 3.2 Effect of pH To find pH effect the study was conducted from pH 2 to12 in acidic and alkaline conditions respectively. The graphical representation is shown in Fig.2 found that Fig.3: Fluoride Conc.– 5mg/L , Dose of adsorbent– 5g/L, the removal of fluoride was increased up to pH 8 and then pH – 8.0,Temp – 30OC, rpm – 150 decreases.Highest adsorption of fluoride was found to be 70.6% to 75.6 % in the pH range 6.0 and 8.0. It is seen that 3.4 Effect of Different Initial Concentration the sorption of fluoride is good in the pH range 6.0- The effect of different initial concentration was 8.0.This may be due to neutralization of the negative studied at 1,3,5,10,15 mg/L.From Fig.4 it shows that charge at the surface of adsorbent material by greater adsorption of fluoride decreased with the increased in hydrogen concentration at lower pH values. In the acidic adsorption concentration because capacity of adsorbent pH range, the amount of fluoride adsorbed slightly material get exhausted slowly with the increase in the decreased and this can be due to the formation of weak initial fluoride concentration. hydrofluoric acid. In the alkaline condition pH range there was sharply drop in adsorption which may be due to the competition of the hydroxyl ions with the fluoride for adsorption. Fig. 4 : Dose of adsorbent – 5g/L, pH –8.0, Temp – 30OC, optimum time – 8 hrs, rpm– 150 Fig.2: Fluoride Conc.– 5mg/L , Dose of adsorbent– 5g/L ,Temp – 30OC,time – 24 hrs, rpm – 150 3.5 Effect of Co-Existing Ions Present of Co-existing ions in grounwater cause 3.3 Effect of Time of Contact positive or adsversed effect on adsorption. The study was The graphical representation is shown in Fig.3 it carried out on anions and cations (Mg ++, Fe ++, NO3 & SO4 shows that as the contact time increased the adsorption of ) fluoride also increased. After 480 min. (8 hrs.) the adsorption of fluoride was 77.6 % and remaining fluoride 335 | P a g e
  • 3. Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 2, Issue 4, July-August 2012, pp.334-338 100 90 % Removal of Fluoride 80 70 60 50 Mg++ 40 30 20 10 0 100 200 400 600 Co-Existing Ion (mg/l) Fig. 5 : Fluoride Conc. – 5mg/L , Dose of adsorbent– Fig. 8: Fluoride Conc. – 5mg/L , Dose of adsorbent –5g/L, 5g/L, Temp – 30OC,optimum time – 8 hrs, rpm – 150 Temp – 30OC, optimum time – 8 hrs rpm – 150 3.6 ADSORPTION MODEL The adsorption of Fluoride can be mathematically expressed in terms of adsorption isotherms. Adsorption isotherm data are commonly fitted to the Langmuir model (equation 1) and the Freundlich model (equation 2).Study carried on various dose of adsorbent and various temperature. Qm K ACe Qe  ....................(1) 1  K ACe Where, Qe = Amount of adsorbate adsorbed per unit amount of adsorbent at equilibrium. Fig. 6 : Fluoride Conc. – 5mg/L , Dose of adsorbent – 5g/L, Temp – 30OC, optimum time– 8 hrs, rpm – 150 Qm = Amount of adsorbate adsorbed per unit amount of adsorbent required for monolayer adsorption. K A = Constant related to enthalpy of adsorption. Ce = Concentration of adsorbate solution at equilibrium. 1 Qe  K F Ce n …................(2) where , K F and n are the constants Fig. 7: Fluoride Conc. – 5mg/L, Dose of adsorbent 5g/L,Temp – 30OC, optimum time – 8 hrs, rpm – 150 Ce = the concentration of adsorbate solution at equilibrium 336 | P a g e
  • 4. Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 2, Issue 4, July-August 2012, pp.334-338 qmax Temp. b r R2 (mg/g) 293K 1.891 0.1509 0.5698 0.8722 303K 4.17 3 0.1584 0.5580 0.9179 313K 4.728 0.203 0.4961 0.9639 Fig. 9: Fluoride Conc. – 5mg/L , rpm – 150 Table 2:Freundlich adsorption isotherm parameters for fluoride adsorption by bark of babool 3.7 Kinetic Adsorption Model It is apparent from the values of correlation coefficients that the pseudo-second-order kinetic model fitted well as compared to pseudo first-order model . Fig. 10: Langmuir Fit for Adsorption of Fluoride at 293K, 303K and 313K Fig.12 :Pseudo-first kinetic model for fluoride removal by bark of babool Fig. 11: Freundlich Fit for Adsorption of Fluoride at 293K, 303K and 313K Temp Kf ( mg/g) n 1/n R2 293K 1.192 1.172 0.85 0.9701 303K 2.847 1.046 0.955 0.8804 313K 1.333 0.879 0.937 0.869 Table 1: Langmuir Adsorption isotherm parameters for Fig.13:Pseudo-Second kinetic model for fluoride removal fluoride adsorption by bark of babool by bark of babool 3.8 Comparison of Simulated and Field Water 337 | P a g e
  • 5. Bhagyashree M Mamilwar, A.G.Bhole, A.M.Sudame / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 2, Issue 4, July-August 2012, pp.334-338 The adsorption experiments were study on simulated and field water containing fluoride concentration of 5mg/L, at [4] Ensar Oguz,“Adsorption of fluoride on gas concrete optimum pH-8.0, by adding optimum dose of adsorbent materials”, Journal of Hazardous Materials, (5g/L) which was put inside the bottles in 50 ml. which Vol.B117,(2005), 227–233. operated at 150 rpm and with constant temperature 303K up to 8hrs. (Time of equilibrium). From Fig.14 the [5] Mohanty.Auroprasad,National institute of removal of fluoride was more in simulated water than the Technology, Rourkela, “Developement of a Hybrid fluoride present in field water. This may be due to the Material for the removal of fluoride from water” 1- presence of cat ions and anions present in field water. 6. [6] Patil S. S, “ Assessments of Concentration of Fluoride from Drinking Water in Yavatmal District in Vidarbha Region by Ion Selective Electrode Method” IE(I) Journal, Vol. 88,(2007), 1-3. [7] Valach R and Sedlacek F “Changes in the use of biologically effective fluorides and the consequences”. Cas Lek Cesk. Vol.129, (1990), 769-777. [8] Raichur A.M, Basu M.J, “Adsorption of fluoride onto mixed rare earth oxides”, Sep. Purif. Technol. Vol.24, (2001), 121–127. [9] Agarwal, M., Rai, K., Shrivastav, R., Dass, S. “Defluoridation of water using amended clay”. J. Cleaner Produc.Vol.11, (2003), 439–444. [10] Ensar Oguz ,“Adsorption of fluoride on gas concrete materials”, Journal of Hazardous Materials, Vol.B117,(2005), 227–233. Fig.14:Fluoride Conc. – 5mg/L , Dose of adsorbent– 5g/L, Temp – 30OC,time– 8 hrs, rpm – 150 [11] Zhang V and Cao S R, “Coal Burning Induced Endemic Fluorosis in China. Fluoride”, CONCLUSION Vol.29,(1996),207-211. From the present result it is concluded that bark of babool as a adsorbent are promising materials for Fluoride removal. These adsorbent material is locally available but requires Pre-treatment to raw material before using for removal of fluoride. Optimum dose of bark of babool was found 5g/L for removal of fluoride concentration of 5 mg/L. Adsorption capacity was more in the pH range of 6-8.Optimum time of contact was found 8 hrs. The removal increased with time and adsorbent dose, but with higher initial concentration decreased with time and adsorbent dose. The present study on defluoridation using bark of babool shows that the equilibrium data fits better to Langmuir isotherm as compared with Freundlich isotherm.The pseudo-second-order kinetic model fitted well as compared to pseudo first-order model . REFERENCES [1] Maheshwari R.C.Meenakshi, “Fluoride in drinking water and its removal” Journal of Hazardous Materials, Vol.B137, (2006), 456–463. [2] Chaturvedi A.k., Yadava K.P, Pathak K.C, Singh V.N, “Defluoridation of water by adsorption on fly ash”, Defluoridation, Air Soil Pollut, 49,(1989). [3] Bhargava, D.S., Killedar, D.J., “Fluoride adsorption on fishbone charcoal through a moving media adsorber.” Vol.26, 1992, 781–788. 338 | P a g e