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Biosorption isotherms of fluoride from aqueous solution on Ulva fasciata sp.-a waste material.


Fluoride ion in water exhibits unique properties, as its concentration in optimum dose in drinking water is advantageous to health and excess concentration beyond the prescribed limits affects the health [1]. High fluoride concentration in the ground water and surface water in many parts of the world is a cause of great concern. High fluoride in drinking water was reported from different geographical regions. The problem of excessive fluoride in ground water in India was first detected in Nellore (part of Prakasam district now) of Andhra Pradesh in 1937 [2]. According to an estimate, 25 million people in 19 states and union territories have already been affected and another 66 million are at risk including 6 million children below the age of 14 years [3]. Though fluoride enters the body mainly through water, food, industrial exposure, drugs cosmetics, etc. drinking water is the major source (75%) of daily in take [4]. A fluoride ion is attracted by positively charged calcium in teeth and bones, due to its strong electro negativity. Major health problems caused by fluoride are dental fluorosis (teeth mottling) skeletal fluorosis (deformation of bones in children and also in adults) and non skeletal fluorosis [5,6]. It can interfere with carbohydrates, lipids, protein, vitamins, enzymes and mineral metabolism when the dosage is high. In some parts of India, the fluoride levels are below 0.5 mg/1, while at certain other places, fluoride levels are as high as 35 mg/1 [7,8].

Defluoridation was reported by adsorption [9], chemical treatment [10,11], ion exchange [12], membrane separation [13,14], electrolytic de-fluoridation [15], and electro dialysis [16-18], etc. Among various processes, adsorption was reported to be effective [19]. Investigators reported various types of adsorbents namely activated carbon, minerals, fish bone charcoal, coconut shell carbon and rice husk carbon, with different degrees of success [9,20-24]. Recently considerable interest was observed on the application of biosorbent materials for removal of various pollutants. Biosorbent materials can passively bind large amounts of metal(s) or organic pollutants, a phenomenon commonly referred to as biosorption [25-32]. Biosorbents are attractive since naturally occurring biomass(es) or spent biomass(es) can be effectively utilized [25]. Besides this, biosorption offers advantages of low operating cost, minimization of the volume of chemical and/or biological sludge to be disposed, high efficiency in dilute effluents, no nutrient requirements and environmental friendly and economical viable. It provides a cost-effective solution for industrial water management [33]. Application of biosorbents/biomass from various microbial sources, leaf based adsorbents and water hyacinth was reported by various investigators [34-42]. Limited number of studies was available on the treatment by algal species (fresh and marine water) in spite of their ubiquitous distribution and their central role in the fixation and turnover of carbon [43-45]. Keeping the above points in view, batch adsorption of studies was carried out on the sorption of fluoride from aqueous phases using commonly available algal Ova fasciata sp. The adsorption studies carried out under various experimental conditions and the results obtained are presented in this communication. Algae are traditionally a food supplement and are generally safe. The algal Ulva fasciata sp. used as biosorbent in this experiment is generally grows profusely on rocks of the tidal zone of costal belt and its availability is easy without any practical investment. Thus using Ova fasciata sp. as biosorbent is environmentally safe and practically economical.

Materials and methods

Preparation of adsorbent

The green colored marine algae Ulva fasciata sp. used in the present study were collected from the coastal belt of Visakhapatnam, Andhra Pradesh, INDIA. The collected algae were washed with deionized water several times to remove impurities. The washing process was continued till the wash water contains no dirt. The washed algae were then completely dried in sunlight for 10 days. The resulting product was directly used as adsorbent. The dried algae were then cut into small pieces and were powdered using domestic mixer. In the present study the powdered materials in the range of 75-212 [micro]m particle size were then directly used as adsorbents without any pretreatment.

Chemical and metal solution

Stock solution of fluoride was prepared by dissolving 2.21 g of sodium fluoride (AR grade) in 1000 ml of double glass distilled water. The stock solution was then appropriately diluted to get the test solution of desired fluoride concentration.

Analysis of fluoride

The residual fluoride concentration in the aqueous phase was analyzed using Orion according to the procedures outlined in Standard methods of APHA.

The results are given as a unit of adsorbed and unadsorbed metal concentrations per gram of adsorbent in solution at equilibrium and calculated by

[q.sub.e] = ([C.sub.o] - [C.sub.eq])V / X (1)

where X is the adsorbent concentration (g/1), [q.sub.e] the adsorbed metal ion quantity per gram of adsorbent at equilibrium (mg/g), [C.sub.o] the initial metal concentration (mg/1), [C.sub.eq] the metal concentration at equilibrium (mg/1) and V is the working solution volume.

Metal adsorption experiments

Adsorption experiments were conducted at 30[degrees]C in batch with 0.1 g of the Ulva fasciata sp. in a 30ml of working solution volume. The flasks were then shaked at 180 rpm.

Adsorption equilibrium

Equilibrium studies were carried out by agitating 30 mL of fluoride solutions of initial concentrations varying from 5-25 mg/L with 0.1 to 0.5 g of algae at room temperature for 45 minutes at a constant stirring speed at a pH of 6.

During the adsorption, a rapid equilibrium is established between adsorbed metal ions on the algal cell ([q.sub.e]) and unadsorbed metal ions in solution([C.sub.eq]). This equilibrium can be represented by the Langmuir [46] or Freundlich [47] adsorption isotherms, which are widely used to analyse data for water and wastewater treatment applications. The Langmuir equation which is valid for monolayer adsorption on to a surface a finite number of identical sites and is given by

[q.sub.e] = [Q.sub.max]b [] / 1 + b[] (2)

where [Q.sub.max] is the maximum amount of the metal ion per unit weight of algae to form a complete monolayer on the surface bound at high [C.sub.eq] (mg/g), and b is a constant related to the affinity of the binding sites (L/mg) [Q.sub.max] represents a practical limiting adsorption capacity when the surface is fully covered with metal ions and assists in the comparison of adsorption performance, particularly in cases where the sorbent did not reach its full saturation in experiments. [Q.sub.max] and b can be determined from the linear plot of [C.sub.eq] / [q.sub.e] Vs [C.sub.eq] [46-48].

The empirical Freundlich equation based on adsorption on a heterogeneous surface is given by

[q.sub.e] = [K.sub.F][C.sup.n.sub.eq] (3)

where [K.sub.F] and n are Freundlich constants characteristic of the system. [K.sub.F] and n are indicators of adsorption capacity and adsorption intensity, respectively. Eq. (3) can be linearized in logarithmic form and Freundlich constants can be determined. The Freundlich isotherm is also more widely used but provides no information on the monolayer adsorption capacity, in contrast to the Langmuir model [48-52].

Results and discussion

The effect of contact time

Fig. 1 shows the effect of contact time on the adsorption of fluoride by adsorbent from aqueous solution. The rate of fluoride adsorption by the nonliving cells was very rapid, reaching almost 90% of the maximum adsorption capacity within 45 min of contact time and the adsorption does not change significantly with further increase in contact time. Microbial metal uptake by nonliving cells, which is metabolism-independent passive binding process to cell walls (adsorption), and to other external surfaces, and is generally considered as a rapid process, taking place within a few minutes [53]. The rapid metal sorption is also highly desirable for successful deployment of the biosorbents for practical applications [54].

Effect of algae concentration

The effect of variation of Ulva fasciata sp. algal cells dosage on fluoride uptake and fluoride % removal is shown in Fig.2. Fig.2 shows that while the percentage removal of fluoride increases with the increase in adsorbent dosage, fluoride uptake increases by increasing adsorbent dose. The increase in metal uptake by increasing adsorbent dose is attributed to many reasons, such as availability of solute, electrostatic interactions, interference between binding sites, and reduced mixing at high biomass densities. Thus, the adsorption sites remain unsaturated during the sorption process due to a lower adsorptive capacity utilization of the sorbent, which decreases the adsorption efficiency. Some of these reasons contributed also in limiting the maximum percentage removal, thus 100% removal was not attained. This suggests that a more economical design for the removal of heavy metal ions can be carried out using small batches of sorbent rather than in a single batch [55].

The influence of adsorbent dosage in removal of fluoride is shown in Fig.2. The increase in adsorbent dosage from 0.1 to 0.5 g. resulted in an increase in adsorption of fluoride. This is because of the availability of more binding sites for complexation of fluoride ions.

Effect of particle size

The effect of different adsorbent particle sizes (72-200 pm) on percentage removal of fluoride was investigated.

Fig.3 reveals that the adsorptions of fluoride on Ulva fasciata sp. decreases from with the increased particle size from 200 to 72 pm at an initial concentration of 5 mg/L. It is well known that decreasing the particle size of the adsorbent increases the surface area, which in turn increases in adsorption capacity.

Effect of initial metal ion concentration

Several experiments were undertaken to study the effect of initial fluoride concentration on the fluoride removal from the solution. The results obtained are shown in Fig.4. and the data show that the metal uptake increases and percentage adsorption of the fluoride decreases with increase in initial metal ion concentration. This increase is a result of the increase in the driving force i.e. concentration gradient. However, the percentage adsorption of fluoride ions on Ova fasciata sp. was decreased. Though an increase in metal uptake was observed, the decrease in percentage adsorption may be attributed to lack of sufficient surface area to accommodate much more metal available in the solution. The percentage adsorption at higher concentration levels shows a decreasing trend whereas the equilibrium uptake of fluoride displays an opposite trend.

At lower concentrations, all fluoride ions present in solution could interact with the binding sites and thus the percentage adsorption was higher than those at higher initial fluoride ion concentrations. At higher concentrations, lower adsorption yield is due to the saturation of adsorption sites. As a result, the purification yield can be increased by diluting the wastewaters containing high metal ion concentrations.

Adsorption equilibrium

The adsorption equilibrium defines the distribution of a solute phase between the liquid phases and solid phases after the adsorption reaction reached equilibrium condition. In the present study, equilibrium studies were carried out at room temperature 28 [+ or -] 2[degrees]C. The equilibrium data were analysed using two of the most commonly used isotherm equations, Freundlich and Langmuir isotherm models.

The equilibrium data were very well represented by all the two equilibrium models (Fig.5 and 6). The calculated isotherm constant at room temperature 28 [+ or -] 2[degrees]C. The best-fit equilibrium model was determined based on the linear regression correlation coefficient [R.sup.2]. From the table it was observed that the adsorption data were very well represented by Langmuir isotherm with an average higher correlation coefficient of 0.9989. The higher [R.sup.2] value for Langmuir isotherm confirms the approximation of equilibrium data to Henrys law at lower initial concentration.








About 100 experimental runs were drawn, results were analytically discussed and the following conclusions could be drawn from study on the removal of fluoride ion from aqueous solution using the adsorption technique. The biomass of the Ulva fasciata sp. demonstrated a good capacity of fluoride adsorption, highlighting its potential for water.

* The data obtained from the adsorption of fluoride ions on the Ulva fasciata sp. showed that a contact time of 45 minutes was sufficient to achieve equilibrium.

* It was observed that the percentage adsorption of the metals decreases with increase in the initial metal ion concentration.

* It reveals that the effect of different adsorbent particle sizes on the adsorption of fluoride is significant. The adsorption of the metal decreases with increase in particle size of Ulva fasciata sp.

* The amount of fluoride adsorbed increases with an increase in adsorbent dosage of Ulva fasciata sp.

* The experimental data gave good fit with Langmuir isotherm and the adsorption coefficient agreed well with conditions of favourable adsorption.


[1] Venkata Mohan, S., Nikhila, P., and Reddy, S.J., 1995, "Determination of fluoride content in drinking water and development of a model in relation to some water quality parameters", Fresen. Environ. Bull., 4, 297-302.

[2] Short, H.E., Mc Robert, G.R., Bernard, T.W., and Mannadiyar, A.S., 1937, "Endemic fluorosis in the madras presidency", Ind. J. Med. Res., 25, 553-561.

[3] Sangam, 2003, "Combating fluorosis with household filters", Newsletters of UN inter agency-working group on water and environmental sanitation in India (UNICEF), 1-2.

[4] Sarala, K., and Rao, P.R., 1993, "Endemic fluorosis in the Village Ralla, Anantapuram in Andhra Pradesh an epidemiological study", Fluoride 26, 177-180.

[5] Susheela, A.K.,Kumar, A., Betnagar, M., and Bahadur, M., 1993, "Prevalence of endemic fluorosis with gastro-intestinal manifestations in people living in some north-Indian villages", Fluoride 26, "97-104.

[6] WHO, 1985, Health Criteria and Other Supporting Information, "Guidelines for Drinking Water Quality", CBS Publishers and Distributors, 2.

[7] Ramanaiah, S.V., Venkata Mohan, S., Rajkumar, B., and Sarma, P.N, 2006, "Monitoring of fluoride concentration in ground water of Prakasham District in India; correlation with physico chemical parameters," J. Environ. Sci. Eng., accepted for publication.

[8] Handa, B.K., 1975, "Geochemistry and genesis or fluoride containing groundwater in India", Ground Water 13, 278-281.

[9] Raichur, A.M., and Jyoti Basu, M., 2001, "Adsorption of fluoride onto mixed rare earth oxides", Sep. Purif. Technol., 24, 121-127.

[10] Reardon, E.J., and Wang, Y., 2000, "Limestone reactor for fluoride removal from waste waters", Environ. Sci. Technol., 34, 3247-3253.

[11] Saha, S., 1993, "Treatment of aqueous effluent for fluoride removal", Water Res. 27, 1347-1350.

[12] Singh, B. Kumar, Sen, P.K., and Maunder, J., 1999, "Removal of fluoride from spent pot liner leachate using ion exchange", Water Environ. Res., 71, 36-42.

[13] Dieye, A., Larchet, C., Auclair, B., and Mar-Diop, C., 1998, "Elimination des fluorures parla dialyse ionicque croisee", Eur. Polym., J. 34, 67-75.

[14] Amer, Z., Bariou, B., Mameri, N., Taky, M., Nicolas, S., and Elimidaoui, A., 2001, "Flu- oride removal from brakish water by electro dialysis", Desalination, 133, 215-223.

[15] Mameri, N., Lounici, H., Belhocine, D., Grib, H., Prion, G.F.,and Yahiat, Y., 2001, "Defluoridation of Sahara Water by small electro coagulation using bipolar aluminium electrodes", Sep. Purif. Technol., 24, 113-119.

[16] Hichour, M., Persin, F., Sandeaux, J., and Gavach, C., 2000, "Water defluoridation by Donann Dialysis and electro dialysis", Sep. Purif. Technol., 18,1-11.

[17] Hichour, M., Persin, F., Sandeaux, J., and Gavach, C., 1999, "Water defluoridation by Donann Dialysis and electro dialysis", Rev. Sci. Eau., 12, 671-686.

[18] Adikari, S.K., Tipnis, U.K., Harkare, W.P., and Govindan, K.P., 1989, "Defluoridation during desalination of brakish water by electro dialysis", Desalination, 71, 301-312.

[19] Venkata Mohan, S.,Chandrasekhar Rao, N., and Karthikeyan, J., 2002, "Adsorption removal of direct azo dye aqueous phase onto coal based sorbents a kinetic and mechanistic study", J. Hazard. Mater, 90 (2), 189-204.

[20] Jayantha, K.S., Ranjana, G.R., Sheela, H.R., Modang, R., and Shivananni, Y.S., 2004, "Defluoridation studies using laterite material", J. Environ. Sci. Eng., 46 (4), 282-288.

[21] Prabavathi, N., Ramachandramoorthy, T., EdisonRaja, R., Kavitha, B., Sivaji, C., and Srinivasan, R., 2003, "Drinking water of Salem district estimation of flu- oride and its defluoridation using lignite rice husk and rice-husk powder", IJEP, 23 (3), 304-308.

[22] Srimurali, S., Pragathi, A., and Karthikeyan, J., 1998, "A study on removal of fluorides from drinking water by adsorption onto low-cost materials", J. Environ. Pollut., 99, 285-289.

[23] Muthukumaran, K., Balasubramanian, K., and Ramakrishna, T.V., 1995, "Removal of fluoride by chemically activated carbon", IJEP, 15 (7), 514517.

[24] Killedar, D.J., and Bhargava, D.S., 1993, "Effects of stirring rate and temperature on fluoride removal by fishbone charcoal", Ind. J. Environ. Health, 35 (2), 81-87.

[25] Ilhami, T., Gulay, B., Emine, Y., and Gokben, B., 2005, "Equilibrium and kinetic studies on biosorption of Hg(II), Cd(II) and Pb(II) ions onto micro algae Chlamy- domonas reinhardtii," J. Environ. Manag., 77, 85-92.

[26] Gupta, R., Ahuja, P., Khan, S., Saxena, R.K., and Mohapatra, H., 2000, "Microbial biosor- bents: meeting challenges of heavy metal pollution in aqueous solutions," Curr. Sci., 78, 967-973.

[27] Williams, C.J., and Edyvean, R.G.J., 1997, "Ion exchange in nickel biosorption by sea- weed materials," Biotechnol. Prog., 13, 424-428.

[28] McHale, A.P.,and McHale, S., 1994, "Microbial biosorption of metals, potential in the treatment of metal pollution," Biotechnol. Adv., 12, 647-652.

[29] Macaskie, L.E., and Dean, A.C.R., 1989, "Biological Waste Treatment," Alan R. Liss, New York, 159-201.

[30] Gadd, G.M., in: Rehm, H.J., and Reed, G., 1988, Eds., "Biotechnology -A Compre- hensive Treatise, Special Microbial Processes," vol. 6b, VCH, Verlagsge- selISchaft, Weinheim, Germany, 401-433.

[31] Macaskie, L.E., and Dean, A.C.R., 1985, "Uranium accumulation by immobilized cells of a Citrobacter sp.," Biotechnol. Lett., 7, 457-462.

[32] Tsezos, M., and Volesky, B., 1982, "The mechanism of uranium biosorption by Rhizopus arrhizus ", Biotechnol. Bioeng., 24 (385), 401.

[33] Volesky, B., and Holan, Z.R., 1995, "Biosorption of heavy metals", Biotechnol. Prog., 11, 235-250.

[34] Arjun Khandare, L., Uday Kumar, P., Shankar, G., Venkaiah, K., and Laxmaiah, N., 2004, "Additional beneficial effects of Tamarind ingestion over defluoridated water supply to adolescent boys in a fluorotic area", Nutrition, 20,433-436.

[35] Venkata Mohan, S., Vijaya Bhaskar, Y., and Karthikeyan, J., 2003, "Biological decol- orization of simulated azo dye in aqueous phase by algae Spirogyra species", Int. J. Environ Pollut., 21 (3), 211-222.

[36] Jamode, B., Chandak, S., and Rao, M., 2004, "Evaluation of performance and kinetic parameters for defluoridating using Azadirachta Indica (neem) leaves as low cost adsorbents", Pollut. Res., 23 (2), 239-250.

[37] Ram Chandra Murthy, T., Jeyakar, A., Chellaraj, R., Edison Raja, T., Venkatachalam, R., Sangeetha, and Sivaraj, C., 2003, " Fluoride estimation in potable water in Tiruchirapalli Rock-Port Area-Dental fluorosis survey and Defluoridation with Emblicaphyllanth", IJEP, 239 (3), 317-320.

[38] Udaya Simha, L., Panigrahy, B., and Ramakrishna, S.V. 2002, "Preliminary studies on fluoride adsorption by water hyacinth", IJEP, 22 (5), 506-511.

[39] Mariappan, P., Yegnaraman, V., and Vasudevan, T., 2000, "Defluoridation of using low cost activated carbons", IJEP, 22 (2), 154-160.

[40] Venkata Mohan, S., Chandrasekhar Rao, N., Krishna Prasad, K., and Karthikeyan, J., 2002, "Treatment of simulated reactive yellow 22 (azo) dye efflu- ents using Spirogyra species," Waste Manag., 22, 575-582.

[41] Venkata Mohan, S., and Karthikeyan, J., 2000, "Removal of diazo dye from aqueous phase by algae Spirogyra species, Toxicol." Environ. Chem., 74, 147154.

[42] Prakasam, R.S., ChandraReddy, P.L., Manisha, A., and Ramakrishna, S.V., 1998, " Deflu- oridation of drinking water using eichhornia SP ", IJEP, 19(2), 119-124.

[43] Bhatnagar, M., Bhatnagar, A., and Jha, S., 2002, "Interactive biosorption by micro algal biomass as a tool for fluoride removal", Biotechnol. Lett., 24, 1079-1081.

[44] Bhatnagar, M., and Bhatnagar, A., 2000, "Algal and cyanobacterial responses to fluo- ride, Fluoride", 33 (2), 55-65.

[45] Semple, K.T., Cain, RB., and Schmidt, S., 1999, 'Biodegradation of aromatic compounds by micro algae", FEMS, Microb. Lett., 176 (2), 291-301.

[46] Langmuir, I., 1916, "The constitution and fundamental properties of solids and liquids." J. Am. Chem. Soc., 38(11), 2221-2295.

[47] Freundlich, H.M.F., Zeitschrift fur Physikalische Chemie, Leipzig, 1906, 57A, 385-470.

[48] Aksu, Z., Wong, Y, S., and Tam, N.F.Y., 1998, "Algae for Waste Water Treatment." Germany: Springer-Verlag and Landes Bioscience, Chapter 3, 3753.

[49] Wilde, E.W., and Benemann, J.R., 1993, "Bioremoval of heavy metals by the use of microalgae." Biotech. Adv., 11, 781-812.

[50] Wehrheim, B., and Wettern, M., 1994, "Biosorption of cadmium, copper and lead by isolated mother cell walls and whole cells of Chlorella fusca. " Appl. Microbiol. Biotechnol., 41, 725-728.

[51] Aksu, Z., and Kutsal, T.A., 1990, "A comparative study for biosorption characteristics of heavy metal ions with C. vulgaris. " Environ. Technol., 11, 979-987.

[52] Aksu, Z., Ozer, D., Ekiz, H.I., Kutsal, T., and Caglar, A., 1996, "Investigation of biosorption of chromium (VI) on C. crispate in two-staged batch reactor." Environ. Technol., England: 17, 215-220.

[53] Gadd, G.M., and De Rome, L., 1988, "Microbial treatment of metal pollution: A working biotechnology." Appl. Microbiol. Biotechnol., 29, 610.

[54] Volesky, B., 1990, in B. Volesky, Ed., "Biosorption of Heavy Metals", CRC Press, Boca Raton: FL.

[55] Abu Al-Rub, F.A., El-Naas, M.H., Benyahia, F., and Ashour, I., 2004, "Biosorption of nickel on blank alginate beads, free and immobilized algal cells." Process Biochem., 39, 1767-1773.

G. Kalyani *, G. Babu Rao *, B. Vijaya Saradhi (@) and Y. Prasanna Kumar (#)

* Department of Chemical Engineering, GMR Institute of Technology, Rajam--532127.

(@) Department of Civil Engineering, A. U. College of Engineering, Visakhapatnam--530 03.

(#) Department of Chemical Engineering, Vignan's Engineering College, Vadlamudi--522 213, Guntur (Dist)

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Author:Kalyani, G.; Rao, G. Babu; Saradhi, B. Vijaya; Kumar, Y. Prasanna
Publication:International Journal of Applied Environmental Sciences
Article Type:Report
Geographic Code:9INDI
Date:Jun 1, 2009
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