Biosorption of Fluoride from Aqueous Solution on Citrus limonium

 

B.Sumalatha1, A.Venkata Narayana2, K. Kirnan Kumar3, Y. Prasanna kumar4, D. John Babu2, M. Vijaya Leela5

1School of Chemical Engineering, Vignan University, Vadlamudi, Guntur-522 213

2School of Biotechnology, Vignan University, Vadlamudi, Guntur-522 213

3Department of Chemical Engineering, Dr. SGIET, Markapur, A.P- 523329

4Sanketika Vidya Parishad Engg College, Madhurawada, Visakhapatnam, A.P 530041

5Department of chemistry, P.N.C & Vijai Institute of Engg., & Tech. Repudi- 522 529

*Corresponding Author E-mail: ksumalatha1@gmail.com

ABSTRACT:

This communication presents results pertaining to the adsorptive studies carried out on fluoride removal onto Citrus limonium biosorbent. Batch sorption studies were performed and the results revealed that biosorbent demonstrated ability to adsorb the fluoride. Influence of varying the conditions for removal of fluoride, such as the fluoride concentration, the dosage of adsorbent, the size of adsorbent, the concentration of metal solution studies were investigated. The rate of fluoride adsorption by Citrus limonium 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. 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.  Experimental data showed good fit with the Langmuir’s adsorption isotherm model. Maximum fluoride sorption was observed at 300C operating temperature.

 

KEYWORDS: Biosorption; Biosorbent; Citrus limonium; Isotherms.

 


INTRODUCTION:

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 intake[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/l, while at certain other places, fluoride levels are as high as 35 mg/l[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. Keeping the above points in view, batch adsorption of studies was carried out on the sorption of fluoride from aqueous phases using commonly available Citrus limonium powder. The adsorption studies carried out under various experimental conditions and the results obtained are presented in this communication. The C. limonium powder used as biosorbent in this experiment and its availability is easy without any practical investment. Thus using C. limonium powder as biosorbent is environmentally safe and practically economical.

 

Materials and methods:

Preparation of Adsorbent

The green colored C. limonium used in the present study were collected from the Juice point and Lemon soda seller. The collected C. limonium were washed with deionized water several times to remove impurities. The washing process was continued till the wash water contains no dirt. The washed C. limonium were then completely dried in sunlight for 10 days. The resulting product was directly used as adsorbent. The dried C. limonium 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 µm 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 un adsorbed metal concentrations per gram of adsorbent in solution at equilibrium and calculated by

 

  ………. (1)

Where X the adsorbent concentration (g/l), qe the adsorbed metal ion quantity per gram of adsorbent at equilibrium (mg/g), Co initial metal concentration (mg/l), Ceq the metal concentration at equilibrium (mg/l) and V is the working solution volume.

Metal Adsorption Experiments

Adsorption experiments were conducted at 30 °C in batch with 0.1 g of the C. limonium 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 C. limonium 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 and unadsorbed metal ions in solution.  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

 ……………….  (2)

where Qmax is the maximum amount of the metal ion per unit weight of algae to form a complete monolayer on the surface bound at high Ceq(mg/g), and  is a constant related to the affinity of the binding sites (L/mg), Qmax 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. Qmax and ‘b' can be determined from the linear plot of Ceq/qe Vs qe[43-44].             The empirical Freundlich equation based on adsorption on a heterogeneous surface is given by

        ……………………. (3)

where KF and  are Freundlich constants characteristic of the  system. KF and  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.

 

RESULTS AND DISCUSSION:

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. The rapid metal sorption is also highly desirable for successful deployment of the biosorbents for practical applications.


 

 

Fig 1. Effect of contact time on the percentage removal of fluoride

 

Fig. 2 Effect of adsorbent concentration on percentage adsorption

 


Effect of C. Limonium Concentration

The effect of variation of C. limonium dosage on fluoride uptake and fluoride % removal is shown in Fig.2.It 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. 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 µm) on percentage removal of fluoride was investigated and shown in Fig.3. It  reveals that the adsorptions of fluoride on C. limonium decreases from with the increased particle size from 72 to 200 µm at an initial concentration of 5 mg/L.  It is well known that increasing the particle size of the adsorbent decreases the surface area, which in turn decreases adsorption capacity.

 

Fig. 3 Effect of particle size on % Adsorption

Effect of Initial Fluoride 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.It shows that the metal uptake increases and percentage adsorption of the fluoride decreases with increase in initial metal ion concentration.  This increase is result of the increase in the driving force i.e. concentration gradient.  However, the percentage adsorption of fluoride ions on C. limonium 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. 

 

 


Fig. 4 Effect of metal concentration on percentage adsorption

 


 

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±20C.  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±20C.  The best-fit equilibrium model was determined based on the linear regression correlation coefficient.  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  value for Langmuir isotherm confirms the approximation of equilibrium data to Henrys law at lower initial concentration.


 

Fig. 5 Langmuir Adsorption Isotherm

 

Fig.6 Freundlich Adsorption Isotherm


 

CONCLUSIONS:

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 Citrus limonium demonstrated a good capacity of fluoride adsorption, highlighting its potential for water. The data obtained from the adsorption of fluoride ions on the Citrus limonium 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 Citrus limonium. The amount of fluoride adsorbed increases with an increase in adsorbent dosage of Citrus limonium. The experimental data gave good fit with Langmuir isotherm and the adsorption coefficient agreed well with conditions of favorable adsorption.

 

ACKNOWLEDGEMENT:

Authors wish to thank Vignan University, Vadlamudi for providing laboratory facilities and financial support to carry out this work.

 

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Received on 05.03.2014          Modified on 30.03.2014

Accepted on 05.04.2014         © RJPT All right reserved

Research J. Pharm. and Tech. 7(5): May, 2014; Page   554-560