- Open Access
- Authors : Amina Rafeek, Anjala Nazar, Baeyou George Zachariah, Dr. Aju Mathew George
- Paper ID : IJERTCONV9IS09002
- Volume & Issue : ICART – 2021 (Volume 09 – Issue 09)
- Published (First Online): 24-06-2021
- ISSN (Online) : 2278-0181
- Publisher Name : IJERT
- License: This work is licensed under a Creative Commons Attribution 4.0 International License
Biomass as a Sustainable Alternative for Defluoridation of Water: An Understanding on the Biosorption Mechanism
Amina Rafeek1, Anjala Nazar2, Baeyou George Zachariap, Bobit Thomas4
1,2,3,4 Final Year U.G Student, Amal Jyothi College of Engineering,
Dr. Aju Mathew George5
Amal Jyothi College of Engineering
Abstract –Consumption of Water with excessive fluoride concentration above 1.5 mg/L can cause severe health issues including skeletal and dental fluorosis. In the present context, utilization of biosorbents from waste biomass would be sustainable and economic option for removal of fluoride ions from water compared to other alternatives. The present paper discusses the summary of various processes used biomasses for defluoridation of water. The theoretical and instrumental methods utilized by the researchers till date to understand the defluoridation mechanisms were also discussed in brief. Literature survey carried out suggested that theoretical models such as Freundlich and Langmuir isotherms, pseudo-first order and second order kinetic models, and different thermodynamic parameters were also used to explain the defluoridation process by biomasses. In addition to various theoretical models, advanced instrumentation facilities like FESEM, FTIR, EDX etc., have been also utilized to study the defluoridation mechanism by biomasses.
Keywords: Defluoridation, Biomass, Biosorption, Mechanism, Instrumentation
Water containing high fluoride is serious concern and is usually unusable for drinking and even cooking purpose to evade health tribulations. Removal of fluoride from contaminated drinking water is inevitable, to avoid ingestion of excess fluoride as an anticipatory measure, until alternative water sources with low fluoride content is available. The reported tolerance limit of fluoride concentration in drinking water is 1.5 mg/L (WHO, 1994). However, continuous consumption of high concentrations of fluorides in excess of 0.5-1.0 mg/L may also lead to accumulation in body tissues capable of causing dental and skeletal fluorosis. To surmount the negative health effects, numerous defluoridation techniques are being attempted around the globe. The most common being membrane separation, chemical coagulation, ion-exchange, contact precipitation and chemical additive methods. However, each of them have some limitations which in general make their use unsustainable under most given conditions, particularly in remote areas in developing countries. Among the defluoridation processes, the adsorption process is reported to be effectiveness of removing fluoride. Adsorption technique has been the most extensively applied method for defluoridation of water because of its low cost, the simplicity of design and ease of operation. Commercial activated
carbon was commonly used as an adsorbent for removing fluoride from water. But, this is expensive and high-tech produced material. Therefore, excessive fluoride is removed from water using a cost effective and eco-friendly alternative.
Indian almond is a large deciduous tree, a hard endocarp enclosing edible seeds and whorled branches. Indian almond leaves contain many functional groups which exhibits affinity to Fluoride ion. These two materials were chosen as biosorbents as they are easily available, natural and low cost.
ADSORBENTS FOR FLOURIDE REMOVAL The different types of biomass used for fluoride removal are seaweeds, algae, fungal mycelia, and lignocellulosic plants. Surfaces of biomasses contain amine, carboxyl, hydroxyl, sulfhydryl, and phosphate functional groups which help in the fluoride removal. The efficiency of any adsorbent is known to depend on their affinity toward fluoride ions and the capacity of the functional groups present within the ad- sorbent. In the following sections of this article, waste bio- mass-based fluoride removal processes are reviewed.
LIGNOCELLULOSIC PLANT MATTERS Lignocellulosic plant matters have hemicelluloses, cellulose, and lignin. This biomaterial can adsorb fluoride from water if they have functional groups. They are inexpensive and easily available. In the following subsection, different treat- ment methods of lignocellulosic plant materials are dis- cussed that are needed for improving the fluoride removal efficacy of lignocellulosic biomatters.
TREATMENT OF ADSORBENTS Lignocellulosic biomass are modified by physical and/or chemical treatments to exhibit higher fluoride removal and regeneration. Removal efficiencies depend on their particle size, surface area, and functionality on their surface.
Lignocellulosic biomasses can be converted to activated charcoal for enhancing specific surface area and pore charac- teristics so that more fluoride adsorption will take place. Surface area and functionality of lignocellulosic plant mat- ters can also be improved by treating chemically. Chemical treatment includes acid and/or alkali treatment. During chemical treatment amorphous cellulose, hemicellulose and
lignin will be removed from the surface of biomass which will enhance the amount of pores on the biomatters surface. These pores will adsorb fluoride ions present in the water. Acid treatment is done for protonation, removal of metal traces and formation of COOH group. Alkali treatment is done for decomposition of surface walls, cellulose, lignin and formation of functional groups.
BATCHSTUDIES OF ADSORBENTS
Batch adsorption studies are conducted for determination of optimum conditions required for removal of fluoride from water. For determination of optimum pH for adsorption, water samples of 5g/L fluoride concentration was taken in five beakers with pH varying from 2-10, and was agitated for one hour at 50rpm with adsorbent dosage of 5g/l. On determination of optimum pH, for optimum adsorbent dosage determination, batch study is done at obtained optimum pH with varying adsorbent dosage from 5g/l-25g/L for a time period of one hour. For determination of optimum contact time, fluoride contaminated water sample are taken in five beakers at optimum pH, at best adsorbent dosage and is stirred at 50 rpm for time periods of 30 mins, 1 hour, 1.5 hrs, 2 hrs, 2.5 hrs etc. Similarly, test is done for determination of removal at different fluoride dosages. Amount of adsorbed fluoride was determined by the equation-
For a favourable sorption process the value of RL lies in the range 0 <RL <1
Freundlich isotherm is applicable to physico-chemical ad- sorption on heterogeneous surfaces. Freundlich isotherm equation is given by:
log qe = (1/n) log Ce + log Kf (5)
where, Ce is the equilibrium sorbate concentration in the liquid phase and Kf and 1/n are Freundlich coefficients, which represent the sorption capacity and intensity of the sorption respectively. These coefficients can be obtained from the slope and intercept of Freundlich plots of log qe vs. log Ce.
Apart from these two isotherm models, many other isotherm Models are also there like Temkin, Elovich, Redlich, and Peterson isotherms
B. Kinetic studies
The data obtained from kinetic evaluation provide a detail description of the sorbate transport mechanisms within the adsorbent. The three main kinetic models are the pseudo first order, the second order and the intra-particle diffusion mod- el. When adsorption is preceded by diffusion through a boundary, the sorption kinetics generally follows the pseudo
Percentage removal of fluoride is given by-
first order rate equation given by Lagergren,
Log (qe qt) = log q (k1/2.303) Ã— t (6)
R% = (0) 100 (2)
Where C0=initial concentration of fluoride, Ce=equilibrium concentration of fluoride, V=Volume of sample and MS= mass of adsorbent used.
A. Equilibrium studies
Equilibrium studies are useful for evaluating if the sorption processes is appropriate to termed as a unit operation. Langmuir and Freundlich models are the mostly used models for biosorption experimental data evaluation, probably due to the simplicity of these models.
Langmuir isotherm is valid for single layer adsorption. The general form of Langmuir isotherm as follows:
1/qe = (1/a) + (1/abCe) (3)
where, a is number of moles of solute sorbed per unit mass of sorbent in forming a monolayer on the surface, b is a con- stant related to energy. A plot of 1/qe against 1/Ce gives a straight line, slope of which gives the value of b and the in- tercept gives the value of a. To predict whether the sorp- tion process is favourableor unfavourable for the Langmuir type of sorption, the isotherm can be further tested by the values of RL, the dimensionless separation factor, given by;
RL = 1/ (1 + bCo) (4)
where, k1 is the first order rate coefficient, qe and qt are the amount sorbed per unit mass of the sorbent at equilibrium and at time t respectively.
The linear form of the second order kinetic equation is given by:
t/qt = 1/h + (1/qe) Ã— t (7)
where, h is equal to k2qe2 and can be considered as the ini- tial rate of interaction
The intraparticle diffusion rate constant (Ki) is given by the equation,
qt = Ki.t0.5 + C (8)
where, C is a constant, given by the intercept of the Weber Morris plots of qt vs. t0.5.
C. Thermodynamic studies
In addition to the isotherm and kinetic data, thermodynamic data are also essential to understand an adsorption process. The important thermodynamic parameters, namely, entropy change (S), enthalpy change (H) and Gibbs energy change (G) for the sorption process can be calculated from the Vant Hoff equation, which is given by,
log (qe/Ce) = S/(2.303R) H/2.303RT (9)
H and S can be calculated from the vant Hoff plots of log (qe/Ce) vs. 1/T and G can be obtained by using the following relationship,
Go = Ho TSo (10)
where, Go, Ho and So are standard Gibbs energy change, standard enthalpy change and standard entropy change for the sorption process respectively.
CONCLUSION AND FUTURE PERSPECTIVES
Extensive laboratory investigations were conducted to evaluate the adsorptive capability of low cost adsorbents prepared from biomass for adsorption of fluoride. Surface characterization and determination of surface ligands present helps identify processes involved in adsorption of flouride onto active sites. Further study of the same helps in in-depth understanding of complex redox reactions involved hence paving scope for future works.
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