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0Hindawi Publishing Corporation Bioinorganic Chemistry and Applications Volume 2010, Article ID 457964, 8 pages doi:10.1155/2010/457964
Research Article
Biofunctional Characteristics of Lignite Fly Ash Modified by Humates: A New Soil Conditioner
Konstantinos Chassapis,1 Maria Roulia,1 Evangelia Vrettou,1 Despina Fili,2 and Monica Zervaki2
1 Inorganic Chemistry Laboratory, Department of Chemistry, University of Athens, Panepistimiopolis, 157 71 Athens, Greece
2 School of Chemical Engineering, National Technical University of Athens, 9 Heroon Polytechniou, Zografou Campus, 157 73 Athens, Greece
Correspondence should be addressed to Konstantinos Chassapis, chassapis@chem.uoa.gr Received 29 December 2009; Accepted 2 March 2010 Academic Editor: Spyros Perlepes
Copyright © 2010 Konstantinos Chassapis et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
Fly ash superficially modified with humic substances from the Megalopolis lignitic power plant was prepared and evaluated for agricultural uses. UV-vis spectrophotometry and IR spectroscopy revealed that fly ash shows high sorption efficiency towards humic substances. Adsorption proceeds stepwise via strong Coulombic and hydrophophic forces of attraction between guest and host materials. Langmuir, Freundlich, BET, Harkins-Jura, and Dubinin-Radushkevich isotherm models were employed to evaluate the ongoing adsorption and shed light to the physicochemical properties of the sorbent-adsorbate system. Humic substances desorption and microbial cultivation experiments were also carried out to examine the regeneration of the humates under washing and explore the possibility of this material acclimatizing in real soil conditions, both useful for biofunctional agricultural applications.
1. Introduction
Fly ash is an amorphous mixture of ferroaluminosilicate minerals generated from the combustion of ground or powdered coal at 400-1500°C and belongs to the coal combustion by-products in power plants produced from bituminous, subbituminus, and lignite combustion. Fly ash is the mineral residue consisting of small particles that are carried up and out of the boiler in the flow of exhaust gases and are collected from the stack gases using electrostatic precipitators, flue gas desulphurization systems, and bag houses [1]. Approximately 70% of the by-product is fly ash collected in electrostatic precipitators, which is the most difficult to handle [2]. This fact pinpoints the necessity for environment-friendly uses of fly ash. Fly ash is mostly used as a substitute for Portland cement in manufacturing roofing tiles and as structural fill, sheetrock, agricultural fertilizer, and soil amendment [3, 4]. Chemically, 90%-99% of fly ash is comprised of Si, Al, Fe, Ca, Mg, Na, and K with Si and Al forming the major matrix. The mineralogical, physical, and
chemical properties of fly ash depend on the nature of parent coal [5, 6]. All these applications are based on the presence of basic mineral elements resembling earth's crust, which makes them excellent substituent for natural materials.
The Greek peaty lignite of the Megalopolis Basin, formed during the Quaternary period and comprising significant quantities of humic substances and inorganic content [7, 8], may be an effective raw material for obtaining both humic substances and fly ash. During the last fifty years, Megalopolis lignite has been almost solely utilized for power generation producing solid wastes such as fly ash, bottom ash, boiler slag, and flue gas desulphurization materials, which have been commonly treated as wastes.
Agricultural utilization of fly ash has been originally proposed mostly thanks to its considerable K, Ca, Mg, S, and P contents [5, 9-11]. It was also realized that fly ash addition could also decrease the bulk density of soils, which, in turn, improved soil porosity and workability and enhanced water retention capacity [9]. Additionally, acidic or alkaline fly ash, may be of agronomic benefit buffering
the soil pH [5, 12, 13] and improving the soil nutrient status, thus increasing plant growth and nutrient uptake [14, 15]. The electrical conductivity of soil also increases with fly ash application and so does the metal content. Mixtures of swine manure with fly ash proved to increase the availability of Ca and Mg balancing the ratio between monovalent and bivalent cations, which otherwise proves detrimental to the soil [16]. This is of major importance as the presence of Ca can enhance flocculation or aggregation of soil particles, particularly clay, keeping soil friable, thus allowing both water and roots to penetrate hard and compact soil layers.
Compared to traditional soil-conditioning materials as asbestos, fly ash seems more advantageous as it is an environmentally safe material, contains plant nutrients, and can be used in biological cultivations (EU dir 889/08). Additionally, it is a low-cost material and, thanks to its granular composition, is readily applicable.
Humic substances are natural organic matter ubiquitous in water, soil, and sediments produced from the decay of animal and plant tissues and/or microbial activity. They are multifunctional amorphous biopolymers composed of hundreds of organic constituents including carbohydrates and condensed aromatic rings substituted by carboxylic, phenolic, and methoxyl groups [17], which may serve as an ideal ligand for bioinorganic applications. Their role in soil environment and their contribution in sustaining plant growth are of significant importance. Soil structure (water retention, texture, and workability), biological activity, and sequestration (chemical bioavailability, bioaccumulation, and transport of nutrients) are properties and processes of the global ecosystem directly affected by humic substances. The major challenge in research arises from the extended diversity of humic substances due to their large chemical heterogeneity and geographical variability [18].
Until now, fly ash has been used only as humic acid adsorbent for waste treatment [19, 20]. Therefore, the possibility of producing a material combining both the humic substances and fly ash advantages would appear particularly attractive.
In this work, fly ash superficially modified with humic substances (both derived from the Greek peaty lignite of the Megalopolis Basin) was prepared. UV-vis spectrophotometry and IR spectroscopy were employed to characterize the adsorption process. Five adsorption models were selected to envisage the physicochemical properties of the sorbent-adsorbate system based on the fundamental considerations and theoretical hypotheses of the specific isotherms. Humic substances desorption experiments were also carried out to determine the release rate of the humates adsorbed under washing. Additionally, cultivation experiments of microorganisms were processed to evaluate the possibility of acclimatizing this material in real soil conditions, useful for biofunctional agricultural applications.
2. Materials and Methods
Both humic substances and fly ash were extracted from the Greek peaty lignite of the Megalopolis Basin, Greece. The
selection of lignite was based on the rich content of humic substances in the particular lignite field [7, 8, 17]. Fly ash is a by-product during lignite combustion in Megalopolis power plants. Samples of fly ash were also received from the Ptolemais Basin (Kardia) for comparison purpose.
The extraction of humic substances from Megalopolis lignite using KOH solutions has been described previously as humates originating from low-rank coals are almost completely soluble in aqueous alkali [17]. A Varian Cary 3E UV-vis spectrophotometer was used to estimate the concentrations of humic substances at Amax = 550 nm. Prior to calculations a linear calibration curve was established by plotting absorbance against humic substances content.
In order to investigate the adsorption of humic substances on fly ash the following procedure was applied: 50 mL of humic substances solution were mixed with 1 g fly ash. The mixture was left under stirring for 1 hour at ambient temperature (291 K) and constant pH and then filtered to separate the humates. The concentration ofhumic substances in the solution was determined spectrophotomet-rically as described above and the retention of the adsorbate onto adsorbent (mgg-1) was calculated by the following equation:
(C0 - Ce)
where Qe is the equilibrium concentration of humic substances on the adsorbent (mg g-1), C0 their initial concentration in solution (mgL-1), Ce the equilibrium concentration of humic substances in solution (mgL-1), m the mass of adsorbent (g), and V the volume of the humic substances solution (L).
Adsorption experiments were also repeated at 308, 323, 338, and 353 K and at several pH values to study the effect of temperature and acidity, respectively. In all cases, a humic substances concentration range 1.90 to 39.1 gL-1 was applied. The effect oftime on humate retention was also investigated in a 2- to 180-minute range.
Desorption experiments were carried out in humic-loadedfly ash (0.5 g) by washing with distilled water (10 mL). The aqueous extract was centrifuged from fly ash and the concentration of the humic substances released in water was calculated spectrophotometrically.
For the determination of microorganisms the method of progressive dilution in liquid media by direct plating was used. In the case of bacteria specimens, 1g of the material tested was mixed with 10mL Ringer solution (2.25gL-1 NaCl, 0.10 gL-1 KCl, 0.12 gL-1 CaCl2-2H2O and 0.05 gL-1 NaHCO3). Nutrient agar was added as growing medium. The samples were incubated at 310 K for 48 hours prior to counting colonies. For the cultivation of fungi 1 g of the sample was mixed with 2 mL Ringer solution. Sabouraud was used as growing medium and X900 vials were also added to increase the selectivity. The samples were incubated at 303 K for 7 days prior to counting colonies and fungi identification. Two replicates per dilution were plated and counted. All materials and equipment used were sterile. Control cultures were also ran in the absence of the studied compounds.
The microbial population was counted in cfug-1 of the compound tested.
A Perkin-Elmer 883 IR spectrophotometer was employed to record infrared spectra; pellets of the specimens were prepared after mixing with dry KBr. The chemical analyses of fly ash samples were obtained from EDXRF measurements on a MDX1000 OXFORD spectrophotometer. Solids were separated from solutions with the use of an MLW T 54 centrifuge (15 minutes at 3600 minutes-1). Acidity measurements were carried out by a SANXIN PHS-3D pH meter.
3. Results and Discussion
3.1. Parameters of Adsorption. The time of sorbent-adsorbate interaction and the acidity of the solution, both useful in setting up the adsorption process, are of great importance in adsorption phenomena. The retention of humic substances on fly ash increased only during the first 30 minutes and then remained practically constant; that is, equilibrium was attained. The solution acidity affects both the surface charge of the adsorbent and the protonation/deprotonation equilibria of the adsorbate. Figure 1 indicates that neutral humic solutions mostly favor the adsorption of humic substances onto fly ash. An increase in pH facilitates deprotonation of both fly ash and humic substances while at low pH values both sorbent and adsorbate become positively charged. Carboxylic groups, the principal source of charge development in natural organic matter, are ionized in pH = 4-5 [21]. Neutrality of humic substances solution seems to compensate the repulsive forces developed in homonymous charges in both host and guest materials, thus, favoring adsorption.
The effect of pH clearly shows that Coulombic interactions are involved in adsorption. However, the low cation exchange capacity of the Megalopolis fly ash (2.5 meq/100 g) cannot account for the whole amount of the adsorbate and, thus, insinuates additional dispersive host-guest interactions of hydrophobic nature (van der Waals, n-n, CH-n) and hydrogen bonds induced by the hydrophobic domains present in the humic superstructures [18].
3.2. Adsorbent Effect. Four different ashes (two fly ashes and two bottom ashes) from the Megalopolis and Ptolemais (Kardia) Basins were tested for the adsorption of humic substances. The chemical composition and properties of these ashes are presented in Table 1. Table 2 points out significant differences in adsorption of humic substances on these ashes. Specifically, both Megalopolis ashes retain more humic substances compared with the corresponding Kardia ones, a fact initially ascribed to the differences in the silicate content (Table 1).
In order to explain this observation, IR spectra were received (Figure 2) to determine changes in structure additional to the changes in the chemical composition of the adsorbents. The main infrared bands are located at approximately 3450 cm-1 and 1640 cm-1 for O-H stretching and OH bending, respectively [22]. The band at 1460 cm-1 represents the sodium carbonate resulting from carbonation [23].
3 100 ffi
Figure 1: Retention of humic substances with pH.
However, major differences are observed in the 850- to 1200-cm-1 envelope providing information on the silicate backbone. Particularly, the intense band at about 1090 cm-1 (accompanied by a shoulder at about 1175 cm-1) has been attributed to the asymmetric stretching vibrations of Si-O-Si bridges [22]. Such Si-O-Si bridges can be broken either by creation of nonbridging oxygen atoms in Si-O-bonds (which are charge-compensated by metal ions) or by hydrolysis effects leading to the formation of Si-OH bonds in Qn structures (Figure 3). The presence of nonbridging oxygen atoms leads to a weakening of the aluminosilicate network manifested as a pronounced shift towards lower frequencies in IR spectra. On this basis, the 850- to 1200-cm-1 envelope in both Megalopolis ashes is wider and more intense, particularly at lower wavenumbers, indicating a less "polymerized" silicate structure that readily adsorbs higher amounts of humic substances compared with the Kardia's corresponding ones, most probably via a cation exchange mechanism.
This explanation is fully compatible with the significant increase in adsorption of Kardia's bottom ash compared with the fly ash. The presence of intense absorption bands peaking at wavelengths lower than 1000 cm-1, in the case of the bottom ash, demonstrates changes in the matrix, that is, the existence of many nonbridging oxygen atoms responsible for humic adsorption.
3.3. Equilibrium Adsorption. The values of equilibrium humic content, Qe, on fly ash as a function of the equilibrium humic concentration in solution, Ce, at several temperatures (291, 308, 323, 338, and 353 K) are plotted in Figure 4. All isotherms appear sigmoidal, corresponding to a type II adsorption isotherm according to the Brunauer-Deming-Deming-Teller (BDDT) classification, this feature becoming more distinct with increasing temperature. Adsorption of humic substances onto fly ash ranges from 40 to 1300 mg humics/g fly ash at 291 and 353 K, respectively. Adsorption capacity increases with temperature from 760 to 1300 mg humics/g fly ash at 291 and 353 K, respectively (Figure 4).
■S 200
Table 1: Chemical analyses of fly ashes.
500 1000 1500 2000 2500 3000 3500 4000 Wavenumbers (cm"1)
- Megalopolis bottom ash - Megalopolis fly ash
Kardia bottom ash - Kardia fly ash
Figure 2: IR spectra of Megalopolis and Kardia ashes.
Figure 3: Schematic structures of silicate tetrahedral units, Qn, with n denoting the number of oxygen atoms bridging two silicon centers (0 = bridging oxygen atom).
Endothermic adsorption processes usually indicate processes activated in a reaction-kinetic sense representing the combined effects of temperature on both the rate of approach to equilibrium and the position of the equilibrium itself. This encounters the surpassing of the energy barriers by the adsorbate to diffuse through narrow constrictions of the fly ash surface to cavities beyond. In addition, adsorption is accompanied by other subprocesses, for example, conformational changes, multiple equilibria, and retention mechanisms, which, when lumped together, contribute to the endothermic character of the adsorption. Thus, the "knee" in the adsorption isotherm represents an adsorption restart, possibly due to multilayer formation and/or the beginning of another adsorption subprocess.
Megalopolis Kardia
Fly ash Bottom Ash Fly ash Bottom Ash
SiO2a 39.6 41.7 23.0 17.8
Al2O3a 15.9 14.1 12.6 8.4
Fe2O3a 8.53 8.47 7.5 3.58
CaO a 18.3 24.6 44.7 29.9
MgO a 2.75 4.10 3.58 2.39
Na2O a 0.484 0.58 0.33 0.19
K2O a 1.72 1.79 2.20 0.40
SO3 a 4.52 4.31 5.5 3.44
pH b 11.8 9.8 12.5 8.8
% w/w,
b10% w/winflyash.
Table 2: Adsorption of humic substances on several bottom and fly ashes.
Adsorbent Retention (g humic substances/g ash)
Fly ash
Megalopolis 1.72
Kardia 0.62
Bottom ash
Megalopolis 2.21
Kardia 1.31
3.4. Adsorption Isotherms. Five of the most valid adsorption models, that is, the Langmuir, Freundlich, BET, HarkinsJura, and Dubinin-Radushkevich (DR) isotherm equations, were fit to the experimental data of humate adsorption onto fly ash particles. The aim was to reveal distinct physicochem-ical properties that characterize both the adsorbents and the sorption process. The Langmuir equation [24], although widely applied, cannot describe the adsorption adequately (R2 < 0.67) in our case. This is not unexpected, since this theoretical model does not apply to Type II adsorption isotherms.
On the other hand, the Freundlich isotherm [25] provides a good mathematical model to describe the adsorption (Table 3) pinpointing heterogeneously distributed adsorption sites. Such an uneven arrangement of the heteroge-neously adsorbed humates has been proved to promote the development of local multilayers and aggregates of the adsorbate [26].
The BET equation [27] describes adequately the adsorption behavior of humates onto fly ash particles, although this model tacitly assumes a homogeneous adsorption surface and gives a linear region only at the lower concentrations of adsorbate where a condensed film exists. On this basis, the applicability of the BET equation results from the existence of different homogeneous surface patches where adsorption occurs consecutively, so that the isotherm actually consists of an assortment of numerous steps each one corresponding to the adsorption occurring at these patches [26, 28].
The Harkins-Jura model [29] is mostly based on the assumption of a nonuniform distribution of the adsorption
Ce (gL-1) (a)
Ce (gL-1)
a 0.4 -
Ce (gL-1)
Ce (gL-1)
Ce (gL-1) (e)
Figure 4: Adsorption of humic substances onto fly ash with temperature.
Table 3: Correlation coefficients of the linear adsorption equations.
Isotherm equation
Temperature
291 0.625
308 0.608
Langmuir
Ce/Qe = 1/KQm + (1/QJQ 323 0.565
338 0.445
353 0.664
291 0.989
Freundlich 308 0.962
log Qe = log Kf + ( 1/n) log Ce 323 0.871
338 0.722
353 0.759
291 0.996
BET 308 0.929
323 0.844
Ce/Qe(1-Ce) = 1/XmKß + ((Kß -1)/XmKß)Ce
338 0.880
353 0.910
291 0.840
Harkins-Jura 308 0.969
1/Q2 = B/A - (1/A) log Ce 323 0.792
338 0.520
353 0.834
291 0.957
Dubinin-Radushkevich 308 0.856
ln Qe = ln Xm - ß[RT ln(1 +(1/Ce))]2 323 0.985
338 0.806
353 0.893
sites and is not applicable unless a condensed film is shaped. Compared with the BET theory the existence of a linear region is much more extensive involving higher adsorbate concentrations. However, the assembling of multilayers in the case of humate adsorption seems to meet better the BET theory requirements as the correlation coefficients of the Harkins-Jura equation summarized in Table 3 are lower.
The DR model [30] presupposes a Gaussian distribution of the adsorption space with respect to the adsorption potential. The adsorption is considered to be the result of the adsorbate molecule entering into a pore; the process is described according to the Polanyi comprehension of the energetics inside the empty space of solids and applies rather to structurally homogeneous systems. Although it is widely applied in Type I isotherms, this model fits quite satisfactorily the experimental data of humate adsorption onto fly ash (Table 3). This may be due to the facts that the DR equation does not reduce to Henry's law at low adsorbate concentrations, the linear region is also extensive, involving higher adsorbate concentrations, and that it applies at low adsorbent loadings. Van der Waals forces to account for host-guest interactions are also encountered.
40 35 -30 -25 -
Number of washings
H pi = 8
□ pH = 9 pH = 10
Figure 5: Desorption ofhumic substances by washing.
From the DR plots, the mean energy of the adsorption, E, can be calculated using the following relationship:
The values of E do not exceed 0.2 kJg-1 of adsorbate, accounting for strong forces of attraction, more intense than the Van der Waals forces.
3.5. Desorption Studies. Desorption experiments were carried out to evaluate the ability of fly ash to render back the humic substances adsorbed, useful in potential applications of superficially modified fly ash as a slow-release fertilizer. Humic substances could not be released neither in acid nor in neutral environments; thus, experiments were processed in the alkaline area (pH = 8-10). Higher pH values were not tested because of their lack of importance for soil applications. The results presented in Figure 5 demonstrate that most of the humates (80%) were released during the first three washings; yet humics could be still identified after the sixth washing of fly ash. These observations clearly indicate that humic substances associate strongly with fly ash allowing for their slow release during repeated washing under alkaline conditions.
3.6. Microbial Populations. Microbial tests were carried out to determine the bacteria and fungi populations as the native microbial population in soil plays a vital role in the recycling of C, N, and P of the biosphere and, therefore, is critical for fertility and plant growth. Megalopolis fly ash proved sterile but humic-loaded samples produced 5 X 104 bacteria. It is important to note that a fertile agricultural soil contains about 107 and 5 X 105 bacteria and fungi, respectively [31]. Penicillium spp, Aureobasidium spp, Alternaria spp, Aspergilus spp, Mucor spp, Rhizopus spp, Rhizomucor spp,
Table 4: Trace elements concentrations in Megalopolis fly ash.
Substance Concentration (ppm)
TiO2 0.823a
P2O5 0.233a
SrO 0.107a
BaO 680
MnO 620
Cr2O3 410
NiO 390
V2O5 340
ZnO 160
CuO 130
ZrO2 110
Rb2O 88
MoO3 73
PbO 58
Y2O3 7
1 % w/w.
and Cladosporium spp were identified, typical in soil and tissue degradation products. The population of fungi leveled the one found in a fertile agricultural soil. These observations annotate that fly ash partly favors the development of microbial life. This may be due to the fact that, as chemical analysis of trace elements shows, the Megalopolis fly ash (Table 4) contains metals that, in high concentrations, may be proved toxic to microbes restraining their growth. The presence of these trace elements causes no environmental risk as the increased pH of the Megalopolis fly ash (about 12) impairs the leaching of the metals [32]. However, it may set limitations regarding the mixing ratio of humic-loaded fly ash with soil in agricultural applications.
4. Conclusions
Humic-loaded fly ash was prepared at various humic to fly ash ratios. The Greek peaty lignite of the Megalopolis Basin was used as raw material for obtaining both fly ash and humates. Retention was studied at 291, 308, 323, 338, and 353 K and at several pH values. The adsorption capacity was found to increase at neutral pH and, also, with raise of temperature, that is, from 760 to 1300 mg humics/g fly ash at 291 K and 353 K, respectively. Fly ash demonstrated a high affinity towards humic substances and adsorption proceeded stepwise via strong Coulombic and hydrophophic forces of attraction between guest and host materials. Langmuir, Freundlich, BET, Harkins-Jura, and Dubinin-Radushkevich isotherm models were employed to evaluate the ongoing adsorption and shed light to the physicochemical properties of the sorbent-adsorbate system. Both the slow release of adsorbed humic substances during washing and the
existence of microbial populations are considered advantageous for employing humic-loaded fly ash in biofunctional agricultural applications, that is, in biological cultivations substituting traditional soil-conditioning materials.
The importance of this study from an economic standpoint is emphasized by the advantageous preparation of humic-modified fly ash from power plant wastes. Its production could also prove profitable, thanks to the extended coal reserves worldwide, strongly supporting the viability of the research on this field.
Acknowledgment
The authors are pleased to acknowledge the assistance of Associate Professor P. Markaki and Mrs. M. Tavoulari in microbial cultivation experiments.
References
[1] S. V. Mattigod, D. Rai, L. E. Eary, and C. C. Ainsworth, "Geo-chemical factors controlling the mobilization of inorganic constituents from fossil fuel combustion residues. I. Review of the major elements," Journal of Environmental Quality, vol. 19, no. 2, pp. 188-201, 1990.
[2] S. Jala and D. Goyal, "Fly ash as a soil ameliorant for improving crop production—a review," Bioresource Technology, vol. 97, no. 9, pp. 1136-1146, 2006.
[3] S. K. Antiohos and S. Tsimas, "A novel way to upgrade the coarse part of a high calcium fly ash for reuse into cement systems," Waste Management, vol. 27, no. 5, pp. 675-683,2007.
[4] S. K. Antiohos, V. G. Papadakis, E. Chaniotakis, and S. Tsimas, "Improving the performance of ternary blended cements by mixing different types of fly ashes," Cement and Concrete Research, vol. 37, no. 6, pp. 877-885, 2007.
[5] D. C. Adriano, A. L. Page, A. A. Elseewi, A. C. Chang, and I. Straughan, "Utilization and disposal of fly ash and other coal residues in terrestrial ecosystems: a review," Journal of Environmental Quality, vol. 9, no. 3, pp. 333-344, 1980.
[6] C. L. Carlson and D. C. Adriano, "Environmental impacts of coal combustion residues," Journal of Environmental Quality, vol. 22, no. 2, pp. 227-247, 1993.
[7] K. Chassapis, M. Roulia, and D. Tsirigoti, "Chemistry of metal-humic complexes contained in Megalopolis lignite and potential application in modern organomineral fertilization," International Journal of Coal Geology, vol. 78, no. 4, pp. 288295, 2009.
[8] K. Chassapis and M. Roulia, "Evaluation of low-rank coals as raw material for Fe and Ca organomineral fertilizer using a new EDXRF method," International Journal of Coal Geology, vol. 75, no. 3, pp. 185-188, 2008.
[9] A. L. Page, A. A. Elseewi, and I. R. Straughan, "Physical and chemical properties of fly ash from coal-fired power plants with reference to enviromental impacts," Residue Reviews, vol. 71, pp. 83-120, 1979.
[10] R. Sikka and B. D. Kansal, "Effect of fly-ash application on yield and nutrient composition of rice, wheat and on pH and available nutrient status of soils," Bioresource Technology, vol. 51, no. 2-3, pp. 199-203, 1995.
[11] N. Kalra, H. C. Joshi, A. Chaudhary, R. Choudhary, and S. K. Sharma, "Impact of flyash incorporation in soil on germination of crops," Bioresource Technology, vol. 61, no. 1, pp. 39-41, 1997.
[12] D. El-Mogazi, D. J. Lisk, and L. H. Weinstein, "A review of physical, chemical, and biological properties of fly ash and effects on agricultural ecosystems," Science of the Total Environment, vol. 74, no. 1,pp. 1-37, 1988.
[13] A. A. Elseewi, S. R. Grimm, A. L. Page, and I. R. Straughan, "Boron enrichment of plants and soils treated with coal ash," Journal of Plant Nutrition, vol. 3, pp. 409-427, 1981.
[14] R. L. Aitken, D. J. Campbell, and L. C. Bell, "Properties of Australian fly ash relevant to their agronomic utilization," Australian Journal of Soil Research, vol. 22, pp. 443-453, 1984.
[15] D. C. Elfving, C. A. Bache, W. H. Gutenmann, and D. J. Lisk, "Analyzing crops grown on waste-amended soils," BioCycle, vol. 22, no. 6, pp. 44-47, 1981.
[16] L. Giardini, "Aspetti agronomici della gestione dei reflui zootecnici," Rivista di Ingegnaria Agraria, vol. 12, pp. 679-689, 1991.
[17] K. Chassapis, M. Roulia, and G. Nika, "Fe(III)-humate complexes from megalopolis peaty lignite: a novel eco-friendly fertilizer," Fuel, vol. 89, no. 7, pp. 1480-1484, 2010.
[18] A. Piccolo, "The supramolecular structure of humic substances: a novel understanding of humus chemistry and implications in soil science," Advances in Agronomy, vol. 75, pp. 57-134, 2002.
[19] S. Wang, T. Terdkiatburana, and M. O. Tade, "Single and co-adsorption of heavy metals and humic acid on fly ash," Separation and Purification Technology, vol. 58, no. 3, pp. 353358, 2008.
[20] S. Wang and Z. H. Zhu, "Humic acid adsorption on fly ash and its derived unburned carbon," Journal of Colloid and Interface Science, vol. 315, no. 1, pp. 41-46, 2007.
[21] A. G. Kalinichev and R. J. Kirkpatrick, "Molecular dynamics simulation of cationic complexation with natural organic matter," European Journal of Soil Science, vol. 58, no. 4, pp. 909-917, 2007.
[22] M. Roulia, K. Chassapis, J. A. Kapoutsis, E. I. Kamitsos, and T. Savvidis, "Influence of thermal treatment on the water release and the glassy structure of perlite," Journal of Materials Science, vol. 41, no. 18, pp. 5870-5881, 2006.
[23] V. F. F. Barbosa, K. J. D. MacKenzie, and C. Thaumaturgo, "Synthesis and characterisation of materials based on inorganic polymers of alumina and silica: sodium polysialate polymers," International Journal of Inorganic Materials, vol. 2, no. 4, pp. 309-317, 2000.
[24] I. Langmuir, "The adsorption of gases on plane surfaces of glass, mica and platinum," Journal of the American Chemical Society, vol. 40, no. 9, pp. 1361-1403, 1918.
[25] H. Freundlich, "Uber die Adsorption in Losungen," Zeitschrift fur physikalische Chemie, vol. 57, pp. 385-470, 1906.
[26] M. Roulia and A. A. Vassiliadis, "Sorption characterization of a cationic dye retained by clays and perlite," Microporous and Mesoporous Materials, vol. 116, no. 1-3, pp. 732-740, 2008.
[27] S. Brunauer, P. H. Emmett, andE. Teller, "Adsorption of gases in multimolecular layers," Journal of the American Chemical Society, vol. 60, no. 2, pp. 309-319, 1938.
[28] S. J. Gregg and K. S. W. Sing, Adsorption, Surface Area and Porosity, Academic Press, London, UK, 2nd edition, 1982.
[29] W. D. Harkins and G. Jura, "Surfaces of solids. XIII. A vapor adsorption method for the determination of the area of a solid without the assumption of a molecular area, and the areas occupied by nitrogen and other molecules on the surface of a solid," Journal of the American Chemical Society, vol. 66, no. 8, pp. 1366-1373, 1944.
[30] L. V. Radushkevich and M. M. Dubinin, "The equation of the characteristic curve of activated charcoal," Doklady Akademii Nauk SSSR, vol. 55, pp. 327-329, 1947.
[31] T. Hattori, Microbial Life in the Soil. An Introduction, Marcel Dekker, New York, NY, USA, 1973.
[32] W. Wang, Y. Qin, D. Song, and K. Wang, "Column leaching of coal and its combustion residues, Shizuishan, China," International Journal of Coal Geology, vol. 75, no. 2, pp. 81-87, 2008.
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