Biosorption of inorganic and methyl mercury by a biosorbent from Aspergillus niger

A biosorbent prepared by alkaline extraction of Aspergillus niger biomass was evaluated for its potential to remove mercury species – inorganic (Hg²⁺) and methyl mercury (CH₃Hg⁺) – from aqueous solutions. Batch experiments were carried out to determine the pH and time profile of sorption for both species in the pH range 2–7. The Hg²⁺ exhibited more rapid sorption and higher capacity than the CH₃Hg⁺. Further, removal of both mercury species from spiked ground water samples was efficient and not influenced by other ions. Sorption studies with esterified biosorbent indicated loss of binding of both mercury species (>80%), which was regained when the ester groups were removed by alkaline hydrolysis, suggesting the involvement of carboxyl groups in binding. Further, no interconversion of sorbed species occurred on the biomass. The biosorbent was reusable up to six cycles without serious loss of binding capacity. Our results suggest that the biosorbent from Aspergillus niger can be used for removal of mercury and methyl mercury ions from polluted aqueous effluents.     

Competing ion effect on chromium adsorption with fresh and starved subsurface bacterial consortium

Summary The sorption of chromium (Cr⁺⁶) was investigated for 50 day starved and fresh cells in the presence of sulfate ion as a competing ion at three pH values (pH 6.0, 7.5 and 9.0). The chromium distribution in the subcellular components was also determined by conducting cell fractionation. Although a previous study showed that cells which had been starved for 50 days prior to being exposed to a chromium containing solution sorbed 10–15% more chromium than did fresh cells (Kong et al., 1992a), this study demonstrated that such cells did not sorb more chromium in the presence of sulfate ion.     

Sorption of Co, Cu, Ni and Zn from industrial effluents by the submerged aquatic macrophyte Myriophyllum spicatum L.

The submerged aquatic plant Myriophyllum spicatum L. (Eurasian water milfoil) has been suggested as an efficient plant species for the treatment of metal-contaminated industrial wastewater. The process of metal removal by plants involves a combination of rapid sorption on the surface and slow accumulation and translocation in the biomass. This study focussed on the sorption/desorption characteristics of the surface of M. spicatum for Co, Cu, Ni and Zn. Batch sorption tests with mixed metal solutions covering a range of 0, 1, 5, 10, 50 and 100 mg l⁻¹ of each metal, were performed. For Co, Ni and Zn, the sorption process was well described by the Langmuir model, whereas sorption of Cu was better described by the Freundlich model. The biomass showed the highest affinity for Cu and Zn. Langmuir sorption maxima of Co, Ni and Zn were 2.3, 3.0 and 6.8 mg g⁻¹ DM, respectively. At the highest initial concentration of 100 mg l⁻¹, a maximum of 29 mg g⁻¹ DM of Cu was sorbed onto the surface of the biomass. Desorption by 0.1 M HCl did not fully recover the metals sorbed onto the surface and there was evidence of leaching from within the biomass. Recovery of heavy metals and regeneration of the biomass by washing with 0.1 M HCl was therefore not suggested as a viable strategy.     

Biosorption of Cr, Cu and Al bySargassum biomass

The biosorption and desorption of Cr, Cu and Al were carried out using brown marine algaeSargassum fluitans biomass, known as the good biosorbent of heavy metals. The content of alginate bound to light metals could be changed by physical and chemical pretreatment. The maximum uptake of Cr, Cu and Al was independent of the alginate content. The maximum uptake of Al was two times(mole basis) than those of Cu and Cr. The aluminum-alginate complex was found in the sorption solution of raw and protonated biomass. Most of Cu, Al and light metals sorbed in the biomass were eluted at pH 1.1. However, only 5 to 10% of Cr sorbed was eluted at pH 1.1. The stoichometric ion exchange between Cu and Ca ion was observed on Cu biosorption with Ca-loaded biomass. A part of Cr ion was bound to biomass as Cr(OH)₂ ⁺ or Cr(OH)²⁺. Al was also bound to biomass as multi-valence ion and interfered with the desorbed Ca ion. The behavior of rawS. fluitans in ten consecutive sorption-desorption cycles has been investigated in a packed bed flow-through-column during a continuous removal of copper from a 35 mg/L aqueous solution at pH 5. The eluant used was a 1%(w/v) CaCl/HCl solution at pH3.     

Factors affecting aluminium sorption by calcium pectate

Extracellular processes, particularly the adsorption of aluminium (Al) by pectate in the cell wall, have been proposed as important in the expression of Al toxicity to plant roots. In vitro studies were conducted on the effects of Al concentration (generally ≤ 32 μM), calcium (Ca) concentration (0.05 to 10 mM) and pH (3.2 to 5.4) on Al sorption by Ca pectate. There was a rapid reaction between Al and Ca pectate, there being no difference in Al remaining in solution after reaction times of 1 to 16 min, and only a slight decrease after 24 h. Increased Al concentration in solution increased linearly the sorption of Al by Ca pectate, with 70 to 84% of the Al originally in solution sorbed with ≤32 μM Al. In contrast, Al sorption decreased with increased Ca concentration in solution, and as pH decreased from 5.4 to 3.2. Only ≤30% of the sorbed Al was desorbed after 1 h by 1 mM CaCl₂, 10 mM CaCl₂ or 1 mM HCl. The amount of Al desorbed increased with a desorption period of 5 h, particularly with 1 mM HCl. These studies suggest that Al sorbed by Ca pectate in root cell walls is in equilibrium with Al in solution, and that Al toxicity is associated with the strong binding between Al and Ca pectate external to the cytoplasm.     

Biosorption of silver ions by processed Aspergillus niger biomass

Summary An alkali treated A. niger biomass was found to efficiently sequester silver ions from dilute as well as concentrated solutions (2.5–1000 ppm Ag⁺), with an ability to bind it to a level of upto 10% of dry weight. Biosorption of silver ions was not influenced by pH between 5–7. The bound Ag⁺ could be fully desorbed by dilute HNO₃ and the biosorbent regenerated by washing with Ca²⁺/Mg²⁺ solution. This biosorbent is unique in that the mechanism of metal ion sorption has been found to be exclusively by stoichiometric exchange with Ca²⁺ and Mg²⁺ of the biosorbent.     

Growth inhibition by ammonia and use of a pH-controlled feeding strategy for the effective cultivation of Mycobacterium chlorophenolicum

The inhibitory effect of ammonia on the growth of the polychlorinated xenobiotic-degrading bacterium Mycobacterium chlorophenolicum was examined. The strain is inhibited by both the ionized and nonionized forms of ammonia. At pH 6.9 50% reduction of the growth rate was observed at 6.8 g l^–1 total ammonium. For 23 experiments performed in shake-flask culture at different pH values and ammonium concentrations a growth model based on the extended Monod kinetic fits the data with a deviation of 5.3%. To overcome growth inhibition in bioreactors a pH-controlled feeding strategy was developed for effective cultivation of M. chlorophenolicum at an ammonium level below 0.3 g l^–1. The ammonium addition was controlled on-line by the stoichiometric interdependence of ammonium consumption and pH decline. With this on-line control strategy a biomass concentration as high as 26.2 g l^–1 can be achieved within less than 1 week of cultivation, compared to a biomass concentration of 15.5 g l^–1 in normal batch culture after 2 weeks of cultivation. The yield is also increased from 0.32 g to 0.43 g biomass (g glucose)^–1. The strategy developed provides an effective method for the production of biomass of M. chlorophenolicum serving as the inoculum in remediation technologies.     

Biosorption of organochlorine pesticides using fungal biomass

Cladosporium strain AJR³18,501 was tested for its ability to sorb the organochlorine pesticide (OCP) p,p′-DDT from aqueous media. When p,p′-DDT was added to distilled water, ethanol or 1-propanol solutions in excess of its solubility, p,p′-DDT was sorbed onto the fungal biomass. Increasing the amount of p,p′-DDT in solution by changing the medium composition increased sorbent uptake: p,p′-DDT uptake by the fungal biomass was 2.5 times greater in 25% 1-propanol (17 mg of p,p′-DDT g⁻¹ dry weight fungal biomass) than in distilled water. When p,p′-DDT was dissolved in 25% 1-propanol (12 mg l⁻¹), rapid p,p′-DDT sorption occurred during the first 60 min of incubation. p,p′-DDT in solution was reduced to 2.5 mg l⁻¹ with the remaining p,p′-DDT recovered from the fungal biomass. A number of environmental parameters were tested to determine their effect on p,p′-DDT biosorption. As arsenic (As) is prevalent at DDT-contaminated cattle dip sites, its effect on p,p′-DDT uptake was determined. The presence of As [As(III) or As(V) up to 50 mg l⁻¹] did not inhibit p,p′-DDT uptake and neither As species could be sorbed by the fungal biomass. Changing the pH of the medium from pH 3 to 10 had a small effect on p,p′-DDT sorption at low pH indicating that an ion exchange process is not the major mechanism for p,p′-DDT sorption. Other mechanisms such as Van der Waals forces, chemical binding, hydrogen bonding or ligand exchange may be involved in p,p′-DDT uptake by Cladosporium strain AJR³18,501. Journal of Industrial Microbiology & Biotechnology (2002) 29, 163–169 doi:10.1038/sj.jim.7000280 Received 15 January 2002/ Accepted in revised form 18 May 2002     

Batch studies on the removal of gold(III) from aqueous solution by Azolla filiculoides

Azolla filiculoides removed 86% and 100% of gold(III) from initial metal solutions of 2–10 mg gold l^–1 increasing with increased initial concentrations of gold(III). The biomass gave greater than 95% removal efficiency from solution at all biomass concentrations measured. Complete removal of gold occurred at pH 2, with 42% removal at pH 3 and 4, and 63% and 73% removal at pH 5 and 6, respectively. No temperature-dependence removal was observed.     

Biosorption of uranium by Myxococcus xanthus

This paper deals with uranium biosorption by Myxococcus xanthus biomass in which dry biomass, accumulating up to 2.4 mM of uranium g⁻¹, is demonstrated to be a more efficient biosorbent than wet biomass. For uranium concentrations of 0.1–0.3 mM, between 95.79% and 95.99% of the uranium was taken up from the solution. Dry biomass biosorption was found to be relatively rapid, reaching equilibrium after 5–10 min. In addition, the pH influenced biosorption, pH 4.5 promoting maximum uptake. It was also established that the biosorbed uranium is located on the cellular wall and within the extracellular mucopolysaccharide of this microorganism. Furthermore, using sodium carbonate as a desorbent agent, 80.82% of the biosorbed uranium could be recovered. The results obtained indicate the possible utilization of M. xanthus biomass to solve some problems of the water contaminated by uranium.     

Phosphorus fixation in lake sediments using LaCl3-modified clays

Fourteen types of clay, including soils and sediments from Lake Taihu, were modified by LaCl₃, and their abilities of phosphorus (P) sorption (the total P up-taken) and fixation (the unleachable P retained in modified clays) were investigated. Results showed that P sorption rates of LaCl₃-modified clays were all higher than 90%, while the fixation rates were raised from 3–14% to 52–95%. Kaolinite was selected to study the pH effect on P sorption and desorption of La³⁺ from the modified clays. In the pH range of 4–8, P sorption on LaCl₃-modified kaolinite could reach over 80%, with a maximum of 97% at pH 5. The desorption rate of La³⁺ decreased with the increase of pH, which was lower than <0.006% at pH > 6.12. This study may provide a solution for internal P pollution from lake sediments.     

Metal biosorption by two cyanobacterial mats in relation to pH, biomass concentration, pretreatment and reuse

The pH-dependent metal sorption by Oscillatoria- and Phormidium-dominated mats was effectively expressed by the Hill function. The estimated Hill functions can fruitfully predict the amount of metal sorbed at a particular initial pH. Pretreatment of biomass with 0.1 mmol L⁻¹ HCl was more effective than pretreatment with CaCl₂, HNO₃, NaOH, and SDS in enhancing metal sorption ability of the biomass. Desorption of metal ions in the presence of 100 mmol L⁻¹ HCl from metal-loaded mat biomass was completed within 1 h. After six cycles of metal sorption/desorption, sorption decreased by 6-15%. Only 6% and 11% of the biomass derived from the Oscillatoria sp.- and Phormidium sp.-dominated mats was lost during the cycling. The cyanobacterial mats seem to have better potential than several biomass types for use in metal sorption from wastewaters as they are ubiquitous, self-immobilized, and have good reusability.     

Assessment of the metal removal capability of two capsulated cyanobacteria, Cyanospira capsulata and Nostoc PCC7936

Two capsulated, exopolysaccharide-producing cyanobacteria, Cyanospira capsulata and Nostoc PCC7936, were tested with regard to their metal removal capability by using copper as model metal. The experiments, carried out with the sole cyanobacterial biomass suspended in distilled water and confined into small dialysis tubings, showed that C. capsulata biomass is characterized by the best efficiency in metal removal, with a q_max (maximum amount of copper removed per biomass unit) of 96 ± 2 mg Cu(II) removed per g of protein in comparison with the value of 79 ± 3 of Nostoc PCC7936 biomass. The experimental data obtained with both cyanobacterial biomass best fit the Langmuir sorption isotherm. The sorption of copper started from the first minutes of contact with the metal and attained the equilibrium state, when no more copper removal was evident, after 5 and 6 hours, for C. capsulata and Nostoc PCC7936, respectively. The best efficiency in Cu(II) removal was obtained at pH 6.1–6.2, while the presence of Mg²⁺ or Ca²⁺ reduced copper removal capability of both species to 60–70% of their q_max. The results showed that the biomass of C. capsulata and Nostoc PCC7936 possesses a high affinity and a high specific uptake for copper, comparable with the best performances shown by other microbial biomass, and suggest the possibility to use the capsulated trichomes of the two cyanobacteria for the bioremoval of heavy metals from polluted water bodies.     

Lanthanum biosorption by a Pseudomonas sp.: equilibrium studies and chemical characterization

Lanthanum biosorption by a Pseudomonas sp. was characterized in terms of equilibrium metal loading, model fitting, kinetics, effect of solution pH, lanthanum–bacteria interaction mechanism and recovery of sorbed metal. Lanthanum sorption by the bacterium was rapid and optimum at pH 5.0 with equilibrium metal loading as high as 950 mg g⁻¹ biomass dry wt. Scatchard model and potentiometric titration suggested the presence of at least two types of metal-binding sites, corresponding to a strong and a weak binding affinity. The chemical nature of metal–microbe interaction has been elucidated employing FTIR spectroscopy, energy dispersive X-ray analysis (EDX) and X-ray diffraction analysis (XRD). FTIR spectroscopy and XRD analysis revealed strong involvement of cellular carboxyl and phosphate groups in lanthanum binding by the bacterial biomass. EDX and the elemental analysis of the sorption solution ascertained the binding of lanthanum with the bacterial biomass via displacement of cellular potassium and calcium. Transmission electron microscopy exhibited La accumulation throughout the bacterial cell with some granular deposits in cell periphery and in cytoplasm. XRD confirmed the presence of LaPO₄ crystals onto the bacterial biomass after La accumulation for a long period. A combined ion-exchange–complexation–microprecipitation mechanism could be involved in lanthanum accumulation by the biomass. Almost 98% of biomass-bound La could be recovered using CaCO₃ as the desorbing agent.     

Zn buffering capacity and Zn accumulation in Swiss chard for some sludge-amended soils

Zinc sorption by soils can greatly affect its availability to plants. This study was conducted to determine the relationship between the Zn sorption capacity and plant Zn accumulation in five sludge-amended soils using Swiss chard (Beta vulgaris L.) as an indicator plant. Zinc sorption as a function of Zn concentration and pH was determined for the soils which received no sludge amendment; also DTPA (diethylenetriaminepentaacetic acid) extractable Zn was determined in all soils. Whereas the responses of DTPA-Zn and plant Zn to pH and the quantities of Zn sorbed were similar, the logarithm of DTPA-Zn accounted for only 82% of the variability in the logarithm of Zn accumulation by the plants. The variability was better explained when pH was included with DTPA-Zn in stepwise multiple regressions. The Zn buffering capacity, defined as the ratio of the change in quantity of Zn sorbed ( Zn_s) to the change in Zn solution concentration (Zn₁) (or Zn_s/Zn₁), and the estimated quantity of Zn sorbed were used as a basis to measure Zn intensity. Zinc intensity, which reflects Zn solution concentration, was the predominant factor controlling Zn accumulation by Swiss chard, judging from the good fit of the values of both parameters to the Michaelis-Menten equation. The maximum Zn accumulation was approximately 9 mmol kg^–1.Scientific paper no. 8901-29, Department of Agronomy and Soils, College of Agriculture and Home Economics Research Center. Washington State University, Pullman, WA 99164, USA.Scientific paper no. 8901-29, Department of Agronomy and Soils, College of Agriculture and Home Economics Research Center. Washington State University, Pullman, WA 99164, USA.     

Enhanced sorption of Cu2+ and Ni2+ by acid-pretreated Chlorella vulgaris from single and binary metal solutions

The influence of HCl pretreatment (0.1 mM) on sorption ofCu²⁺ and Ni²⁺ by Chlorella vulgariswas tested using single and binary metal solutions. The optimal initial pH forsorption was 3.5 for Cu²⁺ and 5.5 for Ni²⁺. Second orderrate kinetics described well sorption by untreated and acid-pretreated cells.The kinetic constant q_e (metal sorption at equilibrium) for sorptionof test metals from single and binary metal solutions was increased afterpretreatment of the biomass with HCl. The Langmuir adsorption isotherm wasdeveloped for describing the various results for metal sorption. In single metalsolution, acid pretreatment enhanced q_max for Cu²⁺ andNi²⁺ sorption by approximately 70% and 65%, respectively.Cu²⁺ and Ni²⁺ mutually interfered with sorption of theother metal in the binary system. The combined presence of Cu²⁺ andNi²⁺ led to their decreased sorption by untreated biomass by 19% and88%, respectively. However, acid-pretreated biomass decreased Cu²⁺and Ni²⁺ sorption by 15 and 22%, respectively, when both the metalswere present in the solution. The results suggest a reduced mutual interferencein sorption of Cu²⁺ and Ni²⁺ from the binary metal systemdue to the acid pretreatment. Acid-pretreated cells sorbed twice the amount ofCu²⁺ and ten times that of Ni²⁺ than the untreated biomassfrom the binary metal system. Acid pretreatment more effectively enhanced thesorption of Ni²⁺ form the binary metal solution. The total metalsorption by untreated and acid-pretreated biomass depended on theCu²⁺ : Ni²⁺ ratio in the binary metal system. Acidpretreatment of C. vulgaris could be an effective andinexpensive strategy for enhancing Cu²⁺ and Ni²⁺ sorptionfrom single and binary metal solutions.     

Biosorption and desorption studies of chromium (III) by free and immobilized Rhizobium (BJVr 12) cell biomass

Experiments with free cell biomass (cells + exopolysaccharides) ofRhizobium BJVr 12 (mungbean isolate) showed that amount ofCr³⁺ ion sorbed is influenced by the amount of biomass toCr³⁺ concentration ratio and time of contact. A ratio of 0.5 gfresh biomass to 10.0 ml 5.03 ppm Cr³⁺ sorbed 0.0275 mg Crequivalent to an uptake of 2.86 mg Cr g-¹ dry biomass and 1.0g: 10.0 ml sorbed 0.0366 mg Cr equivalent to an uptake of 1.9 mg Crg-¹ biomass. Immobilized cell biomass in ceramic beads and inaquacel (a porous cellulose carrier with a charged surface) were moreefficient than free cell biomass in adsorbing Cr(III). A reduction of49.7percnt; of Cr(III) for free cells, 95.6% for cells immobilized inceramic beads and 94.6% for cells in aquacel was achieved after 48hours under shaken conditions. Sorption capacities of immobilized cellbiomass in ceramic beads and aquacel ranged from 5.01 to 5.06 mg Crg^-1 dry cell biomass. The biosorption of Cr³⁺follows generally the Langmuir and Freundlich models of adsorption at lowCr³⁺ concentrations. The Langmuir constant for immobilizedcells in ceramic beads are: Q₀, 0.065 mmol Crg^-1 biomass; b (affinity constant), - 694 lmmol^-1 Cr and for cells in aquacel Q, 0.07 mmol Crg^-1 biomass; b, - 694 l mmol Cr g^-1 Cr. TheFreundlich constants are: K, 0.071 mmol Cr g^-1 biomass; n,0.13 g^-1 biomass l^-1 and for aquacel: K, 0.074mmol g^-1 biomass; n, 0.13 g^-1 biomass. Biotrapsmade up of immobilized cells in ceramic beads and aquacel were tested foradsorbing Cr(III) using two different flow rates: 0.5 ml/min and 1.5 ml/min.A significantly higher amount of Cr(III) was adsorbed at the lower flow rateof 0.5 ml/min. Biosorption of Cr³⁺ is competitive. Thetreatment of a waste water sample containing 6.03 ppm Cr³⁺ andother cations with the biomass reduced the Cr³⁺ concentrationto that much lower than for the test solution containing only Cr. Recoveryof biosorbed Cr(III) was by treatment at a different pH using dilute HClsolution. Recovery was higher for cells imbibed in ceramic beads thanaquacel. Percentage recoveries for cells in aquacel are 46.4% at pH1.0, 33.0% at pH 3.0 and 6.6% at pH 6.0–7.0. For cellsin ceramic beads, percentage recoveries are: 93.1% at pH 1.0,75.6% at pH 3.0 and 16.4% at pH 6.0–7.0. Biosorption ofCr³⁺ by cells immobilized in ceramic beads is reversible butonly partially for cells in aquacel.     

Removal of Pb2+ by Biomass of Marine Algae

New biosorbent material derived from ubiquitous marine algae has been examined in packed-bed flow for Pb²⁺ removal through sorption columns. Mixed biomass of marine algae has been used, consisting of representative species of the following algae: Ulva lactuca (green algae), Jania rubens (red algae), and Sargassum asperifolium (brown algae). A mixture of these three species showed a promising removal capacity for Pb²⁺ from aqueous solution. Lead uptake up to 281.8 mg/g dry algal mixture was observed. Equilibrium was achieved after 120 min. No significant effect of changing the flow rate on the removal capacity was noticed. It was found that Langmuir model expresses the system at pH 4. Mineral acids exhibited good elution properties (a mean of 93%) for recovery of sorbed biomass ions as compared with the tested alkalies (about 60%). Received: 21 December 1999 / Accepted: 24 April 2000     

Copper(II) and lead(II) sorption from aqueous solution by non-living Spirogyra neglecta

Dried biomass of Spirogyra neglecta rapidly sorbed the test metals and the process became saturated in 10-20min. Maximum sorption of Pb(II) [116.1mgg(-1)] and Cu(II) [115.3mgg(-1)] occurred at 0.1gl(-1) biomass and 100mgl(-1) metal concentration in the solution. Sorption of Cu(II) and Pb(II) occurred optimally at pH 4.5 and 5.0, respectively. Lead(II) and Cu(II) sorption were lesser from binary metal solution than from single metal solution. Lead(II) more severely inhibited Cu(II) sorption than vice versa thus reflecting greater affinity of Pb(II) for the biomass. NaOH pretreatment slightly enhanced the metal removal ability of the biomass. During repeated sorption/desorption cycles, Pb(II) and Cu(II) sorption decreased by 11% and 27%, respectively, at the end of the fifth cycle due inter alia to 10-15% loss of biomass. Nevertheless, Spirogyra appears to be a good sorbent for removing metals Cu(II) and Pb(II) from wastewaters.     

Siderophores sorbed on Ca-montmorillonite as an iron source for plants

Previous investigations have shown significant sorption of siderophores to the solid phase in soils, and clay surfaces in particular. The ability of plants to utilize Fe from this reservoir is therefore of great interest. This research focused on the ability of the hydroxamate siderophore ferrioxamine B (FOB) sorbed to Ca-montmorillonite – prevailing in soils – to supply Fe to peanuts (Arachis hypogeae L.). Remediation of Fe deficiency by the sorbed siderophore was found to be similar to that by the free (unsorbed) form. The concentration needed to achieve complete remediation of chlorosis was one order of magnitude higher than that of the optimal FeEDDHA [Fe-ethylenediamine-di(o-hydroxyphenylacetic acid)]. Using dialysis tubes, it was shown that Fe uptake from the sorbed siderophore is executed mainly via long-range pathways and does not require close proximity to the plant roots. It was hypothesized that the process involves chelating agents in solution, which transport the Fe from the immobilized siderophore and enable its uptake by the plant. Under calcareous conditions, the ability of the sorbed FOB to supply Fe was significantly impaired, probably as a result of inactivation of the bridging mechanism. Various possible shuttle compounds were examined. EDDHA was found to be a very efficient shuttle compound, which caused complete remediation of Fe deficiency, even under very harsh calcareous conditions. The findings support our hypothesis and imply the effectiveness of a ligand-exchange mechanism to strategy I plants (commonly attributed to strategy II plants). We suggest that the secretion of substances with chelating abilities, which is usually considered a less effective means of Fe acquisition mechanism, takes on more importance in this context.