New method for sequestration of silver nanoparticles in aqueous media: in route toward municipal wastewater
© The Author(s) 2016
Received: 6 January 2016
Accepted: 4 August 2016
Published: 26 August 2016
Nanomaterials are widely used in industry for their specific properties. Silver nanoparticles (Ag NPs) are largely used in several consumer products notably for their antibacterial properties and will likely be found in wastewater, then in the receiving environment. The development of a product capable to sequestrate those released contaminants is needed. Under environmental conditions, the biopolymer chitosan can generally coordinate the cationic metals. Ag NPs present unique properties due to their high surface/mass ratio which are promising for their sequestration.
The immobilization of chitosan on functionalized silica assisted by microwaves gives a sequestering agent of silver while being easily recoverable. The IR spectrum confirmed the immobilization of N,N–dimethylchitosan (DMC) on silica core. The immobilized DMC gave a percentage of sequestration of Ag NPs (120 µg L−1) in nanopure water of 84.2 % in 4 h. The sequestration efficiency was largely dependent of temperature. By addition of hydrosulfide ions, the percentage of sequestration increased up to 100 %. The immobilized DMC recovered a large portion of silver regardless the speciation (Ag NP or Ag+). In wastewater, the immobilized DMC sequestered less Ag NPs (51.7 % in 97 % wastewater). The presence of anionic (sodium dodecyl sulfate and sodium N–lauroylsarcosinate) and non-ionic surfactants (cetyl alcohol) increased the hydrophobicity of Ag NPs and decreased the percentage of sequestration.
The immobilized DMC is a promising tool for sequestrating such emerging pollutant at low concentrations in a large volume of sample that would allow the characterization of concentrated Ag NPs by transmission electron microscopy. The efficiency of the support to sequestrate would likely be influenced by the chemical environment of the Ag NP solution.
KeywordsAg NP Supported polysaccharide Silica Removal Wastewater Silver sulfide Organic matter
Nanomaterials are widely used in industry for their specific properties. A nanoparticle is defined as a particle possessing at least two dimensions measuring between 1 and 100 nm [1, 2]. In recent years, silver nanoparticles (Ag NPs) have been widely studied since they have a high surface/mass ratio that confers a higher reactivity. They are used in catalysis and for their antimicrobial properties in many areas of applications including consumer products and textiles [1–4]. In 2012, approximately 55 tons of Ag NPs were produced and used . The majority of Ag NPs in consumer products will be likely found in municipal wastewater treatment plants and exposure to aquatic organisms could result in different toxicological effects . The development of new sequestration techniques is therefore important tools for their removal .
Chitosan represents a rare example of cationic biopolymer that is mainly extracted from crustacean exoskeletons. This aminopolysaccharide is known as coagulant and flocculent  and for its capacity to bind transition metals. The alcohol and amino groups in raw chitosan allow the chelation of transition metals. At neutral pH, cationic metals are coordinated by unbounded electrons of nitrogen atoms [4, 8]. Applications of chitosan are limited by its insolubility in aqueous solutions and organic solvents. The protonation of amino groups lead to the solubilization of chitosan in diluted acid conditions. However, its sorption capacity  and utilization in wastewater treatment  are limited. Ag NP recovery methods have been developed including cloud point extraction with Triton X-114  and activated carbon . These methods work for high concentrations of Ag NPs only.
Silica is a widely used support for chromatography and for supported reagents and catalysts . Silica with silanol groups on the surface and a large surface area allow coupling with many molecules including polymers [8, 12]. The immobilization of polymers on silica can be used for a variety of applications such as biosensors and drug delivery, for instance . The use of polymers in the catalytic reactions of chemicals and biological processes is growing. Supported polymers offer opportunities in the production of chemical and new intermediates . Supported polymers are been used in various combinatorial chemicals, in the research for new drugs, in the oil refinery and in catalysis and biosynthesis [14, 15]. Supported polysaccharides allow the formation of support with high surface for sorption where some polysaccharides are used to immobilize various molecules such as enzymes. Some studies have been realized to immobilize chitosan on a support made of silica gel . Immobilized chitosan can bound copper ions  or acted as affinity support for the adsorption of proteins . These syntheses imply more than three steps that necessitate several days and require the removal of starting compounds. Moreover, concentrations of heavy metal ions were as high as the order of milligram per liter. The microwave-assisted heating is a technique with many advantages including the ability to accelerate chemical reactions and to achieve higher heating rates and better reaction yields [18, 19].
Therein, we report the preparation of immobilized chitosan derivative on modified silica and the assessment of potential sequestration of Ag NPs in municipal wastewater. In this work, the removal capacity of this sequestration was then studied against two other silver species (ionic silver and Ag2S NPs).
Results and discussion
Formation of immobilized N,N–dimethylchitosan (DMC) on modified silica
With the DMC/silica ratio used during the reaction, the nitrogen/carbon ratio of supports was quite constant within a variation of 5 %, a small decrease is observed for polymer/silica ratio of 2–5 (Additional file 1: Figure S3). The nitrogen percentage increases until a DMC/silica ratio of 1 and after is relatively constant as well demonstrating that immobilization of DMC on silica is saturated.
Sequestration of silver nanoparticles
It is possible to qualitatively verify the sequestration of a solution of Ag NPs (120 µg L−1) by comparing UV–visible spectra before and after sequestration (Additional file 1: Figure S4). The intensity of the absorption band of citrate-coated Ag NPs at 400 nm decreases after sequestration that was attributed to the reduction of Ag NP concentration.
Percentage of sequestration of Ag NPs, Ag+ and Ag2S NPs by immobilized DMC at different conditions
Time of sequestration (h)
Percentage of sequestration (%)a
59.9 ± 4.1
77.7 ± 3.9
84.2 ± 5.8
3.5 ± 0.2
26.9 ± 0.5
1.34 mg L−1 of Ag+
100.0 ± 0.0
4.25 mg L−1 of Ag+
84.2 ± 4.8
4.25 mg L−1 of Ag+; with immobilized TMC
28.0 ± 8.4
With immobilized TMC
23.0 ± 1.4
+16.0 mg L−1 of Ag2S
24.1 ± 9.1
Zeta potential of Ag NPs (120 µg L−1) by addition of electrolytes
Zeta potential of Ag NPs (mV)a
−7.4 ± 1.2
20 mg L−1 NaSH
−49.3 ± 0.8
35.2 mg L−1 SDS
−9.0 ± 1.3
20 mg L−1 NaSH; 8.8 mg L−1 SDS
−58.2 ± 3.1
Percentage of sequestration of Ag NPs (120 µg L−1) by immobilized DMC with addition of NaSH
NaSH concentration (mg L−1)
Molar ratio NaSH/Ag NP
Percentage of sequestration (%)a
84.2 ± 4.8
99.5 ± 0.2
100.0 ± 0.0
99.6 ± 0.6
Percentage of sequestration of Ag NPs by immobilized DMC at differents conditions after 4 h
Percentage of sequestration (%)a
3.6 µg L−1 SDS
27.0 ± 1.4
8.8 mg L−1 SDS
21.6 ± 7.9
35.2 mg L−1 SDS
23.5 ± 3.3
11.8 mg L−1 SLS
2.7 ± 0.6
8.8 mg L−1 SDS; 20 mg L−1 NaSH
6.0 ± 0.8
20 mg L−1 NaSH; 8.8 mg L−1 SDS
6.4 ± 0.6
0.335 µg L−1 cetyl alcohol
2.4 ± 0.5
1.34 µg L−1 cetyl alcohol
5.9 ± 0.1
Percentage of sequestration of Ag NPs (120 µg L−1) by immobilized DMC in wastewater after 4 h
Composition of aqueous solutions
Percentage of sequestration (%)a
10 % wastewater
90.7 ± 0.2
50 % wastewater
84.6 ± 7.6
97 % wastewater
51.7 ± 6.7
97 % wastewater filtered GF/F 0.7 μm
27.4 ± 5.8
Characterization of immobilized DMC after sequestration of Ag NP
Effect of temperature on sequestration
By varying the temperature during sequestration, it was possible to determine the activation energy from the Arrhenius relationship. A plot of 1/T according to the natural logarithm of the first order rate constant is performed. The slope of the line corresponds to the activation energy divided by the gas constant (8.314 J K−1 mol−1). The activation energy was 803 J mol−1. The immobilized DMC sequesters 3.5 % at 275 K, 84.2 % at 298 K and 26.9 % at 313 K (Table 1, lines 3–5). Sequestration was largely affected by temperature where the best sequestration was obtained at 25 °C. At 2 °C, the activation energy is not completely attained and a low amount of Ag NP is sequestered by the immobilized DMC. This energy is achieved at room temperature. Thus, environmental samples could be easily handled. At 40 °C, the activation energy is reached and environmental temperature increases the molecular motion.
The increase of temperature in the reaction medium would result in competitive reactions explaining the low percentage of sequestration. When modifying the order of addition between NaSH and SDS, the percentage of sequestration of Ag NPs is similar, 6.0 % when SDS (Table 4, line 23) is added first compared to 6.4 % when NaSH (line 24) is added first. These observations indicate that the process is reversible and that there is competition between anions.
SiliaBond® propyl bromide (particle size 40–63 µm, loading 1.69 mmol/g, specific surface area 470–530 m2 g−1), chitosan (viscosity <20 mPa s (cP), degree of deacetylation >95 % from shrimp exoskeletons, Pandalus borealis) and silver nanoparticles (20 nm, 0.02 mg/mL) coated with citrate were purchased respectively from Silicycle (Quebec), Primex (Iceland) and TedPella (USA). All other reagents were bought from Aldrich except sodium N-lauroyl sarcosinate (ICN biomedicals). Sodium dodecyl sulfate (SDS) was reagent plus grade. Concentrated nitric acid (≥69 % v/v) and hydrogen peroxide (≥30 % v/v) were ultrapure grade whereas other reagents were ACS grade. N,N–dimethylchitosan (DMC) was synthesized according to literature . Nanopure water was obtained from a Barnstead nanopure infinity ultrapure water system. Ionic silver comes from AgNO3. All materials were washed with nitric acid and rinsed with nanopure water before use. Municipal wastewater was collected on June 18, 2013 as a 24 h-composite sample from aerated lagoons at Rimouski-Est station (Quebec, Canada). The sample was stored at −20 °C. Municipal wastewater had 0.61 g L−1 of total matter and 0.46 g L−1 of dissolved matter. The microwave heating was realized with a Mars microwave system from CEM Corporation using MarsXpress™ close-vessels. Infrared and Raman spectra were recorded on a Thermo scientific Nicolet iS10 spectrometer with Smart Omni transmission in KBr pellets and on a Thermo scientific DXR Raman Microscope directly on solid, respectively. Elemental analyses were determined using analyzer Costech instruments elemental combustion system 4100. NMR spectra were performed using an Avance III HD 600 MHz NMR from Bruker by NanoQAM (Université du Québec à Montréal). UV–visible spectra were recorded on a Cary 100 Bio UV–visible spectrophotometer from Varian. ICP–MS measurements were achieved on an Agilent 7500c spectrometer octopole reaction system using argon plasma at 7000 K, autosampler ASX-520 Cetac and software ChemStation v.3.04. Analyses from MP-AES were achieved on an Agilent Technologies 4200 MP-AES with a nitrogen generator, autosampler ASX-520 Cetac and MP Expert software version 188.8.131.5245. Zeta potentials were measured by Malvern zetasizer nano ZS with Malvern Zetasizer software version 7.11. Solutions were placed in disposable capillary cells (DTS1070) of Malvern which were washed with nanopure water, nitric acid 10 % v/v, nanopure water and ethanol. A single measurement with zetasizer had 100 runs in manual mode, the zetasizer took three measurements with a delay of 45 s. Zeta potentials of Ag NPs were measured in nanopure water excepted when presence of salts is mentioned. Transmission electron microscopy (TEM) was recorded on a Delong Instruments model LVEM5. Before TEM analyses, dried supports were ground in an agate mortar and then suspended in dry ethanol. A few drops of solution were placed on a copper grid of 400 mesh covered with a hexagonal carbon film provided by Ted Pella Inc. (Redding, CA). SEM microscope was a JEOL JSM-6460 LV scanning electron microscope. Dried supports were placed on a carbon tape and placed on the sample holder. The uncertainty of zeta potential measurements was estimated using the standard deviation between three data collections. The uncertainty on percentage of sequestration comes from the standard deviation between two independent sequestrations.
General procedure for the preparation of immobilized DMC on modified silica (example for polymer/silica ratio 1:1)
A suspension containing DMC (0.30 g), sodium carbonate (0.90 g) and SiliaBond® propyl bromide (0.32 g) was prepared in a mixture of methanol/water (8 mL, 1:9 v/v). In MarsXpress™ close-vessels, the suspension was heated by microwave at 100 °C during 5 min and the temperature was maintained at 100 °C during 15 min using a maximum power of 1600 W. The solution was allowed to reach room temperature (rt). The solid was filtered and suspended in a 1 % (v/v) aqueous acetic acid solution (50 mL) during 15–30 min. The solid was filtered and dried at normal atmosphere. A white solid was obtained (0.33 g). The solid was ground to a size of 250 μm. IR υ (cm−1) 3430 (OH), 2900 (CH), 1558 (CH2 def), 1462 (CH3 def), 1380–1265 (C–N), 1110–1090 (C–O pyranosyl). Raman υ (cm−1) 634, 562 (C–Br).
General procedure for the N-methylation of immobilized DMC on modified silica (polymer/silica ratio 1:1)
A suspension containing TMC (0.30 g), sodium carbonate (0.90 g) and SiliaBond® propyl bromide (0.32 g) in a mixture of methanol/water (8 mL, 1:9 v/v). In MarsXpress™ close-vessels, the suspension was heated by microwave at 100 °C during 5 min and the temperature was maintained at 100 °C during 15 min using a maximum power of 1600 W. The solution was allowed to reach rt. The solid was then filtered and dried under normal atmosphere. The solid was ground to a size of 250 μm.
Procedure for formation of Ag2S nanoparticles
The synthesis method of Ag2S nanoparticles was adapted from Xiang and coworkers  and Brelle and coworkers . Silver nitrate (68 µmol, 11.5 mg) was added to a stirred solution of l-cysteine (68 µmol, 8.2 mg) in 10 mL ethanol. After 15 min, the solution was transferred into a 15 mL Teflon tube. The tube was placed in 120 mL high pressure reactor from Parr Instrument. The reactor was heated at 180 °C during 10 h after that it was allowed to reach rt. The resulting precipitate was centrifuged at 3000 rpm during 10 min and washed using nanopure water and absolute ethanol several times. The dark precipitate was dried at 60 °C during 6 h. The black, dried precipitate was then put into a tube with ethanol and placed in a bath sonicator for 5 min. The solution was decanted for 1 h. The suspension was recovered and evaporated. The Ag2S NP mean size of 77.1 ± 56.8 nm was determined by TEM.
General procedure of sequestration of silver nanoparticles
Ag NP solution was prepared by dilution (factor 33×) of the commercial stock solution. In a Falcon tube (15 mL), the Ag NP solution (10 mL) and immobilized DMC on silica (0.100 g) were stirred with a magnetic bar during 4 h. The sequestrations were carried out in duplicate. The suspension was then centrifuged at 1000×g for 5 min. The supernatant was first collected and the residual solid was filtered (Whatman cellulose filter papers grade 2) and dried under normal atmosphere. The samples were placed in the dark at 4 °C until further analysis. IR of immobilized DMC after sequestration υ (cm−1) 3430 (OH), 2900 (CH), 1651 (C = O in COOH), 1557 (CH2 def), 1110–1090 (C–O pyranosyl).
Sample preparation prior to ICP–MS and MP-AES analyses
Dried support (0.100 g), concentrated nitric acid (6 mL) and hydrogen peroxide (1 mL) were mixed in open flasks until the complete gas evolution during at least 2 h. The flasks were closed and heated to 70 °C in a hot bath for an additional 2 h. The supernatant (2 mL) was digested in the same way than for the support except that 4 mL of nitric acid was used. The samples were stored in dark at 4 °C until ICP-MS or MP-AES analyses. All analyses were performed with the ICP-MS except analyses with TMC immobilized, Ag2S, Ag NPs at 2 and 40 °C, NaSH with SDS and SLS that have been made by MP-AES. The detection of 107Ag was used to measure the total silver in ICP–MS. The limit of detection for silver by ICP–MS was 0.04 µg L−1.
The synthesis of immobilized DMC on silica meets some principles of green chemistry [31, 32], for example, by using renewable products and microwave-assisted heating. Ag NPs are retained in the immobilized DMC by electrostatic interactions. When Ag NPs are highly negatively charged, for example by addition of NaSH, interactions are stronger and thus the sorption efficiency increases. Sequestrations are also highly dependent of hydrophobicity of Ag NPs coming from surfactants or organic matter that would decrease the electrostatic interactions with Ag NPs and lower the sorption efficiency. In a more complex environment, many factors likely influence the interactions between Ag NPs and immobilized DMC resulting in lower sorption capacity.
Immobilized polysaccharides as chitosan derivatives could serve as a promising approach for retrieving or removing emerging pollutants and heavy metals due to the chelation of the nitrogen atom. The immobilized DMC can be used on large volume samples and at low metallic pollutant concentrations. Sequestration optimizations should be carried out to increase selectivity and sensitivity of the method for potential number of uses.
MLR carried out the syntheses and the sequestration experiments and drafted the manuscript. CG and JG conceived of the study, and participated in its design and coordination and helped interpreting data and writing up the manuscript. All authors read and approved the final manuscript.
We thank the Natural Sciences and Engineering Research Council of Canada (NSERC) and the Chemical Management Plan (CMP) of Environment Canada for their financial support. We also acknowledge professor Émilien Pelletier (TEM), Mr. Mathieu Babin (ICP-MS) and Mr. Claude Belzile (SEM) for their supports.
The authors declare that they have no competing interests.
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