Synthesis, characterization and application of Cu–TiO2/chitosan nanocomposite thin film for the removal of some heavy metals from aquatic media

Abstract

A novel Cu–TiO 2 /chitosan hybrid thin film was successfully prepared without any heat treatment process by sol–gel method on a polycarbonate substrate. Based on the photocatalytic activity and adsorption property of the entire thin film, a simple, reliable, reproducible and inexpensive method was developed for the removal of some heavy metals from aquatic media. The removal process of Pb 2+ and Cr 6+ was performed by flotation of coated polycarbonate substrate in the bulk of sample for a definite time in absence and presence of light. The effect of influential parameters in removal process, including thin film surface area, removal time, sample volume and pH was investigated and variation in selected ion concentrations was monitored using a graphite furnace-atomic absorption spectrometer. Considering the optimized conditions, effect of interference ions was studied and according relative standard deviation amounts, no evidence of interference was observed. The proposed method showed good reproducibility in a way that the amounts of relative standard deviation percentage values ( n  = 10) for Pb 2+ and Cr 6+ were obtained 4.303 and 3.865, respectively. The whole procedure showed to be conveniently applicable and quite easy to manipulate.


Background

In recent years, there has been considerable interest in organic/inorganic hybrid membrane composed of polymer matrix and inorganic nanoparticles [ 1 ]. The sol–gel method has been proved to be versatile and has been widely used in the preparation of organic–inorganic hybrid materials, non-linear optical materials, and mesomorphous materials [ 2 ]. To date, many kinds of inorganic nanoparticles, such as SiO 2 [ 3 ], Al 2 O 3 [ 4 ], Fe 3 O 4 [ 5 ], ZnO [ 6 ], ZrO 2 [ 7 ], CdS [ 8 ] and TiO 2 [ 912 ] have been introduced into polymer matrix to prepare polymer/inorganic nanoparticles membranes. Among these inorganic nanoparticles, TiO 2 has been proved to be excellent fillers because of its good stability, hydrophilicity, resisting and usage as an effective, photostable and reusable catalyst in the photodegradation of heavy metals as well as organic pollutants. It was proved that the standard reduction potential of the metals for the reduction reaction affected on the ability of TiO 2 in removal of metals [ 13 ]. However, there are still many limitations such as the recollection and reuse of nanometer TiO 2 . Thin film or the immobilized nanometer TiO 2 on different matrices can resolve the above problems [ 14 ].

Recently, TiO 2 /chitosan hybrid thin film is very promising. It is worth mentioning that chitosan is a biodegradable cationic polysaccharide with antimicrobial activity, nontoxic and excellent film-forming ability with good mechanical strength, with its higher permeability and cost-effectiveness caused wide application in the field of sensor [ 15 ]. The new double function hybrid thin film resolved the recollection and reuses limitation of nano-TiO 2 , and was used not only in degradation of dyes, but also in adsorption of heavy metal ions [ 1619 ]. Among heavy metals, lead (II) and chromium (VI) hold distinct position due to their toxicity, long-term and widespread usages [ 13 , 2023 ]. Therefore, development of a simple, effective method for the removal of these ions from aquatic media is of great importance.

In this work, Cu–TiO 2 /chitosan hybrid thin film was successfully prepared without any heat treatment process by sol–gel method on polycarbonate (PC) substrates. Subsequently, photocatalytic activity and adsorption property of the entire thin film were evaluated to the removal of chromium and lead ions from aquatic medium.

Methods

Materials

Chitosan (85 % degree of deacetylation) was purchased from Pelican Biotech and Chemicals Labs. Titanium tetra isopropoxide (TTIP) and Copper(II) Nitrate (both AR analytical grade, Merck Chemical Company) were used as Titanium and Copper sources for the preparation of the Cu–TiO 2 nanocomposite. Hydroxy propyl cellulose (HPC) was used as a dispersive agent. Other reagents were analytical grade and purchased locally. Double distilled water was used throughout the study. Furthermore, Pb(NO 3 ) 2 and K 2 Cr 2 O 7 , Cd(NO 3 ) 2 .4H 2 O, Ni(NO 3 ) 2 , FeCl 3 .6H 2 O and Zn(NO 3 ) 2 were all bought from Merck company.

Setup of photocatalytic reactor and removal study

The photocatalytic reduction studies of removal heavy metal were carried out using the photoreactor system, which consisted of a cubic borosilicate glass reactor vessel with an effective volume of 1,000 ml, a cooling water jacket and a 400 W H-P mercury vapor lamp positioned above center of cubic, as a light source. The spectrum of this lamp is shown in Fig.  1 . As it shown, large amount of the radiation is located in visible region. The reaction temperature was kept at 25° C by means of cooling water.

Fig. 1

Spectrum of high-pressure mercury vapor lamp

To investigate the photocatalytical properties of thin film an amount of 400 ml of a solution containing 50 ppb of Pb 2+ or Cr 6+ was utilized for removal study while the solution was stirred at 70 % of maximum efficiency of magnetic stirrer. In addition, all experiments were performed in presence and absence of light. Since the allowed levels of both Pb 2+ and Cr 6+ in drinking water are 5 ppb, all experiments were accomplished based on this level of concentration.

Synthesis of Cu–TiO2/chitosan thin film

The solutions were practically prepared based on the method of Yaghobi et al. [ 24 ], and the only difference was the addition of chitosan and Cu 2+ to the solution. The four types of Cu–TiO 2 /chitosan thin films were prepared using the sol–gel method. Solution 1 was a mixture of H 2 O and H 2 O 2 with volume proportions of 90:200, respectively. Chitosan was dissolved in 3 wt% acetic acid solution at 80 °C and then HPC was added to it (solution 2). Then solution 2 was added drop wise to solution 1 with vigorous stirring (solution 3). Afterwards, 12 ml TTIP was added to solution 3 dropwise with vigorous stirring and following the pH was raised to 7.0. The resulting solution was reflux for 10 h to obtain anatase sol. The four types of Cu–TiO 2 /chitosan thin films were prepared with some procedure by addition of different agents (refer to Table  1 ).

Table 1

Formulation of sample thin films

No. of samples

Samples content

Amount of HPC in solution (g gsol−1)

Amount of Cu2+ (molar ratio)

S1

TiO2/chitosan

S2

TiO2/chitosan

4.5 × 10−3

S3

TiO2/chitosan

2 %

S4

TiO2/chitosan

4.5 × 10−3

2 %

The plastic substrates were PC sheets with 1 mm thickness, which are cut into 35 mm × 25 mm pieces. The substrates were washed firstly by water and detergent and then rinsed with double distilled water (DDW). They were further cleaned in 2-propanol using ultrasonication and again rinsed with DDW and finally it was dried. The surface of PC sheets were treated chemically in a solution which is made by dropwise addition of 37.5 ml H 2 SO 4 to 4 g K 2 Cr 2 O 7 followed by adding 12.5 ml DDW. The substrates were immersed in this solution for 15 min, and then the solution was cooled down to room temperature. Cu–TiO 2 /chitosan layers were coated on PC substrates using dip coating at the 3 mm/s. For all the samples, a pre-coat of the amorphous TiO 2 sol was applied initially on the surface of PC substrates. This layer enhances the adhesion of composite layer and also it acts as a barrier to avoid the photocatalytic degradation of PC.

The preparation of this solution is described in details elsewhere [ 25 ]. Briefly, TTIP was dissolved in absolute ethanol with molar ratio TTIP/ethanol/HPC = 1/125/4.5 × 10 −3  g g sol −1 . Afterward, another mixture of absolute ethanol, HNO 3 , deionized water, Cu(NO 3 ) 2 with molar ratio of ethanol/HNO 3 /H 2 O/Nd(NO 3 ) 3  = 43/0.2/1/0.002 was added dropwise under vigorous stirring to it. The obtained transparent colloidal suspension was stirred for 45 min and then aged for 48 h to form gel solution. Subsequent layers of samples were deposited by 3 times dip coating. The samples were dried after each dip in a furnace at 110 °C for 15 min.

Characterization

The microstructure of the film samples was observed with a SEM-XL30 scanning electron microscope. The specific surface area of powder was measured by Beijing JWGB Sic. model JW-K. The phase composition of the powders was determined by a SCIFERT-3003 PTS X-ray Diffractometer. The FT-IR analysis was carried out for the samples by Thermo Nicolet NEXUS-870.

The photocatalytic properties of films were recognized by measuring the optical absorption of a 5 ppm methyl orange solution before and after the photodegradation by Varian UV–Vis spectrophotometer. The photocatalytic activity was investigated at the absorption peak (465 nm) before and after the photodegradation.

Results and discussion

The effect of Cu2+ and HPC on the microstructure

The FT-IR spectra of samples are shown in Fig.  2 , in wave number range of 4,000–400 cm −1 . The band around 3,440, 1,417, 1,421 and 1,418 cm −1 should be assigned to the symmetric vibration of surface hydroxyl group [ 1 , 2 , 14 , 26 ]. Hydroxyl band around 2,888 cm −1 is a characteristic of surface TiO 2 –OH functional group. Furthermore, absorption bands around 1,304 and 1,644 cm −1 were attributed to the amine or amide functional group [ 26 ]. The absorption bands around 1,640 and 1,314 cm −1 attributed to the bending vibration of N–H and stretching vibration of C–N, respectively [ 1 , 26 ]. The band around 620 cm −1 corresponded to the Ti–O–Ti stretching motion [ 25 , 26 ]. The band change around 1,418 cm −1 is due to hydrogen bond and protonation of the amine groups [ 2 ].

Fig. 2

The FT-IR spectra of the sol–gel with various amounts of HPC and CMC additives. a Sample 1, b sample 2, c sample 3, d sample 4

The SEM images are illustrated in Fig.  3 . Presence of HPC and Cu 2+ is influenced on particle size. Sample 2, which contains HPC, has the wide range of particle distribution with high agglomeration. This could be as a result of not using heat treatment process. Cu 2+ as a doping element was added to nanocomposite. In presence of Cu 2+ , nanocomposite particle size decreases and distribution range lowered and coating accomplished monotonously. To sum up, among these samples, samples 3 and 4 show improved uniformity. However, sample 3 was selected for removal study because of its loose structure.

Fig. 3

SEM images for the sample films a sample 1, b sample 2, c sample 3, d sample 4

The effect of Cu2+ and HPC on the anatase phase

XRD pattern of sample 3 is shown in Fig.  4 . The XRD measurements revealed that the sample possessed an anatase structure, and there was no evidence of rutile and mixed phases. Although the amount of anatase phase is not significant, it is important that this phase was formed without any heat treatment, which is a common process after sol–gel method.

Fig. 4

XRD patterns of sample 3

The self-cleaning ability of nanocomposite was investigated, as well. According to Fig.  5 , the methyl orange absorption decreased during contact time with nanocomposite thin film.

Fig. 5

Photodegradation of methyl orange solution under visible irradiation (sample 3)

Removal study using nanocomposite thin film

Parameters affecting removal process including thin film surface area, removal time, sample volume and pH were studied. Effect of interference ions along with reproducibility of method was investigated as well. Variation in selected ion concentrations was monitored using a graphite furnace-atomic absorption spectrometer.

Study on sorbent surface area and time of removal in presence and absence of light

Removal of lead ion was investigated using various surface areas including 131, 218, 306, 437 cm 2 of prepared nanocomposite thin film during 4 h. To study removal time, sampling was accomplished each 30 min while sample was exposed to light. Variation in lead concentration was monitored at room temperature. The entire test was also carried out at the same condition in absence of light. According to Fig.  6 a, among these surface areas, 131 cm 2 caused minimum removal recovery. From the economic point of view, using less amount of sorbent was used to decrease the removal time. Therefore, sorbent surface area of 218 cm 2 was selected.

Fig. 6

Effect of sorbent surface area and time of removal in presence and absence of light for lead ion

As Fig.  6 a shows removal time effect, there is no significant change after 60 min. So, this time chose as the optimum removal time. According to Fig.  6 b, the investigation on removal recovery in absence of light resulted in the same optimum condition.

The effect of removal time was also studied for Cr(VI) using thin film with 218 cm 2 surface area. As shown in Fig.  7 a, there is a considerable increase in removal efficiency up to 90 min for Cr 3+ and slight changes observed after this time while sample exposed to the light. As it is illustrated in Fig.  7 b, the removal efficiency for this ion in absence of light increased up to 150 min. After this time, the extraction efficiency was not increased significantly. Beyond longer equilibrium time, comparing results shows a more rapid removal rate for Cr 3+ in presence of light. It was proved that adsorption of Cr(VI) on TiO 2 in darkness is low and, therefore, the recovery of elimination process decreases in absence of light. Moreover, the amount of Cr(VI) adsorption raises in some extent with increasing irradiation time [ 27 ]. Since similar behavior was observed for Pb 2+ , it might be same mechanism happened.

Fig. 7

Effect of removal time for chromium ion a in presence and b in absence of light

Sample size effect

To study the effect of sample size, different volumes of solutions including 200, 300, 400, 500, 700, 800 ml was used. All these solutions were containing 50 ppb of both Cr 3+ and Pb 2+ ions and each solution exposed to 218 cm 2 of sorbent while it stirred. As the results shown in Fig.  8 a and b, the volumes of more than 400 ml resulted in significant decrease in removal efficiency. It seems that saturation of sorbent could lead to this decline. So the volume of 400 ml was selected for further studies.

Fig. 8

Effect of sample size on removal of a lead and b chromium ions from aqueous sample

pH effect

Since lead and chromium ions are precipitated and polymerized in alkaline media as Pb(OH) 2 , Cr(OH) 3 , Cr 2 (OH) 2 4+ , Cr 3 (OH) 4 5+ , the study on the effect of this parameter is accomplished under neutral and acidic condition in presence and absence of light. Therefore, the amount of 400 ml solutions containing 50 ppb of Pb 2+ and Cr 3+ with different pH in the range of 1–7 was prepared and then each solution was exposed to the sorbent with the surface area of 218 cm 2 for 4 h. As the results shown (Fig.  9 a, b), an improvement in removal recoveries is observed in pH 2 for Pb 2+ and Cr 3+ , when the sample exposed to the light. Decrease in the recoveries after and before the entire pH could be attributed to the solvation, hydrolysis, polymerization of these ions and occupation of active sites of chitosan by H + , respectively. In addition, it was proved that photocatalytic reduction of Cr(VI) in presence of TiO 2 was very sensitive to pH and this process is most efficient less than pH 3. At pH 5, separation of the catalyst and water occurred as Cr(III) ion formed a stable precipitate on the catalyst. The proposed reaction for the process was shown according reaction ( 1 ):

Fig. 9

Effect of pH on removal of a lead and b chromium ions from aqueous sample

Prairie et al. [ 27 ] revealed that thermodynamic driving force for Cr(VI) reduction on TiO 2 in basic aqueous solution was less than in acidic media. In addition, comparing the results in Fig.  9 a and b shows significant removing recoveries in presence of light for both ions.

Method performance

Investigation of interference ions

Since adsorption is a competitive phenomenon, the presence of other ions could affect on removal recovery. It is worth mentioning that interference ion is considered the one, which could affect on removal signal more than 5 %.

Firstly, the effect of chromium ion on adsorption of Pb 2+ in both presence and absence of light was investigated. For this study, an amount of 400 ml solution containing 50 ppb of each ion was used and sampling under optimized condition was accomplished. As shown in Table  2 , the removal process using nanocomposite thin film in presence of chromium ion was performed more significantly, while the sample was exposed to the light. Furthermore, there is no evidence of interference according to RSD amounts in both conditions.

Table 2

Effect of Cr 6+ as interfering ion on removal of lead ion (both ions are at concentration level of 50 μg/l)

Interfering ion

[Pb2+]a ± %RSD

In presence of light

In absence of light

Cr6+

16.321 ± 3.121

19.637 ± 4.253

a Remaining amount (μg/l)

Subsequently, same study was done in solutions containing 50 ppb of Pb 2+ or Cr 3+ along with the amounts of 5 ppm of Cu 2+ , Cd 2+ , Zn 2+ , Fe 2+ and Ni 2+ ions in 400 ml solution. The removal process was evaluated both under optimized condition for lead and chromium. As Tables  3 and 4 illustrated, the studied ions caused just a slight decrease in removal of both analytes in concentration level of 100 times more than their amounts. This decline could be attributed to occupation of chitosan active sites by the investigated ions.

Table 3

Investigation of interfering ions effect at concentration level of 5 mg/l on removal of lead ion (Initial concentration was 50 μg/l)

Interfering ion

[Pb2+]a ± %RSD

In presence of light

In absence of light

Cu2+

22.283 ± 4.128

27.762 ± 4.341

Cd2+

19.259 ± 3.257

21.323 ± 3.357

Zn2+

17.646 ± 3.431

20.238 ± 3.387

Fe2+

20.124 ± 4.390

24.204 ± 3.392

Ni2+

21.852 ± 3.380

23.567 ± 3.754

Cr6+, Fe2+, Ni2+

22.127 ± 3.121

25.377 ± 4.253

Cr6+, Cu2+, Cd2+, Zn2+, Fe2+, Ni2+

23.534 ± 2.987

26.125 ± 3.30

Cu2+, Cd2+, Zn2+, Fe2+, Ni2+

22.187 ± 4.125

25.976 ± 3.361

Cu2+, Zn2+, Fe2+, Ni2+

21.654 ± 3.323

25.351 ± 2.981

Cr6+, Cu2+, Cd2+, Fe2+

21.892 ± 2.325

24.943 ± 3.367

a Remaining amount (μg/l)

Table 4

Investigation of interfering ions effect at concentration level of 5 mg/l on removal of chromium ion (Initial concentration was 50 μg/l)

Interfering ion

[Cr6 +]a ± %RSD

In presence of light

In absence of light

Cu2+

28.117 ± 3.561

31.347 ± 2.794

Cd2+

26.222 ± 3.547

30.341 ± 4.308

Zn2+

26.796 ± 3.329

30.056 ± 2.984

Fe2+

26.405 ± 2.698

30.948 ± 3.657

Ni2+

27.228 ± 3.658

30.025 ± 3.476

Pb2+, Fe2+, Ni2+

25.453 ± 4.201

29.760 ± 3.763

Pb2+, Cu2+, Cd2+, Zn2+, Fe2+, Ni2+

29.748 ± 2.891

32.397 ± 3.851

Cu2+, Cd2+, Zn2+, Fe2+, Ni2+

27.989 ± 3.307

30.437 ± 2.3025

Cu2+, Zn2+, Fe2+, Ni2+

24.693 ± 3.429

28.920 ± 2.870

Pb2+, Cu2+, Cd2+, Fe2+

25.321 ± 3.117

29.104 ± 3.453

a Remaining amount (μg/l)

The results proved steady rising of removal recovery in presence of light. In addition, the dramatic potential of nanocomposite thin film for removing lead ion in comparison with chromium ions is sensible.

Reproducibility of method

Considering the optimized conditions, reproducibility of proposed method was assessed for each ion using 10 replicates. The amounts of RSD% were 4.303 and 3.865 for Pb 2+ and Cr 6+ , respectively.

Conclusions

The primary aim of this study was to develop a simple, reliable, reproducible and inexpensive method for the removal of heavy metals from aquatic environmental samples using photocatalytic reduction. To achieve this purpose, adsorption of lead and chromium ions on the surface of newly synthesized photocatalyst thin film, Cu–TiO 2 /chitosan nanocomposite, was investigated. The Cu–TiO 2 /chitosan nanocomposite film was prepared by sol–gel method without any heat treatment process. Presence of Cu 2+ as a dopant ion improves photocatalytic activity and could also increase adsorption property. The synthesized catalyst was coated on the surface of polycarbonate substrate which provides higher specific surface area and could float readily in the bulk of sample. In comparison with powdered catalysts, using thin film causes readily removing of catalyst from solution without any residue and could decline significantly the cost of water purification process as well. Influential parameters in removal recovery of selected heavy metals based on photocatalytic process were optimized and under this condition, the effects of other ions on removal recoveries were investigated and no evidence of interference was found. Furthermore, the results proved increase in removal recoveries in presence of light along with appropriate reproducibility. Considering feasibility of established method, selective removal of heavy metals could be possible using different doping agents to the entire catalyst.


Acknowledgments

The author is grateful to the experts of Laboratory of Shar-e-Rey Branch, Islamic Azad University for valuable technical assistance.

Conflict of interest

The authors declare that they have no competing interests.


References

  1. Yang et al. (2009) Chitosan/TiO2 nanocomposite pervaporation membranes for ethanol dehydration (pp. 3130-3137) 10.1016/j.ces.2009.03.042
  2. Tao et al. (2007) Tensile strength optimization and characterization of chitosan/TiO2 hybrid film (pp. 84-89) 10.1016/j.mseb.2006.12.013
  3. Khayet et al. (2005) Filled poly (2,6-dimethyl-1,4-phenylene oxide) dense membranes by silica and silane modified silica nanoparticles: characterization and application in pervaporation (pp. 114-122)
  4. Shen et al. (2006) A nanocomposite proton exchange membrane based on PVDF, poly(2-acrylamido-2-methyl propylene sulfonic acid), and nano-Al2O3 for direct methanol fuel cells (pp. 894-899) 10.1016/j.jpowsour.2005.11.070
  5. Han et al. (2006) Preparation of polysulfone-Fe3O4 composite ultrafiltration membrane and its magnetic field (pp. 9-16) 10.1016/j.memsci.2006.07.052
  6. Huang et al. (2003) Preparation and characterization of ZnO–PANI composite film (pp. 91-94)
  7. Bottino et al. (2002) Preparation and characterization of novel porous PVDF-ZrO2 composite membranes (pp. 35-40)
  8. Trigo et al. (2004) Preparation and characterization of ZnO–PANI composite film (pp. 2465-2469) 10.1016/j.eurpolymj.2004.06.027
  9. Vona et al. (2007) SPEEK-TiO2 nanocomposite hybrid proton conductive membranes via in situ mixed sol–gel process (pp. 156-161)
  10. Wu et al. (2008) Nafion and nano-size TiO2–SO42− solid superacid composite membrane for direct methanol fuel cell (pp. 336-343) 10.1016/j.memsci.2008.01.027
  11. Yang (2007) Synthesis and characterization of the cross-linked PVA/TiO2 composite polymer membrane for alkaline DMFC (pp. 51-60) 10.1016/j.memsci.2006.10.048
  12. Zhou et al. (2008) Water vapor permeability of the polyurethane/TiO2 nanohybrid membrane with temperature sensitivity (pp. 3002-3007) 10.1002/app.28427
  13. Kabra et al. (2004) Treatment of hazardous organic and inorganic compounds though aqueous-phase photocatalysis: a review (pp. 7683-7696) 10.1021/ie0498551
  14. Li et al. (2008) Synthesis of ion-imprinted chitosan–TiO2 adsorbent and its multifunctional performances (pp. 212-218) 10.1016/j.bej.2007.07.007
  15. Vargas et al. (2009) Characterization of chitosan oleic acid composite films (pp. 536-547) 10.1016/j.foodhyd.2008.02.009
  16. Zhang et al. (2011) Degradation characteristic of TiO2-Chitosan adsorbent on Rhodamine B and purification of industrial wastewater (pp. 1241-1246)
  17. Liu et al. (2011) Facile fabrication of porous chitosan/TiO2/Fe3O4 microspheres with multifunction for water purifications (pp. 137-140) 10.1039/C0NJ00593B
  18. Buraidah, M.H., Teo, L.P., Yusuf, S.N.F, Noor, M.M., Kufian, M.Z., Careem, M.A., Majid, S.R., Taha, R.M., Arof, A.K.: TiO2/chitosan-NH4I(+I2)-BMII-based dye-sensitized solar cells with anthocyanin dyes extracted from black rice and red cabbage. Int. J. Photoenergy 2011 , 1–11 (2011)
  19. Zubieta et al. (2008) Reactive dyes remotion by porous TiO2-chitosan materials (pp. 765-777) 10.1016/j.jhazmat.2007.07.043
  20. Ahmad et al. (2010) Cd(II), Pb(II) and Zn(II) removal from contaminated water by biosorption using activated sludge biomass 38(2) (pp. 153-158)
  21. Tao et al. (2009) Removal of Pb(II) from aqueous solution on chitosan/TiO2 hybrid film (pp. 718-722) 10.1016/j.jhazmat.2008.04.012
  22. Colón et al. (2002) Effect of ZrO2 incorporation and calcinations temperature on the photocatalytic activity of commercial TiO2 for salicylic acid and Cr(VI) photodegradation (pp. 185-199) 10.1016/S0926-860X(02)00051-0
  23. Selli et al. (1996) Humic acid-sensitized photoreduction of Cr(VI) on ZnO particles (pp. 598-604) 10.1021/es950368+
  24. Yaghoubi et al. (2010) Self cleaning TiO2 coating on polycarbonate: surface treatment, photocatalytic and nanomechanical properties (pp. 1562-1568) 10.1016/j.surfcoat.2009.09.085
  25. Aberoomand Azar et al. (2011) Effect of CMC and HPC mixture on the photocatalytic activity of Nd-TiO2/SiO2 film under visible light irradiation (pp. 37-44)
  26. Gomez-Serrano et al. (1998) Adsorption of mercury, cadmium and lead from aqueous solution on heat-treated and sulphurized activated carbon (pp. 1-4) 10.1016/S0043-1354(97)00203-0
  27. Prairie, M.R., Evans, L.R., Martinez, S.L.: Destruction of organics and removal of heavy metals in water via TiO 2 photocatalysis. In: Eckenfelder, W.W., Bowers, A.R., Roth, J.A. (eds.) Chemical Oxidation: Technology for the Nineties. Second International Symposium, pp. 428–441. JA Technomic Publishing Company, Lancaster, PA (1994)