5.2
Impact Factor
Generic selectors
Exact matches only
Search in title
Search in content
Post Type Selectors
Search in posts
Search in pages
Filter by Categories
Corrigendum
Current Issue
Editorial
Erratum
Full Length Article
Full lenth article
Letter to Editor
Original Article
Research article
Retraction notice
Review
Review Article
SPECIAL ISSUE: ENVIRONMENTAL CHEMISTRY
5.3
Impact Factor
Generic selectors
Exact matches only
Search in title
Search in content
Post Type Selectors
Search in posts
Search in pages
Filter by Categories
Corrigendum
Current Issue
Editorial
Erratum
Full Length Article
Full lenth article
Letter to Editor
Original Article
Research article
Retraction notice
Review
Review Article
SPECIAL ISSUE: ENVIRONMENTAL CHEMISTRY
View/Download PDF

Translate this page into:

Original article
10 (
2_suppl
); S3459-S3467
doi:
10.1016/j.arabjc.2014.02.008

Polyaniline nanofibers and nanocomposites: Preparation, characterization, and application for Cr(VI) and phosphate ions removal from aqueous solution

Polymer Research Unit, College of Science, Mustansiriya University, Baghdad, Iraq

⁎Corresponding author. Tel.: +964 7703608825. tariq_pru@yahoo.com (Tariq S. Najim)

Disclaimer:
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.

Peer review under responsibility of King Saud University.

Abstract

Interfacial and rapid-mixing polymerization were used for preparation of polyaniline nanofiber (PANI). PANI nanocomposites were prepared by in situ oxidative polymerization of aniline in acidic medium using ammonium persulphate as initiator in the presence of natural silica (PANIS), acid treated natural silica (PANISA), fiber glass (PANIFG), and poly(ethylene terephthalate) powder from waste bottles (PANIPET). The pure PANI nanofibers and their nanocomposites were characterized by FTIR, X-ray diffraction (XRD) and Scanning Electron Microscope (SEM). The characteristic absorption bands of polyaniline nanofiber in pure polyaniline and nanocomposites were observed by FTIR. XRD also confirms the formation of PANI nanofiber, the SEM images have clearly shown the formation of pure PANI nanofiber alone and in the nanocomposites. The nanocomposites were used for removal of Cr(VI) and phosphate ion pollutants from aqueous solutions. The adsorption experiments reveal that PANISA nanocomposite was potential for removal of Cr(VI) and phosphate. PANISA nanocomposite takes less time to reach adsorption equilibrium and less amount of PANISA was needed to achieve maximum adsorption in comparison with other nanocomposites. This behavior was attributed to the large surface area, due to, increase in number of pores and channels in the structure of PANISA after treatment with acid. It was also found that the Pseudo-second-order kinetic model well represents the experimental data for all nanocomposites.

Keywords

Polyaniline nanofibers
Nanocomposites
Cr(VI) and phosphate
Adsorption
1

1 Introduction

Polyaniline nanofiber has become one of the most attractive conducting polymers due to high stability, easy methods of synthesis, feasibility of electrical conductivity control by changing either the protonation state or the oxidation state and finally the low cost of the aniline monomer (Ding et al., 2008; Kim et al., 2000; Guo and Zhou, 2007). PANI is either totally insulating or electrically conductive, depending on the oxidation state and protonation level. Only in the intermediate oxidation state, the protonated emeraldine form, is conductive Fig. 1. The fully reduced leucoemeraldine and fully oxidized pernigraniline are insulating materials (Li et al., 2009).

Schematic diagram showing the chemical structure, synthesis, reversible acid/base doping/dedoping, and redox chemistry of PANI (Li et al.,2009).
Figure 1
Schematic diagram showing the chemical structure, synthesis, reversible acid/base doping/dedoping, and redox chemistry of PANI (Li et al.,2009).

PANI nanofibers have received much attention due to their superior properties compared to the conventional bulk PANI (Virji et al., 2004; Wang et al., 2004; Huang et al., 2004). PANI nanofibers show enhanced water processability (Li and Kaner, 2005), and improved acid–base sensitivity and time response when they are exposed to chemical vapor as they have porous characteristic resulting in large surface area. On the other hand, PANI nanofibers have numerous applications, including electric devices, flash welding (Huang, 2006), sensors and actuators (Densakulprasert et al., 2005; Gao et al., 2003), rechargeable batteries (Ghanbari et al., 2007), electromagnetic shielding devices and anticorrosion coating (Huang and Kaner, 2004). Besides that polyaniline nanocomposites in its salt form have the ability to remove anionic pollutants from waste water. Hexavalent chromium is one of most toxic heavy metal ions; Chromium exists in two stable oxidation states Cr(III) and Cr(VI). The Cr(VI) state is of particular concern, because this form is hazardous to health due to carcinogenic properties, the maximum permissible levels for Cr(III) and Cr(VI) ions in waste water are 5 and 0.05 mg/L, respectively (Karthikeyan et al., 2005). Many methods were used to remove toxic metal ions from water, but most of these methods have many disadvantages including incomplete metal removal, use of expensive equipment, and higher energy consumption. Adsorption remains the most economical and widely used process for removal of toxic metal ions from waste water. Polyaniline nanocomposites have been widely used as adsorbents for removal of pollutants from aqueous solution, because bare polyaniline particles or nanofibers are generally aggregated in solution, which lowers the adsorption capacity and slow down the kinetics. The adsorption capacity could be enhanced by removing this aggregation. So, polyaniline composites and nanocomposites had been used for controlling aggregation (Ansari, 2006; Ansari et al., 2011; Keivani et al., 2009; Ansari and Raofie, 2006A; Ansari and Raofie, 2006B; Kanwal et al., 2012; Zheng et al., 2012; Zhang et al., 2011). Photodegradation of methylene blue by polyaniline-titanium dioxide nanocomposites (PANITiO2) was studied by (Ahmed and mondal, 2012), it was found that OH. radicals play an important role in the degradation of methylene blue and its intermediates. Polyaniline/α-zirconium phosphate nanocomposite (PANi/α-ZrP) was synthesized and used as adsorbent for removal of methyl orange (MO) in water environment, a synergistic effect of PANI and α-ZrP on promoting the adsorption of MO was observed (Wanq et al., 2012).

This work focuses on the synthesis and characterization of PANI nanofibers via interfacial and rapid mixing polymerization as well as its nanocomposites by in situ polymerization of aniline with the following materials: natural silica (S), natural silica pretreated with acid (SA), fiber glass powder (FG), and poly(ethylene terephthalate) PET powder from waste bottles. These fillers have been used as cheap and available materials for nanocomposites’ preparation. Application of these nanocomposites for removal of Cr(VI) and phosphate ions from aqueous solution was investigated, kinetics of the adsorption were also explored.

2

2 Experimental

2.1

2.1 Instrumentation

Water bath shaker type Lab. Companion BS-11, digital scale KERN-ABS, UV–visible spectrometer, CARY 100 Conc, pH meter type Trans BP 300, Scanning Electron Microscope (SEM) model Philips XL series 30, Shimadzu 8400 FTIR and Shimadzu-XRD 6000 were employed in this work.

2.2

2.2 Materials

Ammonium peroxydisulphate (APS), hydrochloric acid, sodium hydroxide and potassium dihydrogen phosphate were of analytical grade and used as received, aniline was double distilled under vacuum pressure; deionized water was used throughout this work. Powdered PET was obtained by grinding waste bottles in a small grinder after shredding to a small pieces, the PET powder was washed several times with deionized water then acetone. PET powder was sieved with ⩽500 μm. Natural silica (S) of particle size 150–200 μm was washed with deionized water and dried, acid treated natural silica (SA) was prepared by treating dried natural silica with 0.1 M HCl for overnight then washed with deionized water and dried, fiber glass was obtained by grinding chopped strand fiber glass, then treated with acetone for 3 h and dried.

2.3

2.3 Preparation of PANI nanofiber

PANI nanofibers were prepared by two methods: interfacial and rapid mixing polymerizations (Jiazing and Richard, 2004). In the former toluene was used as an organic phase, in which aniline was dissolved, and aqueous phase containing APS and the doping acid (hydrochloric acid 1 M). The aniline was polymerized at the interface between the two phases. In the latter the polymerization was performed by rapid mixing of two solutions, aniline in acidic deionized water and APS in acidic deionized water into a beaker and the mixture was stirred moderately with a magnetic bar at 5–10 °C. In both methods the polymerization lasted for 3 h, the doped PANI was filtered and washed with plenty of distilled water then with ethanol and acetone to remove all unreacted aniline, oligomers and impurities, then dried.

2.4

2.4 Preparation of nanocomposites

The polyaniline nanofiber composites were prepared by in situ polymerization of aniline in the presence of S, SA, FG and PET in hydrochloric acid solution by rapid addition of a specified amount of APS in 1 M HCl to the mixture then was moderately stirred using magnetic bar. After 3 h, the product was filtered and washed with distilled water then ethanol and acetone to remove unreacted aniline, oligomers and impurities then dried in an oven at 80 °C for 6 h and stored in a sealed container.

2.5

2.5 Adsorption experiments

A stock solution of potassium dichromate and potassium dihydrogen phosphate of 1000 mg/L was prepared separately. From these stock solutions different concentrations of Cr(VI) and phosphate were prepared by dilution of specified volume of the stock solution. All batch experiments were carried out by mixing 50 ml of certain concentration of Cr(VI) or phosphate with certain amount of nanocomposite in a water bath shaker for definite time interval. At the end of each adsorption experiment the solution was made alkaline at pH ⩾ 12, and the residual Cr(VI) was determined using UV–Visible spectrophotometer (Ansari, 2006), residual phosphate was also determined spectrophotometrically after complexation with ammonium molybdate and sodium sulfide in concentrated sulfuric acid. For calibrating the UV–Visible spectrophotometer, standard samples of dichromate and phosphate were prepared and the corresponding absorption for each concentration was measured at λmax 372 nm and λmax 715 nm, respectively. The linear regression curve was drawn between the absorption and concentration for each sample, Figs. 2 and 3. The adsorption capacity of the nanocomposites for Cr(VI) and phosphate was calculated by the following equation:

(1)
q e = ( C - C e ) V W The removal percentage of Cr(VI) and phosphate were calculated using the following equation:
(2)
R % = C o - C e C o × 100
where, Co and Ce are the initial and final concentrations (mg/L) of Cr(VI) or phosphate ions, W is the adsorbent weight (g) and V is the volume of solution (L).
Calibration curve between the concentration of dichromate and absorbance at λmax 372 nm.
Figure 2
Calibration curve between the concentration of dichromate and absorbance at λmax 372 nm.
Calibration curve between the concentration of phosphate ion and absorbance at λmax 715 nm.
Figure 3
Calibration curve between the concentration of phosphate ion and absorbance at λmax 715 nm.

3

3 Results and discussions

3.1

3.1 Characterization of PANI nanofiber

Pure polyaniline nanofibers were prepared by interfacial and rapid mixing methods, whereas, the PANI nanocomposites were prepared by rapid mixing method. Analysis of the prepared nanofibers was carried out by Scanning Electron Microscope, X-ray diffraction and FTIR. The presence of the characteristic absorption peaks of PANI in the FTIR spectrum indicates the successful polymerization of aniline via interfacial or rapid mixing methods and nanocomposites, as shown in Fig. 4 and Table 1.

FTIR spectrum of PANI nanofiber by interfacial polymerization.
Figure 4
FTIR spectrum of PANI nanofiber by interfacial polymerization.
Table 1 Characteristic FT-IR band absorption frequencies of PANI nanocomposites.
Vibrational assignment Adsorbents
PANI cm−1 PANISA cm−1 PANIS cm−1 PANIPET cm−1 PANIFG cm−1
N—H streching 3412 3450 3448 3433 3462
N⚌Q⚌N 1554 1518 1575 1576 1575
N—B—N 1475 1487 1496 1251 1236
C—N streching 1296 1290 1298 1296 1300
C⚌N streching 1244 1240 1242 1238 1238
Aromatic C—N—C 1114 1122 1120 1103 1109
C—H out of plane bending 798 786 796 794 798
C—Cl streching 704 692 694 694 696

B = Benzenoid.

Q = Quinoid.

The X-ray diffraction confirms the formation of PANI nanofiber, two characteristic peaks around 2θ = 20° and 2θ = 25° presented in the XRD pattern of the PANI nanofiber Fig. 5, the same XRD pattern was obtained by other researchers (Yangyong and Xinli, 2007). According to the studies reported by (Lunzy and Banka, 2000; Banka and Lunzy, 1999) and (Chaudhari and Kelkar, 1996) the nanofibers are in partial crystallinity. The partial crystallinity of polyaniline nanofiber may be due to the amine and imine groups in the structure of doped PANI, which can form stronger intermolecular and intramolecular hydrogen bonds. SEM images of PANI nanofiber after completion of polymerization by interfacial and rapid-mixing techniques as well as nanocomposites, are clearly shown in Fig. 6, with PANI nanofibers of diameter of 30–80 nm.

XRD of polyaniline nanofiber.
Figure 5
XRD of polyaniline nanofiber.
SEM images of PANI nanofiber (A) interfacial (B) rapid mixing (C) PANIFG (D) PANIPET (E) PANISA (F) SA.
Figure 6
SEM images of PANI nanofiber (A) interfacial (B) rapid mixing (C) PANIFG (D) PANIPET (E) PANISA (F) SA.

3.2

3.2 Adsorption of Cr(VI) and phosphate

The adsorption is the affinity of interaction between the adsorbent active sites on its surface and the adsorbate molecules. The fillers S, SA, PET powder, and FG powder were used to prepare the PANI nanocomposites. The pH of the adsorption medium is an important factor that controlled the adsorption process; therefore, the effect of pH on adsorption was investigated. It was observed that maximum removal of Cr(VI) was obtained at pH 2 onto all nanocomposites, while, the maximum removal of phosphate was obtained at pH 1 onto PANIS and PANISA. Generally the removal percentage decreased with increasing pH for adsorption of both adsorbates onto nanocomposites. The removal percentage of Cr(VI) onto PANIS was reduced from 95% at pH 2 to 34% at pH 6, from 99% at pH 2 to 55% at pH 6 onto PANISA, from 84% at pH 2 to 36% at pH 6 onto PANIFG and from 84% at pH 2 to 34% at pH 6 onto PANIPET. Whereas, the removal percentage of phosphate by PANIS was reduced from 21% at pH 1 to 7% at pH 6 and from 40% at pH 1 to 16% at pH 6 by PANISA. The higher removal percentage of Cr(VI) onto PANISA is attributed to the pores and channels present in natural silica that were opened after treating with acid, Fig. 6F, which gave the chance for PANI nanofiber to enter these pores and channels and in turn, increase the surface area of PANI nanofiber, to whom the higher adsorption capacity belongs. S, SA, and PET waste were also explored as adsorbent for Cr(VI) and phosphate ions, it was found that there was a very low adsorption of these adsorbates onto the surfaces of S, SA, and PET, while pure PANI nanofiber alone exhibits more than 99% removal for Cr(VI). These experiments gave an indication that the process occurred on the PANI surfaces only.

It seems that the mechanism of Cr(VI) and phosphate ions’ sorption onto nanocomposites mostly occurred via anion exchange process. When the HCl doped PANI is treated with an aqueous solution of Cr(VI) or phosphate ( PO 4 - 3 ) ions in acidic media, the chloride ion (mobile dopant anion) in the polymer is readily exchanged for chromate or phosphate anions, so the removal of Cr(VI) or phosphate results. At pH ⩽ 2 the dichromate is converted to chromate HCrO 4 - ions as follows: Cr 2 O 4 - 2 + 2 H + 2 HCrO 4 - Then the nanocomposite surfaces can remove chromate anions as follows: PANI + Cl - ( polymer ) + HCrO 4 - ( solution ) PANI + HCrO 4 - ( polymer ) + Cl - ( solution ) Exchangeable anions Cl in the PANI exist only in the acid doped state, so undoped PANI does not adsorb Cr(VI) or phosphate ions, Fig. 1.

The phosphate uptake obviously increased with the decrease of pH. When the pH is low the positive charge on the surface of PANI is concentrated leading to static electricity force between positive PANI surfaces and negative phosphate ions, then the mechanism of phosphate ion removal may be due to electrostatic force besides interaction of ion-exchange (Long et al., 2011; Kanwal et al., 2012). At low pH the phosphate anions can be present in solution as HPO 4 - 2 or H 2 PO 4 - as follows: PO 4 - 3 + H + HPO 4 - 2 HPO 4 - 2 + H + H 2 PO 4 - The low removal percentage of phosphate ion H 2 PO 4 - 2 onto nanocomposites in comparison to chromate anion HCrO 4 - can be attributed to the difficulty in replacing monovalent anion Cl- for divalent anion H 2 PO 4 - 2 unless more doped PANI is required, as follows: PANI + Cl - ( polymer ) + HPO 4 - 2 ( solution ) ( PANI + ) 2 HPO 4 - 2 ( polymer ) + Cl - ( solution ) The effect of contact time and nanocomposite weight for Cr(VI) and phosphate adsorption were also investigated. All nanocomposites take about 90 min to reach equilibrium and concentration of 10 g/L for Cr(VI) adsorption, except PANISA, where the adsorption was very rapid, and takes less than 2 min and 2 g/L of adsorbent to attain equilibrium Table 2. This behavior is attributed to the large surface area of PANISA, due to, an increase in number of pores and channels in the structure of PANISA after treatment with acid, these pores and channels are clearly shown in Fig. 6F. The weight and time effect on the adsorption of phosphate ions are presented in Table 3. The effect of adsorbent weight was studied by varying the nanocomposite weight and keeping all the other experimental variables constant.

Table 2 Time and weight effect of nanocomposites for the adsorption of Cr(VI) at pH 2, 25 °C and shaking speed 140 rpm.
Nanocomposite Weight (g/L) Contact time (min) Initial conc. (mg/L) Final conc. (mg/L) R%
PANISA 4 2 20 0.138 99.31
PANIS 10 90 20 0.96 95.20
PANIPET 10 90 20 0.957 95.21
PANIFG 10 90 20 1.35 93.25
Table 3 Time and weight effect of nanocomposites for the adsorption of phosphate ions at pH 1, 25 °C and shaking speed 140 rpm.
Nanocomposite Weight (g/L) Contact time (min) Initial phosphate conc. (mg/L) Final phosphate conc. (mg/L) R%
PANIS 4 90 20 15.85 20.75
PANISA 4 90 20 12.03 39.85

3.3

3.3 Adsorption kinetics

In order to obtain further insight into the mechanism of the adsorption of Cr(VI) and phosphate onto nanocomposites, the experimental data were regressed against the Pseudo-first order model represented by the following linear equation (Long et al., 2011):

(3)
log ( q e - q t ) = log q e - K 1 2.303 t and Pseudo-second-order kinetic model (Ho and Mckay, 1999):
(4)
t q t = 1 k 2 q e 2 + 1 q e ( t )
where qe and qt are the adsorption capacity at equilibrium and time (t), respectively. k1 and k2 are the rate constants of the Pseudo-first-order and Pseudo-second-order kinetics, respectively. In the first-order kinetic model, log(qeqt) was plotted against time t. While the linear curves of the second-order kinetic model were obtained when t/qt was plotted against time, for the adsorption of Cr(VI) and phosphate onto nanocomposites Figs. 7 and 8. The results reveal that the second-order kinetic model well represents the experimental data for the adsorption of Cr(VI) onto PANIS, PANIFG and PANIPET, and phosphate onto PANIS and PANISA, this conclusion came from the good correlation coefficient obtained from second-order plot as well as the good match between the values of qe(cal) and qe(exp) Tables 4 and 5. In comparison between the adsorption of Cr(VI) onto PANIFG, PANIS and PANIPET, it was observed that the adsorption capacity of PANS was higher than that of PANIFG and PANIPET, Table 4, which was attributed to large surface area of PANS relative to other adsorbents. Table 4 also reveals that there was little effect of temperature on the equilibrium capacity of the adsorption of Cr(VI) onto PANIPET, PANIFG and PANIS surfaces, the kinetics of adsorption of Cr(VI) onto PANISA surface was not evaluated because the time required to reach the equilibrium was too low, about 2 min, therefore it is too difficult to follow-up. On the other hand, the kinetics of adsorption of phosphate onto PANISA and PANIS were evaluated, and found that the capacity at equilibrium of PANISA was much higher than that of PANIS Table 5, the higher surface area of PANISA was the main reason for such behavior, moreover, the capacity at equilibrium of PANISA and PANIS especially that of PANISA was decreased with increasing temperature which may be attributed to the weak interaction between adsorbent surface and adsorbate, due to larger size of divalent anion HPO 4 - 2 in comparison to the monovalent positive charge.
Second-order plot of adsorption of phosphate onto nanocomposites.
Figure 7
Second-order plot of adsorption of phosphate onto nanocomposites.
Second-order plot of adsorption of Cr(VI) onto nanocomposites.
Figure 8
Second-order plot of adsorption of Cr(VI) onto nanocomposites.
Table 4 Kinetic parameter of adsorption of Cr(VI) onto PANIS, PANIFG and PANIPET nanocomposites.
Nanocomposite Kinetic model Parameter 25 °C 35 °C 45 °C 55 °C
PANIFG First-order qeexp (mg/g) 3.13 3.14 3.16 3.17
k1 (min−1) 0.024 0.025 0.021 0.024
qecal (mg/g) 2.23 5.10 5.38 5.61
R2 0.9866 0.8416 0.8185 0.8472
Second-order k2(g mg−1 min−1) 0.18 0.43 0.43 0.47
qecal (mg/g) 3.15 3.15 3.17 3.17
R2 0.999 1.00 1.00 1.00
PANIPET First-order qeexp (mg/g) 3.02 3.02 3.1
k1 (min−1) 0.06 0.06 0.04
qecal (mg/g) 1.22 1.42 1.95
R2 0.9658 0.9629 0.8607
Second-order k2(g mg−1 min−1) 0.16 0.18 0.22
qecal (mg/g) 3.09 3.08 3.13
R2 0.9999 0.9999 0.9999
PANIS First-order qeexp (mg/g) 4.68 4.77 4.77 4.79
k1 (min−1) 0.03 0.05 0.06 0.04
qecal (mg/g) 1.07 1.47 1.68 1.11
R2 0.9123 0.9336 0.9706 0.9684
Second-order k2(g mg−1 min−1) 0.07 0.073 0.088 0.091
qecal (mg/g) 4.75 4.87 4.87 4.88
R2 0.9991 0.9994 0.9997 0.9997
Table 5 Kinetic parameter of adsorption of phosphate ions onto PANIS and PANISA nanocomposites.
Nanocomposite Kinetic model Parameter 25 °C 35 °C 45 °C 55 °C
PANIS First-order qeexp (mg/g) 4.92 4.90 4.85 4.77
k1 (min−1) 0.033 0.021 0.021 0.024
qecal (mg/g) 0.37 0.67 1.21 1.61
R2 0.9309 0.9630 0.9670 0.9239
Second-order k2(g mg−1 min−1) 0.261 0.146 0.550 0.450
qecal (mg/g) 4.94 4.95 4.90 4.86
R2 1.000 0.9999 0.9979 0.9981
PANISA First-order qeexp (mg/g) 7.47 7.33 6.85 5.52
k1 (min−1) 0.035 0.029 0.026 0.033
qecal (mg/g) 1.98 2.24 1.75 2.88
R2 0.9653 0.7394 0.9054 0.8997
Second-order k2(g mg−1 min−1) 0.047 0.036 0.044 0.025
qecal (mg/g) 7.61 7.41 6.93 5.74
R2 0.9995 0.9968 0.9984 0.9933

4

4 Conclusions

The results showed that PANISA was potential in removal of chromium and phosphate, due to, large surface area of PANISA. The pores and channels in the structure of natural silica were increased after treatment with HCl. Lower time and weight of PANISA nanocomposite are required to attain equilibrium. The mechanism of chromium and phosphate ions’ adsorption onto nanocomposites mostly occurred via electrostatic force besides the ion-exchange process. The lower efficiency of PANISA for phosphate removal, in comparison with Cr(VI) removal, is an indication of such mechanism, which was attributed to the charge difference between the exchangeable chloride anion Cl and divalent phosphate anion HPO 4 - 2 .

References

  1. , , . Adsorption and photodegradation of methylene blue by using PANI/TiO2 nanocomposite. J. Dispers. Sci. Tech.. 2012;33(3):380-386.
    [Google Scholar]
  2. , . Application of polyaniline and its composites for adsorption/recovery of chromium(VI) from aqueous solutions. Acta Chim. Slov.. 2006;53:88-94.
    [Google Scholar]
  3. , , . Removal of lead ion from aqueous solutions using sawdust coated by polyaniline. Eur. J. Chem.. 2006;3:49-59.
    [Google Scholar]
  4. , , . Removal of mercuric ion from aqueous solutions using sawdust coated by polyaniline. Eur. J. Chem.. 2006;3:35-43.
    [Google Scholar]
  5. , , , , . Adsorption of cationic dyes from aqueous solutions using polyaniline conducting polymers as novel adsorbent. J. Advan. Sci. Res.. 2011;2:27-34.
    [Google Scholar]
  6. , , . Structure properties of polyaniline protonated with camphorsulphonic acid. Synth. Met.. 1999;101:715-716.
    [Google Scholar]
  7. , , . X-ray diffraction study of doped polyaniline. J. Appl. Polym. Sci.. 1996;62:15-18.
    [Google Scholar]
  8. , , , , , , . Electrical conductivity of polyaniline/zeolite composites and synergetic interaction with CO. Mater. Sci. Eng.. 2005;B117:276-282.
    [Google Scholar]
  9. , , , , , , . Micelle-assisted synthesis of polyaniline magnetite nanorods by in situ self – assembly process. J. Coll. Interf. Sci.. 2008;320:341-345.
    [Google Scholar]
  10. , , , . Chemical vapour driven polyaniline sensors/actuators. Synth. Met.. 2003;135–136:809-810.
    [Google Scholar]
  11. , , , . Synthesis of polyaniline/graphite composites as a cathode of Zn-polyaniline rechargeable battery. J. Power Sour.. 2007;170:513-519.
    [Google Scholar]
  12. , , . Polyaniline nanofibers fabricated by electrochemical polymerization: a mechanistic study. Eur. Polym. J.. 2007;43:2292-2297.
    [Google Scholar]
  13. , , . The adsorption of lead(II) ions on peat. Water Res.. 1999;33:578-584.
    [Google Scholar]
  14. , . Synthesis and applications of conducting polymer polyaniline nanofibers. Pure Appl. Chem.. 2006;78:15-27.
    [Google Scholar]
  15. , , . A general chemical route to polyaniline nanofibers. J. Am. Chem. Soc.. 2004;126:851-855.
    [Google Scholar]
  16. , , , , . Nanostructured polyaniline sensors. Chem. Eur. J.. 2004;10:1314-1319.
    [Google Scholar]
  17. , , . Nanofiber formation in the chemical polymerization of aniline: a mechanistic study. Angew. Chem. Int. Ed.. 2004;43:5817-5821.
    [Google Scholar]
  18. , , , , . Batchwise removal of chromium (VI) by adsorption on novel synthesized polyaniline composites with various brans and isothermal modeling of equilibrium data. J. Chem. Soc. Pak.. 2012;34(5):1134-1139.
    [Google Scholar]
  19. , , , . Chromium(VI) adsorption from aqueous solution by Hevea brasilinesis sawdust activated carbon. J. Hazard. Mater.. 2005;124:192-199.
    [Google Scholar]
  20. , , , , . Removal of methylene blue dye by application of polyaniline nanocomposite from aqueous solution. J. Phys. Theor. Chem.. 2009;6(1):50-56.
    [Google Scholar]
  21. , , , , . Preparation of polyaniline nanoparticles in micellar solutions as polymerization medium. Langmuir. 2000;16:5841-5845.
    [Google Scholar]
  22. , , , . Polyaniline nanofibers: a unique polymer nanostructure for versatile applications. Acc. Chem. Res.. 2009;42:135-145.
    [Google Scholar]
  23. , , . Processable stabilizer-free polyaniline nanofiber aqueous colloids. Chem. Commun.. 2005;26:3286-3288.
    [Google Scholar]
  24. , , , , , , , , , . Removal of phosphate from aqueous solution by magnetic Fe–Zr binary oxide. Chem. Eng. J.. 2011;171:448-455.
    [Google Scholar]
  25. , , . Relations between the structure and electric conductivity of polyaniline protonated with camphorsulphonic acid. Macromolecules. 2000;33:425-429.
    [Google Scholar]
  26. , , , , . Polyaniline nanofiber gas sensors: examination of response mechanisms. Nano Letters. 2004;4:491-496.
    [Google Scholar]
  27. , , , , , , , , . Electrochemically fabricated polyaniline nanoframework electrode junctions that function as resistive sensors. Nano Letters. 2004;4:1693-1697.
    [Google Scholar]
  28. , , , , , , . Stable organic-inorganic hybrid of polyaniline/α-zirconium phosphate for efficient removal of organic pollutants in water environment. ACS Appl. Mater. Interf.. 2012;4(5):2686-2692.
    [Google Scholar]
  29. , , . Transparent conductive films based on polyaniline nanofibers. J. Mater. Sci. Eng. B. 2007;138:95-100.
    [Google Scholar]
  30. , , , , . Batch adsorption and mechanism of Cr(VI) removal by polyaniline/humic acid nanocomposite. J. Environ. Eng.. 2011;137(12):1158-1164.
    [Google Scholar]
  31. , , , , . Kapok fiber oriented-polyaniline nanofiber for efficient Cr(VI) removal. Chem. Eng. J.. 2012;191:154-161.
    [Google Scholar]
Show Sections