s-1
Supporting Information
Iron-Carbon Hybrid Magnetic Nanosheets for Adsorption-Removal of Organic Dyes and 4- Nitrophenol from Aqueous Solution
Sai Rashmi Manippady,
†Ashish Singh,
#‡Bhavya Moodalegowda Basavaraja,
#†Akshaya Kumar Samal,
†Sachchidanand Srivastava,
||Manav Saxena*
†AUTHOR ADDRESS
†
Centre for Nano and Material Sciences, Jain University, Ramanagaram, Bangalore-562112, Karnataka, India.
‡
Department of Chemistry, Indian Institute of Technology Kanpur, Kanpur-208016, Uttar Pradesh, India
||
Solid State and Structural Chemistry Unit, Indian Institute of Science, Bangalore-560012, Karnataka, India.
#
These authors (AS and BMB) contributed equally.
Corresponding author: [email protected], [email protected] (MS)
S. No. Table of contents Page no.
Table S1 Different dye removal techniques s-3
Figure S1 EDS analysis of (a) CF-0, (b) CF-2. s-4
Figure S2 X-ray photoelectron spectroscopy (XPS) survey spectra of CF-0 and CF-2 s-5
Table S2 Magnetic properties of CF-0 and CF-2. s-6
Table S3 pH dependent Zeta potential study s-7
Figure S3 Zeta potential measurement of CF-2 (a) pH 2, (b) pH 3, (c) pH 5, (d) pH 7, (e)
pH 8, (f) pH 10, (g) pH of zero point charge s-8
Figure S4
(a) Dye adsorption efficiency of CF-0 and CF-2 at t=24 min for 50 mgL-1 MB (pH 8) and CR (pH 2), (b) Dosage study for CF-2 at t=24 min with 50 mgL-1 MB,
s-9
Figure S5 UV-Vis absorbance spectra for the adsorption of (a) MB by CF-2 at pH: 8 (b)
CR by CF-2 at pH: 2 and (c) CR by CF-2 pH: 7 s-10
Figure S6
(a) UV-Vis absorbance spectra for the adsorption of MB by CF-0, (b) Percent removal, (c) Effect of contact time on adsorption capacity of MB (d) Pseudo- first-order (e) Pseudo-second-order kinetics (f) Intraparticle diffusion model of MB
s-11
Figure S7
(a) Effect of pH on MB dye adsorption, (b) Effect of contact time on CF-2 adsorption capacity with 50 mg L-1 MB, (c) Pseudo-first-order (d) ) Freundlich isotherm for MB.
s-12
Figure S8
(a) UV-Vis absorbance spectra for the adsorption of CR by CF-0, (b) Percent removal, (c) Effect of contact time on adsorption capacity of CR (d) Pseudo- first-order (e) Pseudo-second-order kinetics (f) Intraparticle diffusion model of CR
s-13
Figure S9
(a) Effect of pH on CR dye adsorption, (b) Effect of contact time on CF-2 adsorption capacity with 50 mg L-1 CR, (c) Pseudo-first-order (d) ) Langmuir isotherm for CR.
s-14 Figure S10 Comparative intraparticle diffusion of MB and CR. s-15 Figure S11 Optical images of (a) Recovered adsorbent. Recovery process of (b) MB (c)
CR and (d) N2 adsorption-desorption study of CF-2 after MB adsorption. s-16 Figure S12 Comparative UV-Vis spectroscopic study of standard and recovered (a) MB
and (b) CR using CF-2. s-17
Figure S13
(a) Collected Rhodamine based textile dye “suti gulabi” after centrifuge (b) UV-Visible spectra for the textile waste water before and after adsorption (inset: photograph of dye before and after adsorption).
s-18 Figure S14 (a) Effect of pH on hair dye adsorption, (b) UV-Vis absorbance spectra of hair
dye waste. s-19
Figure S15 (a) UV-Vis absorbance spectra for 50ppm 4-NP (b) Pseudo-first-order (c) Freundlich isotherm model and (d) Recovered 4-NP with methanol s-20 Figure S16 FESEM image of CF-2 (a) as synthesized (b) recovered after 5th cycle (c)
PXRD of as synthesized and reused CF-2. s-21
Table S4 Comparative study of the adsorption parameters & performance of other s-22-
s-3
Table S1: Different dye removal techniques.
Dye removal technique Ref.
Adsorption
1Photocatalytic degradation
2Membrane filtration
3Osmosis
4Coagulation and flocculation
5Ion exchange
6Irradiation
7Figure. S1. EDS analysis of (a) CF-0, (b) CF-2.
(a)
(b)
s-5
FigureS2. X-ray photoelectron spectroscopy (XPS)-survey spectra of CF-0 and CF-2
Table S2. Magnetic properties of CF-0 and CF-2.
Adsorbent M
s(emu g
-1) M
r(emu g
-1) H
c(Oe) M
r/M
sCF-0 0.01 0.0002 195 0.02
CF-2 19.52 3.65 423 0.19
s-7
Table S3. pH dependent mean zeta potential of CF-2
Sample pH Mean zeta potential (mV)
2 25.3
3 18.7
5 -8.4
7 -22.4
8 -24.4
CF-2
10 -32.5
FigureS3. Zeta potential measurement of CF-2 (a) pH 2, (b) pH 3, (c) pH 5, (d) pH 7, (e) pH 8,
(f) pH 10 (g) pH of zero-point charge
s-9
Figure S4. (a) Dye adsorption efficiency of CF-0 and CF-2 at t=24 min for 50 mgL
-1MB (pH 8)
and CR (pH 2), (b) Dosage study for CF-2 at t=24 min with 50 mgL
-1MB,
Figure S5. UV-Vis absorbance spectra for the adsorption of (a) MB at pH: 8 (b) CR at pH: 2 and
(c) pH: 7 by CF-2.
s-11
Figure S6. (a) UV-Vis absorbance spectra for the adsorption of MB by CF-0, (b) percent
removal, (c) effect of contact time on adsorption capacity of MB on control (d) Pseudo-first-
order (R
2: 0.601) (e) pseudo-second-order kinetics (R
2: 0.999) (f) Intraparticle diffusion model
of MB on control (R
2: 0.625, R
2: 0.392).
Figure S7.
(a) Effect of pH on MB dye adsorption, (b) Effect of contact time on CF-2 adsorption capacity with 50 mg L-1 MB, (c) Pseudo-first-order (d) Freundlich isotherm for MB.s-13
Figure S8. (a) UV-Vis absorbance spectra for the adsorption of CR by CF-0, (b) percent removal, (c) effect of contact time on adsorption capacity of CR on control (d) Pseudo-first-order (R
2:0.917) (e) pseudo-second-order kinetics (R
2: 0.978) (f) Intraparticle diffusion model of CR on control (R
2:0.928, R
2:0.719), contact time:32 min, adsorbent dosage: 6 mg, dye concentration:
50 mg L
-1and pH: 2.
Figure S9.
(a) Effect of pH on CR dye adsorption, (b) Effect of contact time on CF-2 adsorption capacity with 50 mg L-1 CR, (c) Pseudo-first-order (d) Langmuir isotherm for CR.s-15
Figure S10.
Comparative intraparticle diffusion of MB and CR.Figure S11. Optical images of (a) Recovered adsorbent. Recovery process of (b) MB (c) CR and
(d) N
2adsorption-desorption study of CF-2 after MB adsorption.
s-17
Figure S12. Comparative UV-Vis spectroscopic study of standard and recovered (a) MB and (b)
CR using CF-2.
Figure S13. (a) Collected Rhodamine based textile dye “suti gulabi” after centrifuge (b) UV- Visible spectra for the textile waste water before and after adsorption (inset: photograph of dye before and after adsorption).
Textile waste water: The waste dye effluent of textile coloring industry locally known as “suti
gulabi” a rhodamine-based dye was collected from Kanpur, Uttar Pradesh, India. The collected
effluent was centrifuged to remove any dispersed fibers and supernatant was collected for the
study (Figure S12a). Initial absorbance of the effluent was measured using UV-Vis
spectrophotometer. The adsorption study of effluent with CF-2 was performed at normal lab
conditions at STP. As collected effluent showed absorbance maximum at 540 nm and pink in
color. Upon addition of CF-2, the pink color disappeared and the absorbance intensity decreased
drastically (inset, Figure S12b). The absorbance study suggested that CF-2 could adsorb effluent
upto 90.2% in just 10 sec (Figure S12b) and the used adsorbent could be easily recovered upon
s-19
Figure S14. (a) Effect of pH on hair dye adsorption, (b) UV-Vis absorbance spectra of hair dye
waste.
Figure S15. (a) UV-Vis absorbance spectra for 50 ppm 4-NP (without AcOH) (b) Pseudo-first-
order (c) Freundlich isotherm model and (d) Normalized UV-Vis spectra for standard and
recovered 4-NP in methanol.
s-21
Figure S16: FESEM image of CF-2 (a) as synthesized (b) recovered after 5
thcycle (c) PXRD of
as synthesized and reused CF-2.
Table S4. Comparative study of the adsorption parameters & performance of other adsorbents.
Adsorbent
Adsorption capacity (mg g
-1) Adsorbent wt. per dye volume (mg/mL) Time (min) Removal %
Ref.
Methylene Blue dye
CNTs/Fe@C 132.6 1.00 80 ~100 8
PB@PVP/rGO 44.7 1.00 10 99.6 9
NF/CF-BYs 141.8 3.33 120 >90 10
Fe
3O
4@C 52.6 1.00 2160 97.8 11
magnetite/silica/pectinNPs 197.2 2.00 150 82 12
Fe
3O
4@PPy/RGO 270.3 0.33 60 ~55 13
CoFe
2O
4/rGO composites 93.5 0.20 30 98.6 14
Fe
3O
4/montmorillonite nanocomposite
106.4 2.50 25 99.4 15
C/Fe
3C/γ-Fe2O
3185.2 0.40 24 99.9 This work
Congo Red Dye
α-Fe2
O
3nanocrystals 161 0.60 180 97 16
CoFe
2O
4/rGO composite 104.5 0.25 30 86.4 14
Fe(OH)
3@cellulose PHFs 689.6 - 6000 >99 17
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pTSA-Pani@GO-CNT 66.7 1.00 300 96.0 20
Aerogels from corn stalks 549 - 60 ~89 21
C/Fe
3C/γ-Fe2O
3531.9 0.40 24 96.6 This work
4-Nitrophenol
Fe
3O
4-graphene-oxysilane 142 0.5 5 ~75 22
Acid activated carbon 234 2.4 2880 68.4 23
Amine-Al-MOF 192.6 6.0 300 - 24
C/Fe
3C/γ-Fe2O
3109.1 1.0 24 99.5 This work
Table S5. Kinetic parameters of pseudo-first order and pseudo-second order and intraparticle diffusion model calculated using linear fits for the adsorption of MB and CR on CF-2. Isothermal parameters of the Langmuir and Freundlich model calculated using linear fits for the adsorption of MB and CR on CF-2.
Kinetic Study
Pseudo-first order Pseudo-second order
q
e(exp)K
1q
e(cal)K
2q
e(cal)Dye mg.g
-1min
-1R
2mg.g
-1g/mg/min R
2mg.g
-1MB 127.34 0.88 0.943 30338.9 0.0245 0.999 142.85
CR 116.02 0.396 0.799 39174.2 0.0079 0.991 115.60
4-NP 49.78 0.638 0.883 386.2 0.206 0.999 49.90
Intraparticle Diffusion
K
p1R
2C
1K
p2R
2C
2Dye mg.g min
-1mg.g
-1mg.g min
-1mg.g
-1MB 4.028 0.872 109.38 - - -
CR 9.902 0.937 66.18 - - -
4-NP 0718 0.998 46.81 0.066 0.998 49.422
Isotherm study
Langmuir isotherm Freundlich isotherm
Dye K
L(L/mg)
q
max(mg/g) R
LR
2K
F(mg/g) n R
2MB 0.108 185.2 0.156-0.035 0.950 0.698 8.465 0.704
CR 0.057 531.9 0.258-0.065 0.916 0.544 1.925 0.993
4-NP 0.407 109.1 0.046-0.013 0.985 0.581 7.606 0.977
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