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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2022, Vol. 16 Issue (5) : 57    https://doi.org/10.1007/s11783-021-1491-6
RESEARCH ARTICLE
Concurrent adsorption and reduction of chromium(VI) to chromium(III) using nitrogen-doped porous carbon adsorbent derived from loofah sponge
Feng Chen1, Shihao Guo1, Yihao Wang1, Lulu Ma1, Bing Li1, Zhimin Song1(), Lei Huang2,3(), Wen Zhang4
1. School of Environmental and Biological Engineering, Henan University of Engineering, Zhengzhou 451191, China
2. School of Environmental Science and Engineering, Guangzhou University, Guangzhou 510006, China
3. Guangzhou University-Linköping University Research Center on Urban Sustainable Development, Guangzhou University, Guangzhou 510006, China
4. John A. Reif, Jr. Department of Civil and Environmental Engineering, New Jersey Institute of Technology, Newark, NJ 07102, USA
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Abstract

• A high-efficiency N-doped porous carbon adsorbent for Cr(VI) was synthesized.

• The maximum adsorption capacity of Cr(VI) reached up to 285.71 mg/g at 318K.

• The potential mechanism for Cr(VI) adsorption by NHPC was put forward.

• DFT analyzed the adsorption energy and interaction between NHPC and Cr(VI).

To develop highly effective adsorbents for chromium removal, a nitrogen-doped biomass-derived carbon (NHPC) was synthesized via direct carbonation of loofah sponge followed by alkali activation and doping modification. NHPC possessed a hierarchical micro-/mesoporous lamellar structure with nitrogen-containing functional groups (1.33 at%), specific surface area (1792.47 m2/g), and pore volume (1.18 cm3/g). NHPC exhibited a higher Cr(VI) adsorption affinity than the HPC (without nitrogen doping) or the pristine loofah sponge carbon (LSC) did. The influence of process parameters, including pH, dosage, time, temperature, and Cr(VI) concentration, on Cr(VI) adsorption by NHPC were evaluated. The Cr(VI) adsorption kinetics matched with the pseudo-second-order model (R2≥0.9983). The Cr(VI) adsorption isotherm was fitted with the Langmuir isotherm model, which indicated the maximum Cr(VI) adsorption capacities: 227.27, 238.10, and 285.71 mg/g at 298K, 308K, and 318K, respectively. The model analysis also indicated that adsorption of Cr(VI) on NHPC was a spontaneous, endothermal, and entropy-increasing process. The Cr(VI) adsorption process potentially involved mixed reductive and adsorbed mechanism. Furthermore, computational chemistry calculations revealed that the adsorption energy between NHPC and Cr(VI) (−0.84 eV) was lower than that of HPC (−0.51 eV), suggesting that nitrogen doping could greatly enhance the interaction between NHPC and Cr(VI).

Keywords Chromium(VI)      Nitrogen-doped porous carbon      Adsorption      Reduction      Loofah sponge     
Corresponding Author(s): Zhimin Song,Lei Huang   
Issue Date: 18 October 2021
 Cite this article:   
Feng Chen,Shihao Guo,Yihao Wang, et al. Concurrent adsorption and reduction of chromium(VI) to chromium(III) using nitrogen-doped porous carbon adsorbent derived from loofah sponge[J]. Front. Environ. Sci. Eng., 2022, 16(5): 57.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-021-1491-6
https://academic.hep.com.cn/fese/EN/Y2022/V16/I5/57
Fig.1  SEM images and elemental maps of NHPC (a) and NHPC after Cr adsorption (b). Elemental maps of carbon (red), oxygen (yellow), nitrogen (green), and chromium (pink).
Fig.2  The different characteristics of LSC, HPC, and NHPC (a) XRD, (b) Raman spectra, (c, d) Brunauer-Emmett-Teller.
Parameters Samples
LSC HPC NHPC
SBET (m2/g) 967.16 1684.34 1792.47
Smicro (m2/g) 883.48 900.31 1342.05
Sext (m2/g) 83.68 784.03 450.42
Vt (cm3/g) 0.52 1.43 1.18
Vmicro (cm3/g) 0.40 0.47 0.66
Vext (cm3/g) 0.12 0.96 0.52
Dave (nm) 2.14 3.40 2.62
Tab.1  The textural parameters (mean values) of LSC, HPC, and NHPC
Fig.3  (a) pH-Cr(VI) removal efficiency and the species of Cr, (b) influence of dosage, (c, d) kinetics and isotherms.
Adsorbent Initial concentration (mg/L) Temperature (K) qm
(mg/g)
References
Waste peanut hull derived N-doped spherical carbons 25–250 298 181.82 Wei and Cai, 2020
Cassava sludge-based activated carbon 2–10 298 9.84 Guo et al., 2021
N/P co-doped biochars from (NH4)3PO4-pretreated coffee shells 50–300 303 223.5 Li et al., 2020a
Activated carbon obtained from teakwood sawdust 5–225 298 72.46 Ramirez et al., 2020
H3PO4-treated biochar 60–1050 298 116.28 Zhao et al., 2017
Nitrogen-containing activated carbon preparation from bamboo processing residues 50–280 303 185.2 Shang et al., 2014
Nitrogen-enriched activated carbon from waste medium density fiberboard 50–280 303 250 Wu et al., 2014
Nitrogen-doped hierarchical porous biomass-derived carbon 5–90 298 227.27 This work
318 285.71 This work
Tab.2  Summary of different adsorbents for Cr(VI) adsorption that published before
Fig.4  The X-ray photoelectron spectroscopy: (a) Cr 2p, (b) C 1s, (c) N 1s, and (d) O 1s spectra of NHPC and NHPC-Cr.
Fig.5  The density functional calculation of HPCHCrO4 (a, c) and NHPCHCrO4 (b, d).
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