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Journal ArticleDOI

Adsorption and desorption of cationic malachite green dye on cellulose nanofibril aerogels.

01 Oct 2017-Carbohydrate Polymers (Elsevier)-Vol. 173, pp 286-294
TL;DR: Ultra-light aerogels have been assembled from cellulose nanofibrils into hierarchically macroporous (several hundred μm) honeycomb cellular structure surrounded with mesoporous (8-60nm) thin walls, demonstrating facile recovery of both dye and aerogel as well as the robust capability of thisaerogel for repetitive applications.
About: This article is published in Carbohydrate Polymers.The article was published on 2017-10-01 and is currently open access. It has received 208 citations till now. The article focuses on the topics: Adsorption & Langmuir adsorption model.

Summary (3 min read)

1. Introduction

  • To further increase the specific surface, inter-CNF hydrogen bondings were reduced by solvent exchange the hydrogels with tert-butanol prior to freeze-drying into aerogels.
  • The adsorption mechanism, kinetics and capacity of cationic malachite green dyes on these cellulose nanofibril aerogels as well as their desorption were investigated.

2.1. Materials

  • Pure cellulose was isolated from rice straw (Calrose variety) following a previously reported process to a 36% yield (Lu & Hsieh, 2012) .
  • Cellulose nanofibrils (CNFs) were derived from pure rice straw cellulose employing 5 mmol NaClO per gram of cellulose and mechanical blending at 37,000 rpm for 30 min (Jiang et al., 2013) .
  • Malachite green (Fisher Scientific), sodium chloride (NaCl, >99%, Fisher Scientific), and tert-butanol (certified, Fisher Scientific) were used as received without further purification.
  • All water used was purified and deionized by Milli-Q plus water purification system (Millipore Corporate, Billerica, MA).

2.3. Cellulose aerogel characterization

  • CNF aerogel was cut in the transverse direction, coated with gold and visualized by a field emission scanning electron microscope (FE-SEM) (XL 30-SFEG, FEI/Philips, USA) at a 5-mm working distance and 5-kV accelerating voltage.
  • The specific surface was determined by the Brunauer-Emmett-Teller (BET) method from linear region of the isotherms in the 0.06-0.20 relative P/P 0 pressure range.
  • Pore size distributions were derived from desorption branch of the isotherms by the Barrett-Joyner-Halenda (BJH) method.
  • The total pore volumes were estimated from the amount adsorbed at a relative pressure of P/P 0 = 0.98.
  • CNF aerogels before and after dye adsorption (MG concentration of 100 mg/L, dried in air) were pressed into KBr pellets (1:100, w/w).

2.4. Adsorption of malachite green

  • For MG removal from dilute solution, the adsorption was carried out at 10 mg/L MG concentration and 1:5 aerogel-to-MG v/w ratio for 2 h.
  • After adsorption, a piece of fresh aerogel was put into the residual solution for three repeated times until the solution becomes colorless.

3.2. Adsorption kinetics

  • While both kinetic models of the adsorption data yielded correlation coefficient R 2 values over 0.97 (Table 1 ), pseudo-second order kinetic model was clearly a better fit with all R 2 values above 0.9943, showing linearity in the t/q t versus t plots (Fig. 2d ).
  • This indicates that the overall rate of the MG adsorption onto CNF aerogels is controlled by chemisorption.

3.3. Adsorption mechanism

  • The intra-particle diffusion rate constant k i and boundary layer thickness or resistance constant C values were calculated from the second intra-particle diffusion region using Eq. ( 8) to yield R 2 ranging from 0.9835 to 0.9961, very high at all concentrations (Fig. 3b ).
  • The boundary layer thickness constant C also increased with increasing MG concentrations, indicating greater adsorption via the initial electrostatic interaction at higher MG concentrations.

3.5. Effectiveness of CNF aerogel in complete removal of malachite green

  • The effectiveness of CNF aerogel to remove MG dye was first evaluated using varying aerogel quantities at a constant 100 mg/L MG concentration.
  • Therefore, repetitive adsorption using fresh aerogels is effective in completely removing MG at low concentrations.

3.6. MG-CNF aerogel interactions

  • As sodium carboxylate dissociates, the negatively charged carboxylate anions on CNF surfaces can electrostatically attract the MG iminium cations (Fig. 6c ).
  • The FTIR spectra of MG adsorbed CNF aerogel showed several peaks in the 800-400 cm −1 fingerprint region, consistent of the mono-substituted and para-disubstituted benzene rings in MG and confirming its presence in the aerogel.
  • The sodium carboxylate carbonyl peak at 1618 cm −1 became smaller which could be due to the interaction between the carboxylate and iminium groups, whereas the carboxylic acid peak at 1720 cm −1 remained essentially unchanged, suggesting that the carboxylic acid did not participate in the adsorption.
  • Therefore, FTIR spectra further confirmed electrostatic interactions to be predominantly responsible for MG dye adsorption onto CNF aerogel.
  • The maximum adsorption of 212.7 mg g −1 MG/aerogel corresponds to 0.59 mmol/g MG/aerogel or approximately 46% of the CNF surface carboxyls were involved in binding MG.

3.7. Desorption of malachite green from CNF aerogel

  • MG dye desorption from aerogels at varied NaCl concentrations also fitted to pseudo-second order kinetic well, with all R 2 above Fig. 7 .
  • Desorption of malachite green from CNF aerogel at varied salt concentrations, insets are pictures of aerogels after desorption (a); fitting of pseudo-second-order desorption kinetics (b); Pseudo second order kinetics fitting parameters for dye desorption from CNF aerogels (c). 0.9958 (Fig. 7b & c ).
  • The remaining less than 10% of residual dyes could be removed using a fresh NaCl solution.
  • The substantial and fast desorption process indicates that the aerogel could be facilely regenerated for repeated dye removal applications.

4. Conclusions

  • Ultra-lightweight aerogels have been fabricated from TEMPO oxidized cellulose nanofibrils (CNFs) via a three-step freezingthawing induced hydrogel formation, tert-butanol exchange and freeze-drying to a honeycomb cellular structure consisting of a few hundred m wide irregularly shaped open cells surrounded by mesoporous (8-60 nm) thin walls of self-assembled CNFs.
  • This unique hierarchical macro-and meso-porous structure coupled with high specific surface (193 m 2 /g) and surface carboxyl (1.29 mmol/g) has shown to be highly effective in removing cationic dye via electrostatic interactions between the CNF surface anionic carboxylate groups and MG iminium groups.
  • With increasing initial dye concentrations from 10 to 200 mg/L, the adsorption kinetics of MG on CNF aerogels showed a pseudosecond-order adsorption model with the initial adsorption rate increasing from 2.3 to 59.8 mg g −1 min −1 and the equilibrium adsorption capacity increasing from 53.0 to 203.7 mg g −1.
  • The excellent wet resiliency and fast release of the adsorbed dye could be achieved by increasing ionic strength to recover the aerogel for repetitive use.

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Citations
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TL;DR: Owing to its demonstrated properties such as 3D interconnected porous structure, lightweight, large specific surface area, superparamagnetic behavior at room temperature, excellent adsorbent efficiency (93% removal) and also its simple and eco-friendly synthesis process, MBCNF/GOPA could be considered a promising candidate for removing cationic dye pollutants from aqueous solution.

212 citations

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TL;DR: In this paper, the adsorption performance of pre-composed poly(methyl methacrylate)/graphene oxide-Fe3O4 (PMMA/GO-Fe 3O4) nanocomposite for removing malachite green (MG) dye from aqueous solution was investigated.
Abstract: The adsorption performances of as prepared poly(methyl methacrylate)/graphene oxide-Fe3O4 (PMMA/GO-Fe3O4) and poly (methyl methacrylate)/graphene oxide (PMMA/GO) nanocomposite as adsorbents were investigated for malachite green (MG) dye removal. For MG dye adsorption on PMMA/GO and PMMA/GO-Fe3O4 nanocomposite, 35 min was selected as the best contact time because there was no main change after 35 min. Optimum adsorption of the dye by both adsorbents occurred at 298 K. The calculated values of the entropy (ΔS°), enthalpy (ΔH°) and Gibbs energy (ΔG°) indicated that the adsorption process was exothermic in nature. The results indicated that PMMA/GO and PMMA/GO-Fe3O4 were good adsorbents for removing MG dye from aqueous solution and were good construed with the pseudo-second-order type (I) due to the law value for chi-square (X2) and high value of the correlation coefficients.

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TL;DR: It could be concluded that CuFe2O4/DC is a cost-effective and promising adsorbent for an efficient and rapid removal of Pb(II) and MG from both unary and binary systems.

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TL;DR: This contribution introduces the application of nanocellulose-based lightweight porous materials in the fields of adsorption, biomedicine, energy storage, thermal insulation and sound absorption, flame retardancy and catalysis.

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TL;DR: The interaction and main factor and optimum conditions of the under study process were determined from response surface plots based on desirability function and the maximum CR adsorption were achieved at pH of 4, 15 mg L-1 of CR, 0.017 g of Au-Fe3O4-AC and 5 min sonication which owing to 99.49% removal efficiency is highly recommended for future CR removal from different matrixes.

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References
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TL;DR: In this article, the absorption index at the wave length of the band maximum was found to be proportional to the total concentration of metal at shorter wave lengths, however, deviations were observed, the absorption increasing more rapidly with concentration than Beers' law would demand.
Abstract: solutions investigated, the absorption index diminishing approximately 1% for a rise in temperature of one degree. 6. In liquid ammonia rough measurements of concentration showed the absorption index to be proportional to the total concentration of metal. 7. In methylamine the absorption index, at the wave length of the band maximum is also proportional to the total concentration of metal. At shorter wave lengths, however, deviations were observed, the absorption increasing more rapidly with concentration than Beers’ law would demand. The ratio of the absorption index a t 650pp to that a t 53opp increases not only with increasing concentration of the metal but also with increasing concentration of the reaction product of the metal with methylamine, and probably also with increasing temperature. 8. These observations can be accounted for by the following hypotheses: The color in all cases is due to electrons combined with the solvent. In ammonia the dissociation of the metal into electrons is nearly complete, and the concentration of electrons uncombine4 with solvent is negligible compared with that of the solvated electrons. In other words, the solvation of the electrons is nearly complete. In methylamine, on the other hand, the concentration of un-ionized metal is no longer negligible and is responsible for the increased absorption a t the shorter wave lengths. The solvation of the electrons in methylamine is incomplete and diminishes as the temperature is increased.

18,573 citations


"Adsorption and desorption of cation..." refers background in this paper

  • ...The Langmuir adsorption isotherm represents monolayer adsorption onto a finite number of homogeneous sites and is described as (Langmuir, 1918): qe = qmax × KL × Ce1 + KL × Ce (9) where qe is the adsorbed MG at equilibrium (mg/g), q max is the adsorption capacity (mg/g), KL is the equilibrium…...

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TL;DR: In this paper, a literature review of the use of sorbents and biosorbents to treat polluted aqueous effluents containing dyes:organics or metal ions has been conducted.

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  • ...The Ho’s pseudo-second-order model was expressed as (Ho & McKay, 1999): qt = q 2 e × k2 × t 1 + qe × k2 × t (5) where qt and qe are the amount of MG adsorbed at time t and equilibrium (mg/g), k1 is the pseudo-first-order rate constant (min−1) and k2 is the pseudo-second-order rate constant (g mg−1…...

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TL;DR: In this paper, it was shown that the rate of adsorption of persistent organic compounds on granular carbon is quite low and the rate is partially a function of the pore size distribution of the adsorbent, of the molecular size and configuration of the solute, and of the relative electrokinetic properties of adsorbate and adsorbents.
Abstract: Laboratory investigations show that rates of adsorption of persistent organic compounds on granular carbon are quite low. Intraparticle diffusion of solute appears to control the rate of uptake, thus the rate is partially a function of the pore size distribution of the adsorbent, of the molecular size and configuration of the solute, and of the relative electrokinetic properties of adsorbate and adsorbent. Systemic factors such as temperature and pH will influence the rates of adsorption; rates increase with increasing temperature and decrease with increasing pH. The effect of initial concentration of solute is of considerable significance, the rate of uptake being a linear function of the square-root of concentration within the range of experimentation. Relative reaction rates also vary reciprocally with the square of the diameter of individual carbon particle for a given weight of carbon. Based on the findings of the research, fluidized-bed operation is suggested as an efficient means of using adsorption for treatment of waters and waste waters.

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  • ...As the slowest intra-particle diffusion being usually the ate-determining step, the Weber’s intra-particle diffusion model as applied (Weber & Morris, 1963): t = ki × t 1 2 + C (8) here qt is the MG quantity adsorbed at time t, ki is the intraarticle diffusion rate constant (mg g−1 min−1/2), and C…...

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TL;DR: From a comprehensive literature review, it was found that some LCAs, in addition to having wide availability, have fast kinetics and appreciable adsorption capacities too.

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Frequently Asked Questions (1)
Q1. What contributions have the authors mentioned in the paper "Adsorption and desorption of cationic malachite green dye on cellulose nanofibril aerogels" ?

The rapid MG adsorption was driven by electrostatic interactions and followed a pseudosecond-order adsorption kinetic and monolayer Langmuir adsorption isotherm.