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Zeta potential of magnetic biochar as a function of pH

Zeta potential of magnetic biochar as a function of pH

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In this study, the use of magnetic biochar particles recovered from biorefinery by-products (humins) for adsorption of hydrophilic organic pollutants was investigated. The biochar was prepared by thermal treatment of crude humins followed by a grinding step after which a magnetic iron oxide was co-precipitated on the biochar surface. The resulting...

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... The SEM images of Fe 3 O 4 /BC (Fig. 2c-d) low pressure, revealing the high microporosity in Fig. 3a. The hysteresis loop appeared when the relative pressure of BC was greater than 0.2, which was mainly caused by the mixed presence of micropores and mesopores [30]. Therefore, it could be concluded that BC was a graded porous material with micropores and mesopores. ...
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... For example, chemical harshness can come in the form of corrosive wastewaters (Shokri & Fard, 2022) or highly acidic wastewaters (Meng et al., 2020). Physical harshness can be encountered in the form of strong hydrodynamic forces acting on the adsorbent's structure (Lomenech et al., 2021;Mudhoo, Patel, Mohan, Pittman, & Sillanp€ a€ a, 2021). Such harsh conditions may thus induce permanent structural damage (e.g. ...
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... The adsorption capacity of P-H-0.5 tends to be stable when pH > 5, while P-2-H-2 still slightly increases, indicating that the two-step sample is more acidic and more sensitive to pH [14,53]. The surfaces of both samples are negatively charged when pH > pH PZC (insets), whereas in the relatively acidic (pH < pH PZC ) system, MB molecules mainly undergo protonation [54]. Thereafter, with increasing pH, deprotonation dominates and the proportion of cation in the dye molecule gradually rises. ...
... Both the Langmuir and Freundlich isotherm models match with the sorption data, yet the former fit is obviously better (Figure 11b,d, and Table 3). This means the adsorption by the two samples is relatively uniform and monolayer [54]. The calculated RL values (Supplementary Material) range from 0.00034-0.001 ...
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... Formerly, the pristine biochar is prepared and undergoes co-precipitation of magnetic particles onto the biochar matrix. Lomenech et al. (2021) prepared humin-derived biochar by heating it at 250°C for one hour and then its magnetic composite was formed by dissolving it in FeCl 3 and FeSO 4 solutions. The magnetic biochar is suspended in NaOH solution for the precipitation of iron oxide nanoparticles on its surface. ...
Chapter
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... Formerly, the pristine biochar is prepared and undergoes co-precipitation of magnetic particles onto the biochar matrix. Lomenech et al. (2021) prepared humin-derived biochar by heating it at 250°C for one hour and then its magnetic composite was formed by dissolving it in FeCl 3 and FeSO 4 solutions. The magnetic biochar is suspended in NaOH solution for the precipitation of iron oxide nanoparticles on its surface. ...
Chapter
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... Formerly, the pristine biochar is prepared and undergoes co-precipitation of magnetic particles onto the biochar matrix. Lomenech et al. (2021) prepared humin-derived biochar by heating it at 250°C for one hour and then its magnetic composite was formed by dissolving it in FeCl 3 and FeSO 4 solutions. The magnetic biochar is suspended in NaOH solution for the precipitation of iron oxide nanoparticles on its surface. ...
Chapter
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... As presented in Fig. 3B, the surface of the biochar is covered with iron oxide microparticles, among which spherically shaped ones predominate (Zhang et al., 2016). The iron oxide nanoparticles are not distributed homogeneously on the biochar surface, but rather form islands, which is common for hybrid biochar/iron oxide materials (Lomenech et al., 2021). ...
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Raspberry stalks-derived biochar (BC), magnetic biochar-iron oxide composite (BC–Fe) and its derivative modified with urea (BC–Fe–U) were synthesized, characterized and tested as(V) and Cr(VI) ion sorbents. The surface area of BC, BC-Fe and BC-Fe-U was 259, 163 and 117 m² g⁻¹, respectively. The structure of BC was dominated by micropores, while in BC-Fe and BC-Fe-U mesopores predominated. Based on the XRD results, it was found that the magnetic properties of the biochar-iron oxide composites are due to the presence of ferrimagnetic magnetite (Fe3O4) and maghemite (Fe2O3). The optimal pH of As(V) and Cr(VI) adsorption onto the studied sorbents is in the range of 2.3–5.7. Pristine biochar (BC) does not adsorb As(V) ions; however, it enables rapid adsorption of Cr(VI) with the static adsorption capacity of 19.2 mg g⁻¹. The maximum static adsorption capacities of As(V) and Cr(VI) ions onto BC-Fe and BC-Fe-U are within the range of 13.5–16.3 mg g⁻¹. For most adsorption systems tested, adsorption equilibrium is reached within 4 h, though even a few minutes is enough to reach half of the adsorption static value. Phosphates over 0.005 mol L⁻¹ hinder adsorption of As(V) and Cr(VI) ions. Application of at least 5 mol L⁻¹ nitric acid allows about 95% of Cr(VI) and As(V) to be desorbed from adsorbate-loaded BC-Fe material. For other materials, the desorption efficiencies are significantly lower. BC-Fe and BC-Fe-U materials were successfully used for simultaneous Cr(VI) and As(V) removal from river water.
... Digestion of residual biomass by microbes or bacteria to produce biogas or enzymes also attracted high attention since the production costs are low. Valorization of residual biomass as biofuels [3,4], biogas [5,6], biosorbent [7,8], biochar [9,10] and biopesticides [11,12] was also investigated, as well as reuse of residual biomass as soil amendment [13,14], organic mulch [15] and animal feed [16]. ...
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Lavandin hydrochars obtained by hydrothermal carbonization (HTC) of Lavandula distilled straw (LDS) have been studied as an eco-friendly and economical valorization route of residual biomass from cosmetic industry into solid fuels. The critical parameters of the HTC process (temperature and retention time) were normalized to severity factor (SF). Proximate and ultimate analysis, microscopy and thermal analysis were used to characterize hydrochars surface, combustion behavior and kinetics as a function of SF, and to compare them with those of the raw lavandin sample. Results showed that preparation of lavandin hydrochars in temperature and retention time conditions providing SF close to 6 seemed to be the best compromise since under these conditions, the combustion performance of the hydrochar was close to the bituminous coal and lignite.
... Magnetic modification of biochar provides a feasible solution to overcome these drawbacks (Ahmed et al., 2021b). There are a lot of magnetic biochars for water purification (Chen et al., 2011;Wang et al., 2018;Zhang et al., 2015;Li et al., 2020;Lomenech et al., 2021;Nie et al., 2021;Zahedifar et al., 2021), but only a few used for uranium removal. Recently, there have been studies of using magnetized biochar, including iron nanoparticles in silicon-containing biochar (Sen et al., 2021), biochar derived from Tribulus terrestris (Ahmed et al., 2021b), Citrullus lanatus L. seeds biochar (Ahmed et al., 2021a), nano zero-valent iron-activated biochar (Zhang et al., 2021), and others (Thines et al., 2017;Nie et al., 2021) for removal of U(VI). ...
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Biosorption using modified biochar has been increasingly adopted for the sustainable removal of uranium-contaminated from an aqueous solution. In this research study, the facile preparation and surface characteristics of magnetized biochar derived from waste watermelon rind to treat U(VI) contaminated water were investigated. The porosity, specific surface area, adsorption capacity, reusability, and stability were effectively improved after the magnetization of biochar. The kinetics and isotherm studies found that the U(VI) adsorption was rate-limiting monolayer sorption on the homogeneous surface of magnetized watermelon rind biochar (MWBC). The maximum adsorption capacity was found to be 323.56 mg of U(VI) per g of MWBC at pH 4.0 and 293 K that was higher than that of watermelon rind biochar (WBC) (135.86 mg g⁻¹) and other sourced biochars. The surface interaction mechanism, environmental feasibility, applicability for real-filed water treatment studied in the electromagnetic semi-batch column, and reusability of MWBC were also explored. Furthermore, salient raised the ion exchange and complexation action capacity of MWBC due to the presence of Fe oxide. The overall results indicated that MWBC was not only inexpensive and had a high removal capacity for U(VI), but it also easily enabled phase separation from an aqueous solution, with more than three times reusability at a minimum removal capacity of 99%.