2022
DOI: 10.1016/j.indcrop.2022.115314
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Simultaneous production of clean water and organic dye from dyeing wastewater by reusable lignin-derived porous carbon

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Cited by 23 publications
(7 citation statements)
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“…The adsorption efficiency slightly decreased from 100 % to 89.86 % after the 3 cycles of adsorbed SWC regeneration. Moreover, the OTC adsorption was decreased to 61.37 % after 5 cycles, indicating that the regeneration using a heat treatment significantly generated the soot particles from adsorbed OTC molecules covering the SWC pore structure [ 70 ], as well as the high temperature during regeneration may impact the pore degradation between carbon matrix and OTC adsorbate [ 71 ], resulting in the continuously lowering OTC adsorption efficiency after several regenerations, as displayed in Fig. 8 b.…”
Section: Resultsmentioning
confidence: 99%
“…The adsorption efficiency slightly decreased from 100 % to 89.86 % after the 3 cycles of adsorbed SWC regeneration. Moreover, the OTC adsorption was decreased to 61.37 % after 5 cycles, indicating that the regeneration using a heat treatment significantly generated the soot particles from adsorbed OTC molecules covering the SWC pore structure [ 70 ], as well as the high temperature during regeneration may impact the pore degradation between carbon matrix and OTC adsorbate [ 71 ], resulting in the continuously lowering OTC adsorption efficiency after several regenerations, as displayed in Fig. 8 b.…”
Section: Resultsmentioning
confidence: 99%
“…The equilibrium adsorption capacity ( Q e , mg g −1 ), the instantaneous adsorption capacity at a certain adsorption time t ( Q t , mg g −1 ) and the dye solution removal rate ( R , %) were calculated according to eqn (1)–(3).where C 0 (mg L −1 ), C e (mg L −1 ), and C t (mg L −1 ) represent the initial, equilibrium and instantaneous concentration of the dye solution at a certain adsorption time of t , respectively; m (g) is the mass of the as-prepared samples added; V (mL) represents the volume of the reaction solution. Moreover, in order to explore the adsorption mechanism of MB molecules on the pudding-like Fe/C, the obtained experimental data were fitted using the pseudo-first (4) 28 and second-order (5) models. 29 ln ( q e − q t ) = ln q e − k 1 t where q e is the equilibrium absorption capacity (mg g −1 ) and q t is the absorption amount (mg g −1 ) at a specific time of t (min).…”
Section: Methodsmentioning
confidence: 99%
“…where C 0 (mg L À1 ), C e (mg L À1 ), and C t (mg L À1 ) represent the initial, equilibrium and instantaneous concentration of the dye solution at a certain adsorption time of t, respectively; m (g) is the mass of the as-prepared samples added; V (mL) represents the volume of the reaction solution. Moreover, in order to explore the adsorption mechanism of MB molecules on the pudding-like Fe/C, the obtained experimental data were fitted using the pseudo-first (4) 28 and second-order (5) models. 29 ln (q e À q t ) = ln q e À k 1 t (4)…”
Section: Adsorption Activity Tests and Kinetic Adsorption Isotherm Mo...mentioning
confidence: 99%
“…At present, pollution control technology had become an important factor affecting economic and social development, and the adsorption treatment technology of the organic dyes had been widely concerned. [27][28][29][30] The traditional adsorption materials were not easy to separate and regenerate. They carried the risk of secondary pollution.…”
Section: Introductionmentioning
confidence: 99%