2018
DOI: 10.1007/s10570-018-1868-2
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PEI-grafted magnetic cellulose for Cr(VI) removal from aqueous solution

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Cited by 57 publications
(15 citation statements)
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“…These results suggest that the process controlling the adsorption rate may be chemical sorption involving valency forces through sharing or exchange of electrons between biosorbent and adsorbate. 56,65 Diffusion from the solid-liquid interface to the interior of the solid particles plays a very important role in adsorption. Fig.…”
Section: Kinetic Studiesmentioning
confidence: 99%
See 1 more Smart Citation
“…These results suggest that the process controlling the adsorption rate may be chemical sorption involving valency forces through sharing or exchange of electrons between biosorbent and adsorbate. 56,65 Diffusion from the solid-liquid interface to the interior of the solid particles plays a very important role in adsorption. Fig.…”
Section: Kinetic Studiesmentioning
confidence: 99%
“…Therefore, studying these isotherms is critical for optimizing the development of the adsorbent. 65,67 To optimize the design of an adsorption system, it is essential to establish the most appropriate correlation for the equilibrium curve (Fig. S4-S6 †).…”
Section: Kinetic Studiesmentioning
confidence: 99%
“…156 Similarly, epichlorohydrin has been employed in a system of cellulose solution, PEI, and magnetic particles to create a crosslink between the cellulose and PEI. 179 The application of magnetic cellulose in devices like loudspeakers indeed is becoming a reality. However, cellulose may also have negative effects on the properties of the device due to its tendency to absorb moisture, which may have an impact on the stability of the device.…”
Section: Discussionmentioning
confidence: 99%
“…The adsorption kinetics were analyzed by means of the pseudo‐first‐order, pseudo‐second‐order, and intraparticle diffusion model. Their linear forms are described in Equations ), respectively 31,32 Qt=Qe()1ek1t Qt=k2Qe2t1+k2Qet Qt=kidt12+C where t is the adsorption time (min); Q e and Q t represent the amount of MB adsorbed at equilibrium and time t (mg g −1 ), respectively; k 1 , k 2 , and k id are the rate constants of the pseudo‐first‐order kinetics (min −1 ); pseudo‐second‐order kinetics (g mg −1 min −1 ), and intraparticle diffusion model (mg [g min 1/2 ] −1 ); and C is a constant involved in the thickness of the boundary layer of the intraparticle diffusion model (mg g −1 ).…”
Section: Methodsmentioning
confidence: 99%
“…Their linear forms are described in Equations (4)-(6), respectively. 31,32 Q t = Q e 1 −e − k 1 t À Á ð4Þ…”
Section: Adsorption Kinetics Modelingmentioning
confidence: 99%