期刊
SEPARATION AND PURIFICATION TECHNOLOGY
卷 292, 期 -, 页码 -出版社
ELSEVIER
DOI: 10.1016/j.seppur.2022.120996
关键词
Wastewater treatment; Heavy metal adsorption; Pore and surface diffusion model; Breakthrough curve; gPROMS; Transport parameters
资金
- University Grant Commission (UGC)
Separation of heavy metals from water bodies is crucial for the protection of human, marine life, and the environment. The adsorptive separation of heavy metals using cheap and environmentally friendly biosorbents shows promise. This study applies the pore volume and surface diffusion (PVSD) model to investigate the mass transfer processes involved in the adsorption of Cu (II), Cd (II), and Pb(II) using different biosorbents. The PVSD model is able to accurately predict concentration decay and breakthrough curves for batch and continuous modes.
Separation of heavy metals from water bodies is a need of hour, to protect human kind, marine life, and the environment. In this context, adsorptive separation of heavy metal over cheap and environmental friendly biosorbent remains promising. Numerous studies have been carried out to characterize the adsorption of heavy metal ions through isotherms, kinetics, and simple mathematical models. However, such studies lacked in detailed mass transfer models evaluating heavy metal adsorption in batch and continuous modes. This work reports the application of pore volume and surface diffusion (PVSD) model investigating mass transfer processes of Cu (II), Cd (II), and Pb (II) adsorptions over alkali-treated Caryotaurens seeds, chemically modified Albizia lebbeck pods, and Schleichera oleosa bark, respectively, in batch and continuous modes. Heavy metal-biosorbent systems are represented by Freundlich, Temkin, and Langmuir isotherms, respectively. PVSD model equations (algebraic, ordinary, and partial differential equations) for batch and continuous modes are solved in gPROMS (General Process Modelling System). For validation, concentration decay and breakthrough curves concerning batch and continuous modes, respectively, are predicted and matched excellently with in-house experimental data and justified with R-2 and RMSE values. In batch mode, external mass transfer coefficient suggested no constraint for heavy metal external transport, whereas, surface and pore volume diffusion coefficients were found to control the adsorption process. For continuous mode, breakthrough curves are predicted concerning metal solution flowrate, initial metal concentration, and bed height, and parameters viz. breakthrough time, exhaustion time, adsorption column capacity, and mass transfer zone are calculated. Axial dispersion and mass transfer coefficients signify negligible resistance for metal ions' bulk transport within the column. Surface and pore volume diffusions affected continuous adsorption process, with surface diffusion being dominant. The current PVSD model may represent other metal-biosorbent systems to estimate transport parameters suitable for continuous adsorber operation.
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