Table 1.
Comparison of adsorption capacities of MG adsorbed by various adsorbents.
Adsorbents |
Experimental conditions |
qmc (mg/g) |
References |
|||
---|---|---|---|---|---|---|
Dosage (g/L)a |
pH | Temp.(K) | C0b (mg/L) | |||
CO2-activated porous carbon | 0.4 | Undefined | 313 | 40–100 | 284 | [52] |
PVP@CNTs-Cu2O | 2.0 | Undefined | 293 | 50–3000 | 1423 | [53] |
Fe-Cu bagasse composite | 1.0 | Undefined | 298 | 1–150 | 61 | [54] |
chitosan–surfactant–core–shell (CSCS) beads | 0.8 | 7.00 | 298 | 10–400 | 360 | [55] |
AC-H3PO4/Steam | 1.0 | Undefined | 298 | 500–1200 | 769 | [56] |
granular composite hydrogel(AA–IA–APT5) | 0.5 | Undefined | 303 | 200–1800 | 2433 | [57] |
NiO flowerlike nanoarchitectures | 0.3 | Undefined | Ambient | 50 | 142 | [58] |
Gx-cl-P(AA-co-AAm)/Fe3O4 hydrogel nanocomposite | 0.2 | neutral pH | 298 | 100–500 | 497 | [59] |
bivalve shell-Zea mays L. husk leaf | 2.5 | 6.00 | 303 | 10–200 | 82 | [60] |
Fe-Cu based adsorbent | 0.3 | 6.58 | 303 | 50–500 | 1399 | This work |
Fe-Cu based adsorbent | 0.3 | 6.58 | 313 | 50–500 | 1476 | This work |
the mass of the adsorbent contained in each volume of MG aqueous solution
the initial concentration of MG in the aqueous solution
the maximum adsorption capacity of adsorbent (calculated from the Langmuir model)