Table 5.
Material | Target | Performance | Advantages | Ref. |
---|---|---|---|---|
CS‐ PAA hydrogel |
Removal of: Cu2+ Pb2+ |
Adsorption capacity: 302 mg g−1 613 mg g−1 |
Easily regenerated for five cycles | [212] |
CMC‐MMT‐PAM |
Removal of: Pb2+ removal Cd2+ removal |
Adsorption capacity: 456 mg g−1 278 mg g−1 |
Five adsorption–desorption cycles without any significant loss of uptake capacities | [272] |
Fe3O4 NPs‐P(St‐co‐DVB) |
Removal of: Pb2+ Cd2+ |
Adsorption capacity: 257 m2 g−1 129 m2 g−1 |
Easily separated and recycled by a magnet | [197] |
Magnetic HPC‐PAA beads |
Removal of: Cd2+ Cu2+ |
Adsorption capacity: 300 mg g−1 243 mg g−1 |
Easy separation with a magnet, similar capacities for five cycles | [194] |
PAA−Fe3O4 NC beads |
Removal of: Crystal violet (CV) Pb2+ removal |
Adsorption capacity: 80 mg g−1 291 mg g−1 |
Easily handled No leaching of iron |
[103] |
Organo‐silica foam |
Removal of: Sunset yellow MB Cu2+ |
Adsorption capacity: 1.21 g g−1 280 mg g−1 226 mg g−1 |
Materials containing amino, epoxy, and carboxyl groups | [172] |
Amino‐organosilica monolith | Cr4+ removal | Removing efficiency: 92.8% | Working capacity: 4.24 kg g−1 | [275] |
FeOOH NP hydrogels | As5+ | Removal efficiency: 50% | Easily recovered | [198] |
Al2O3‐PAA‐PEI |
Cr(VI) CR |
141 mg g−1 37 mg g−1 |
No chance of secondary contamination | [201] |
Ag NPs‐PVI beads |
Adsorption of: As3+ Eriochrome black T |
Adsorption capacity: 333.36 mg g−1 81.14 mg g−1 |
Multifunctional for removing inorganic, organic and biological contaminants Easily handled |
[102] |
Inactivation of S. aureus | Bactericidal efficiency: ≈96% | |||
Inactivation of E. coli | Bactericidal efficiency: ≈100% | |||
Amine‐modified PEGMA |
Removal of: Ag+ Cu2+ Cr3+ |
Adsorption capacity: 9.05 mmol g−1 4.31 mmol g−1 2.92 mmol g−1 |
[156] | |
Polyelectrolyte‐based polyHIPEs | Ag+ ion exchange | Exchange capacity: 3.53 mmol g−1 | [146] | |
GMA‐based microspheres | Adsorption of Li+ | Adsorption capacity: 38.13 mg g−1 |
Selective removal Recycled five times |
[277] |
Ag‐modified PS sulfonate | Removal of Li+ |
Adsorption capacity: 59.85 mg g−1 at 15 °C 35.06 mg g−1 at 25 °C 27.09 mg g−1 at 35 °C |
Adsorption efficiency: 80.71% after being recycled seven times | [204] |
Amidoxime‐modified hollow MF resin microspheres | UO2 2+ removal | Adsorption capacity: 553.3 mg g−1 | Higher selectivity in the presence of other ions | [165] |
P4VP grafted P(St‐co‐DVB) | Pu separation | Ion exchange column with convective mass transfer property | [115] | |
CMC‐PAM/MMT |
Removal of: Rb+ Cs+ |
Adsorption capacity: 178 mg g−1 266 mg g−1 |
[219] | |
Yeast‐PAA |
Removal of: Rb+ Cs+ Sr2+ |
Adsorption capacity: 180 mg g−1 230 mg g−1 167 mg g−1 |
Materials recycled five times with good performance | [155] |
CS‐g‐PAM | MB removal | Adsorption capacity: 454 mg g−1 | [139] | |
UiO‐66‐PAM | MB removal | Adsorption capacity: 50 mg g−1 | [142] | |
PDMAEMA and HEMA polymers |
Adsorption of: MB methyl orange (MO) |
Adsorption capacity: 6.5 mg g−1 1.6 mg g−1 |
[157] | |
Polyampholytes |
Removal of: MB Erythrosine |
Adsorption capacity: 88 mg g−1 57 mg g−1 |
[147] | |
Porous PAM microspheres |
Removal of: MB methyl violet (MV) |
Adsorption capacity: 669 mg g−1 750 mg g−1 |
Prepared by O/W/O emulsion templating | [169] |
TiO2/P(AM‐co‐AMPS) monoliths |
Removal of: MB TC |
Adsorption capacity: 1.66 g g−1 1.13 g g−1 |
[134] | |
Molecularly imprinted polymers hollow microspheres | Removal of λ‐cyhalothrin | Adsorption capacity: 24.79 mg g−1 | Material can be recycled seven times with 8.11% loss of affinity | [167] |
P(St‐co‐NPA) beads | Removal of atrazine | Removal efficiency: 98% | [117] | |
Graphene and silicon‐doped porous carbon | Removal of trifluralin | Removal efficiency: up to 100% | Used as a column for solid phase extraction to detect trifluralin in soil samples | [256] |
Fe3O4@HKUST‐1‐embedded P(EHA‐DVB‐MMA) [poly(2‐ethylhexyl acrylate‐divinylbenzene‐methyl methacrylate)] | Sorptive extraction of TC |
Limit of detection: 1.9–4.6 and 5.5–13.9 ng mL−1 for milk and egg samples of chicken Limit of quantification: 1.8–3.7 and 5.3–13.0 ng g−1 for muscle and kidney samples of chicken |
[215] | |
Modified Fe3O4 NPs‐CS‐PAMPS porous adsorbents |
Removal of: TC Chlorotetracycline (CTC) |
Adsorption capacity: 806.60 mg g−1 876.60 mg g−1 |
Material recycled five times | [193] |
rGO‐polyHIPE hybrids | Adsorption of polyaromatic hydrocarbons (PAHs) | Adsorption capacity: 47.5 mg g−1 | Reused for ten consecutive cycles | [254] |
poly(4‐vinylbenzyl chloride) (PVBC) monolithic columns | Removal of benzoyl chloride | Removal efficiency: 98% | [116] | |
P(St‐EGDMA) |
Adsorption of: Toluene Benzene |
Adsorption capacity: 0.777 g g−1 0.907 g g−1 |
Material can be reused ten times | [120] |
P(St‐co‐VBC‐co‐DVB) monoliths | Absorption of chemical warfare agents | Mass increase 40–55 times that of dry polymer | [113] | |
P(St‐co‐DVB) aerogels | Adsorption of organic liquids and oil | Adsorption capacities: 13–29 g g−1 | Material stable and reusable | [110] |
P(St‐co‐DVB) |
Adsorption of: n‐hexane Mineral ether Kerosene Benzene THF DCM Salad Gasoline Machine oil |
Adsorption capacity: 4.45 g g−1 5.02 g g−1 6.19 g g−1 18.71 g g−1 15.23 g g−1 20.21 g g−1 2.75 g g−1 16.49 g g−1 2.51 g g−1 |
Materials recycled ten times | [109] |
Silica‐P(tBMA‐DVB) composites |
Adsorption of: n‐hexane Benzene DCM THF Ethanol Methanol Acetone Kerosene oil Used‐transformer oil |
Adsorption capacity: 3.86 g g−1 15.37 g g−1 17.33 g g−1 13.42 g g−1 5.61 g g−1 4.52 g g−1 3.43 g g−1 8.17 g g−1 4.98 g g−1 |
Materials recycled at least 13 times | [181] |
PPI‐SPS‐b‐PE‐r‐Bt‐b‐PS xerogels |
Adsorption of: Hexane Toluene Xylene DCE Chloroform Vegetable oil Gasoline Diesel Engine oil Crude oil |
Adsorption capacity: 19.8 g g−1 22.3 g g−1 24.9 g g−1 22.6 g g−1 32.2 g g−1 24.2 g g−1 21.2 g g−1 23.8 g g−1 31.5 g g−1 15.1 g g−1 |
Materials recycled at least 40 times | [126] |
SPS‐b‐PE‐r‐Bt‐b‐PS and PAMAM dendrimers‐based sponges |
Removal of: n‐hexane Chloroform Crude oil |
Adsorption capacity: 25.4 g g−1 25.8 g g−1 14.4 g g−1 |
Material recycled 30 times with ≈15% loss of performance Oil/water separation |
[125] |
Fluorinated P(PEM‐St‐DVB) material | Remove of DCM | Removal efficiency: 95% | Materials reused for ten cycles | [122] |
PDMS‐infused PS‐based slippery membrane systems | Liquid (oil and water) and solid‐ contaminant repelling | Materials showing self‐repairing and regeneration properties | [171] | |
PU monoliths | Oil spill reclamation | Recovery rate: ≈85% | Materials recycled 20 times | [128] |
Cellulose‐based PU |
Adsorption of: DMSO Non‐polar solvent |
Adsorption capacity: 22 cm3 g−1 9.5 cm3 g−1 |
Void filling, no expansion | [129] |
PU with reactive block copolymer |
Adsorption of: Chloroform DCE |
Adsorption capacity: 36 g g−1 27.3 g g−1 |
2 min half equilibrium time | [130] |
Silica−polyHIPE composite networks | Sorption/desorption of crude oil | Sorption/desorption capacity: ≈16 g g−1 | Material reused for 25 cycles | [190] |
Fe3O4/PS composites | Diesel/water separation | Adsorption capacity: 7.9 g g−1 | Materials recycled ten times | [196] |
Edible oil/water separation | Adsorption capacity: 8.3 g g−1 | |||
Lubricating oil/water separation | Adsorption capacity: 16.4 g g−1 | |||
P(St‐co‐DEAEMA) membranes | Oil/water separation | Chloroform/water, hexane/water | CO2‐switchable separation | [119] |
sPS‐based nanofibrous monoliths |
Adsorption of: Organic solvent Edible oil Fuel oil |
Adsorption capacity: 81.3 g g−1 44.4 g g−1 41.9 g g−1 |
Highly reusable, loss of 10% uptake capacity after 20 cycles. | [112] |
Graphene foams | Removal of oil (toluene, hexadecane, and olive oil) | [258] | ||
rGO‐based cellular network | Adsorption of diesel, gasoline, motor oil, petroleum, and toluene | Adsorption capacities: 100–300 g g−1 using the material with a density of 4.3 mg cm−3; over 600 g g−1 with a lower density material (1.5 mg cm−3) | Recycled by compression for at least six cycles with the capacity maintained at >95% | [259] |
Ag NPs‐PVSA beads |
Adsorption of: Hg2+ Rhodamine B |
Adsorption capacit: 190.58 mg g−1 53.02 mg g−1 |
Multifunctional in removing inorganic, organic, and biological contaminants Easily handled |
[98] |
Inactivation of S. aureus | Bactericidal efficiency: 98.39% | |||
Inactivation of E. coli | Bactericidal efficiency: ≈100% | |||
Ag‐m‐MOP‐PAM composites | Catalytic reduction of 4‐nitrophenol | Rate of reaction: 0.037–0.197 min−1 | [205] | |
Fe3O4‐PAM beads | Decomposition of MO | Decomposition efficiency: 99.6% | Material reused six times | [195] |
TiO2 beads | Photodegradation of MB | Degradation efficiency: 98.53%; rate constant = 0.05 min−1 | Photodegrading the organic and photodisinfection of biological contaminants | [101] |
Photodisinfection of E. coli | Bactericidal efficiency: 100% | |||
Photodisinfection of S. aureus | Bactericidal efficiency: 100% | |||
PAE‐based polyHIPEs | Degradation of bisphenol A (BPA) | Degradation efficiency: 98% |
Organic photocatalyst Visible light‐active |
[147] |
P(St‐co‐DVB) impregnated with PEI | CO2 capture from different sources |
Adsorption capacity: 5.6 mmol g−1 (pure CO2); 4.5 mmol g−1 (10% CO2/N2); 6.4 mmol g−1 (under moisture) |
High CO2/N2 selectivity, fast kinetics, stability | [108] |
P(St‐co‐DVB)/nano‐TiO2/PEI | CO2 capture | Capture capacity: 5.25 mmol g−1 | Rapid adsorption/desorption within 10 min; reused 50 times with a capacity loss of less than 10% | [199] |
PGD‐HKUST‐1‐PEI | CO2 capture from different sources | Adsorption capacity: 4.3 mmol g−1 (pure CO2); 3.0 mmol g−1 (simulated flue gas); 1.8 mmol g−1 (air) | 2.8 mmol (CO2 from simulated flue gas) per gram after 20 cycles | [217] |
CNT‐PEI foam | CO2 capture | Capture capacity: 2.555 wt% | Highly recyclable | [288] |
HIPE templated p(NMe3 +–MS OH−) material | CO2 capture |
Overall sorption rate: 2.5 × 10−2 mmol; Swing size: 4.9 × 10−1 mmol g−1 |
Reversible CO2 capture by humidity swing | [186] |
P(VBC‐DVB) modified with quaternary ammonium hydroxide groups | CO2 adsorption |
Adsorption rate: up to 1.1 × 10−1 mmol min−1 g−1; desorption rate = up to 3.5 × 10−2 mmol min−1 g−1; overall rate = up to 2.5 × 10−2 mmol min−1 g−1 Swing size: up to 7.2 × 10−1 mmol g−1 |
[291] | |
Zeolite‐embedded PAM‐derived carbon foams | CO2 capture |
Capture capacity: 5 mmol g−1 Regenerated by electric swing adsorption |
CO2/N2 selectivity of up to 80 70% performance retention after 30 cycles under humid conditions |
[250] |
Silica‐P(St‐co‐DVB) | Removal of particulate matters (PM2.5) |
Removal efficiency: 93% Saturated adsorption capacity: ≈520 mg g−1 |
Easily separated, recycled | [187] |
P(St‐co‐MMA) monolith filter | Removal of particulate matters (PM2.5) and CO2 | Removal efficiency: 73% for PM2.5 and 77.2% for CO2 | Materials showing excellent dust loading capacity and good resistance | [118] |
Zwitterionic hydrogel polyHIPEs | Environmental sensitivity | Anti‐polyelectrolyte effect | [145] | |
Modified P(St‐DVB‐EHA) membranes | Sensing K+ ions | Improved detection limits and selectivity [compared to poly(vinyl chloride) (PVC) membranes] | Nernstian response to K+ ions | [121] |
Porous Co3O4 | NH3 gas sensing | Sensitivity 146% and response time 2 s for a concentration of 100 ppm | Limit of detection: 0.5 ppm | [293] |
rGO/PolyHIPE foam | Pressure sensing |
High sensitivity (over 0.6 Pa to 200 kPa pressure range) Response time: less than 15.4 ms Cyclic stability: at least 10 000 cycles |
[253] | |
rGO/polyHIPE foam | Pressure sensing |
Gauge factor: 1.5 within 15% strain Pressure response range: up to > 200 kPa Pressure sensitivity: 0.83 kPa−1 for pressure <20 kPa |
[255] |