Table 4 The mechanisms and enhanced performance of chemically oxidized and base/acid modified biochars.

From: Recent trends and economic significance of modified/functionalized biochars for remediation of environmental pollutants

Modification

Pollutant

Sorption capacity

Improvement

Functionalities

Mechanism

Reference

NaOH

Chloramphenicol

Around 2100 mg kg−1

Enhance surface graphitic C and oxygen-enrich groups

Carboxyl and carbonyl groups

Formation of H-bonds among N-comprising groups in adsorbent surface and chloramphenicol, Electron-donor–acceptor π-π interaction

22

KOH

As (v)

30.98 mg g−1

More than about 1.3 times higher removal capacity

Carbonyl group

Ion exchange

21

KOH

Cd and Cu

34 and 31 mg g−1

Approximately 20 times higher removal capacity than other raw biochars

Aromatic carbon

Surface precipitation, ion exchange electrostatic attraction, and surface complexation

23

H2SO4

Tetracycline

23.26 mg g−1

Larger SSA and porosity, higher oxygen and carbon contents, lower ash content

O-containing functional groups

Π-π electron donor acceptor interaction between the treated adsorbent surface and aromatic ring

25

H2SO4 + oxalic acids

Sulfamethazine

183–229 L kg−1

–

–

Ligand- and proton-enhanced processes; Increase in SA by acid modification

29

H3PO4

–

–

Enhance water extractable organic carbon content

–

Hydrolysis of ester groups formed during the pyrolysis

26

(Oxidation) H2O2

Pb

22.82 mg g−1

Removal for Pb was 20 times greater than un-treated biochar

Carboxyl groups

Enhance carboxyl groups expedite the formation of bound complexes with Pb

27

(Oxidation) H2O2

Hg

1470.5–1347.9 µg g−1

Substantially higher removal capacity than other un-treated biochars (380–618 ng mg−1)

Ester, Carboxyl, and Carbonyl groups

Higher SSA and total pore volume Surface O-enrich functional groups increase electron transfer, and Hg-oxidation and allow chemisorption centers

28

Acetic acid + Na2S2O4 + H2SO4

Cu

15.97 mg g−1

Enhancing removal capacity in fixed-bed and batch experiments

Amino groups

Ion exchange

40

HNO3 + H2SO4

Cu

12.47 mg g−1

Around 4.62% N was present on the treated adsorbent, fivefold enhancement of removal capacity

Amino groups

Foundation of outer-spherecomplexes with amino groups of treated biochar

41