|
Biological treatments
|
| Biological degradation |
• Phenol is consumed by microorganisms such as bacteria, algae, yeast, and fungi and convert them to harmless compound |
• Can lead to toxic by-products |
67–69
|
| • Growth control problem |
| • Not suitable for high concentrations of phenol |
| • Sludge production |
| • Requires use of co-solvent when the concentration of phenol is low |
| Enzyme degradation |
• Enzymatic reactions are specific in nature and happened under moderate pH and temperature |
• Non-reusability of the enzymes |
69–71
|
| • Higher catalytic efficiency and lower cost than the traditional chemical methods |
• Enzyme instability in the harsh environment of the wastewater |
| |
|
Chemical treatments
|
| Oxidative process |
• In gaseous oxidation, there is no increase in the volume of wastewater and sludge |
• Use of expensive chemicals |
|
| • Simplicity of application |
• Incomplete oxidation of phenol |
72 and 73
|
| • Safety issue due to the use of hazardous chemicals |
| • H2O2 needs to be activated by some other means |
| • Wet oxidation of phenol is not economical due to the need for high pressure and temperature |
| Electrochemical destruction |
• No need for expensive chemicals |
• Requires expensive equipment |
74
|
| • Sludge is not produced |
• High energy consumption |
| • Safety issues in handling toxic chemicals |
| Photochemical |
• Phenols are greatly degraded, and sludge is not produced |
• By-products are formed |
75 and 76
|
| • Expensive equipment is needed |
| Fenton reagents (H2O2 + Fe(ii) salts) |
• Fenton reagents are environmentally safe and therefore can be easily handled |
Sludge production |
77 and 78
|
| • No need for expensive and complicated apparatus |
| Irradiation |
• Effective oxidation at lab scale |
The requirement of a high amount of dissolved O2
|
|
| |
|
Physical treatments
|
| Membrane filtration |
• Removes all types of dyes |
• Concentrated sludge is produced |
79
|
| Electrocoagulation |
• Economically feasible |
• Production of large amounts of sludge |
80
|
| Distillation |
• Phenols are separated from aqueous media based on relative volatility |
• Needs high energy consumption |
37
|
| • Used for low concentration of phenol removal |
| Adsorption |
• Good for removal of phenol |
• Regeneration is difficult |
4, 81–83
|
| • Need mild temperature and pressure |
• Regeneration need calcination or the use of solvent |
| • Economical |
• Many adsorbents have low adsorption efficiency |
| • Easy to operate and no expensive equipment's required |
• Not suitable for adsorption low level of phenol |
| • Sometimes chemicals are used for adsorbent modification which are expensive and toxic |
|
• Sometimes need a high amount of adsorbent required |
| Liquid–liquid extraction |
• Easy to operate |
• Sometimes has low selectivity |
66, 83–85
|
| • Performed at mild conditions |
• Use of toxic, flammable, and volatile solvents in the extraction process |
| • The extract can be recycled as a raw material |
• Regeneration of solvent might be expensive and challenging |
| Ion exchange |
• Regeneration of adsorbent |
Not effective for all dyes |
66
|