“… Generation of leachate, waste of valuable organic/inorganic materials, emission of greenhouse gases if not engineered | Cheap process with no energy consumption, reduces SS volume | [ 85 , 87 ] | Farm land | – | Direct use of SS without any treatment | Contamination of heavy metals | Great source of inorganic/organic substances as fertilizer or to improve soil properties | [ 81 , 149 ] |
Drying | 60–93 °C. | Spread of waste/SS on open bed of sand and allowed to remain until dry | Climate dependent, unstable temperature conditions, cover large land surface, emit odor, heavy metals pollution | Performed in natural way, affordable, destroy pathogen, reduce sludge volume | [ 136 , 138 ] |
Dewatering | 30–70 °C and 1–300 bar | Minimization of water content from SS for its effective disposal | This treatment process can't mitigate HMs pollution in SS | Improve bio-energy utilization, reduce volume, easy transportation, lessen leachate in landfills, does not contribute to carbon emission | [ 61 ] |
Torrefaction | >300 °C | Low/slow thermal process in oxygen starving environment | Pollution of HMs through different application of torrefied product | Produce high amount of biochar, improves solid fuel properties, low energy consumption, short torrefaction time, enhance carbon fixation and hydrophobicity of torrefied material | [ 134 , 135 ] |
Incineration | Temperatures of 750–925 °C (1400–1700 °F). Residence times are typically 2–5 s. | Straight combustion in excess oxygen supply | Expensive, emit some pollutant gases such us furans and nitrous, ammonia emission, leads to the second pollution via residue (ash) | Odor minimization, reduction of raw waste mass (SS), production of energy. |
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