Skip to main content

Table 1 The product yields of microwave pyrolysis sludge under different moisture content and operating conditions

From: Microwave pyrolysis of sludge: a review

Sludge source

Composition

Pyrolysis conditions/carrier gas

Pyrolysis temperature (°C)

Catalysts/microwave absorbers

Pyrolysis carbon yield (wt%)

Pyrolysis oil yield (wt%)

Pyrolysis gas yield (wt%)

Ref.

Wastewater sludge in a petrochemical plant.

Moisture: 84.9 ± 1.20 wt%; Volatile solids: 9.4 ± 0.11 wt%; Ash: 5.6 ± 0.06 wt%; Combustiblesa: 62.9 ± 1.5 wt%; Asha:37.1 ± 0.85 wt%

Multimode-microwave oven; N2;

400–800d

Not reported

69–51d

16.3–20.3d

14.8–29.5d

[6]

Wastewater sludge in a chemical plant.

Moisture: 32.6 ± 2.5 wt%; Volatile solids: 39.3 ± 1.8 wt%; Ash: 28.1 ± 1.3 wt%; Combustiblesa: 58.3 ± 2.7 wt%; Asha:41.7 ± 3.1 wt%

400–800d

Not reported

65–42d

16.2–23.8d

8.3–37.7d

Sludge in a wastewater treatment plant.

Moisture:78%; Asha: 42%;Volatile mattera: 55%;

Multimode-microwave oven; Ar;

500–800d

Not reported

40–36d

45–18d

15–46d

[12]

Sludge in the wastewater treatment facility of a petrochemical plant.

Moisture: 84.9 ± 1.2 wt%; Solids: 15.1 ± 0.3 wt%; Volatile: solidsa: 62.9 ± 0.27 wt%; Asha: 37.5 ± 0.18 wt%;

Multimode-microwave oven; N2;

400–800d

Not reported

57–69d

14–20d

15–29d

[24]

The dewatered high-ash sludge from. Industrial wastewater treatment plant

Moisture: 88.10 wt%; asha: 61.88 wt%; organic substancea: 38.12 wt%; for ash analysis indicated that the contents of Si, Fe, and Al were more than 10.10 wt% and all existed in the form of oxides.

Self-made single-mode and linear adjustable microwave oven; N2;

1131.7b

SiC

78.3 ± 3.9

3.0 ± 0.7

17.0 ± 4.8

[29]

919.2b

Graphitec

84.3 ± 7.3

3.4 ± 0.7

10.8 ± 3.4

1003.5b

Pyrolysis residues

82.5 ± 4.5

3.5 ± 0.6

12.1 ± 5.1

Sludge in the metropolitan wastewater treatment plant.

Moisture: 78 wt%; Asha:17.5 wt%;Volatile mattera: 82.2 wt%; Fixed carbona: 0.3 wt%;

Modified microwave oven; Vacuum;

450–600d

ZSM-5 SiC balls

62.3–33.0d

16.5–28.0d

Not reported

[34]

The remaining sludge in the 5 secondary sedimentation tank of a sewage treatment plant.

Moisture:84.3%; asha: 46.72%; organic substancea: 50.42%; fixed carbona: 2.86%; C, H, N and Sa: 28.86 wt%, 7.35 wt%, 3.88 wt% and 0.89 wt%.

Single-mode and linear adjustable microwave oven; N2;

500–900d

Not reported

70.0 ± 3.4–60.0 ± 2.0d

14.5 ± 0.7–14.4 ± 0.5d

11.3 ± 0.6–23.5 ± 1.1d

[35]

10 wt% CaO

65.2 ± 2.7–51.0 ± 0.8d

15.5 ± 0.7–15.8 ± 0.6d

17.1 ± 0.8–33.1 ± 1.6d

10 wt% Fe2O3

70.2 ± 2.9–55.0 ± 1.4d

11.5 ± 0.5–14.4 ± 0.6d

15.1 ± 0.7–29.5 ± 0.8d

Sludge in urban wastewater treatment plants.

Moisture: 80 wt%; Asha: 24.5%;Volatile mattera: 75.5%;

Multimode-microwave oven; N2;

490c

Not reported

39.4

49.8

10.8

[36]

330–1200d

77.3–32.6d

18.3–7.2d

4.4–60.2d

  1. aDry base
  2. bMaximum quantity
  3. cOptimal amount
  4. dProcess temperature value or addition amount. Indicating the temperature range of the pyrolysis process or the added amount, and corresponds to the range of the pyrolysis product yield