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Table 2 Parameters monitored during operation of the laboratory stirred-tank anaerobic digesters (R1–R6)

From: Effluent solids recirculation to municipal sludge digesters enhances long-chain fatty acids degradation capacity

 

Daysa

R1

R2

R3

R4

R5

R6

Average specific biogas production (ml g−1VSsubstrate day−1)b

0–84

510 ± 95

590 ± 100

570 ± 110

610 ± 100

610 ± 90

570 ± 90

85–171

510 ± 75

590 ± 80

590 ± 80

525 ± 85

940 ± 310

950 ± 310

172–200

515 ± 65

745 ± 400

821 ± 480

590 ± 80

1540 ± 175

1315 ± 310

Cumulative residual biogas (ml)c

201–255

16,340

108,930

85,240

25,280

73,360

97,130

Cumulative residual biogas from oleate (ml)d

201–255

0

92,590

68,900

0

48,080

71,850

Methane (% of biogas)

0–84

61 ± 2

60 ± 2

64 ± 1

60 ± 1

61 ± 1

64 ± 1

85–171

61 ± 1

62 ± 3

64 ± 1

60 ± 1

61 ± 2

66 ± 1

172–200

61 ± 2

63 ± 1

65 ± 1

60 ± 2

64 ± 3

66 ± 2

Gaseous H2S (ppm)

0–84

< 20

< 20

50 ± 35

< 20

 < 20

50 ± 30

85–171

< 20

< 20

190 ± 80

< 20

 < 20

70 ± 20

172–200

< 20

< 20

320 ± 200

< 20

 < 20

150 ± 15

pH

0–200

7.4 ± 0.1

7.4 ± 0.1

7.5 ± 0.1

7.6 ± 0.2

7.6 ± 0.2

7.7 ± 0.2

Total solids (% of total weight)

0–84

2.1 ± 0.3

1.9 ± 0.3

2.4 ± 0.1

2.6 ± 0.2

2.4 ± 0.5

2.8 ± 0.4

85–171

2.0 ± 0.4

2.3 ± 0.4

2.9 ± 0.4

3.5 ± 0.7

3.6 ± 0.4

4.1 ± 0.7

172–200

2.3 ± 0.4

3.5 ± 0.2

3.9 ± 0.8

4.6 ± 0.2

5.0 ± 0.5

5.5 ± 0.3

Volatile solids (% of TS)

0–84

56 ± 2

58 ± 2

53 ± 2

56 ± 2

56 ± 2

53 ± 3

85–171

53 ± 2

54 ± 3

50 ± 2

47 ± 4

48 ± 3

45 ± 3

172–200

50 ± 1

61 ± 5

61 ± 6

43 ± 1

48 ± 2

43 ± 2

  1. aDay 0–84: start-up phase; day 85: start of semi-continuous oleate feeding to R2, R3, R5, and R6; day 172: start of oleate pulse feeding; day 201: end of PASS and oleate feeding
  2. bCalculation of specific biogas production is based on the influent VS content of fresh substrate, does not include the recirculated VS
  3. cCumulative biogas production between days 201 and 255 after the PASS and oleate feeding was stopped
  4. dCumulative residual biogas production from oleate calculated by subtracting the cumulative biogas production in control digester, R1, from the values obtained for oleate-amended R2 and R3 and subtracting the cumulative biogas production of control digester with effluent recirculation, R4, from the values obtained for R5 and R6