Table 2 Conventional parameters of the effluents from different stages of the rapid Fenton process of BDFW at second-scale intervals.

From: A Rapid Fenton treatment of bio-treated dyeing and finishing wastewater at second-scale intervals: kinetics by stopped-flow technique and application in a full-scale plant

Parameter

Average value ± standard deviation

Secondary effluent

Fenton effluent

Floatation effluent

COD

(mg·L−1)

140 ± 3

77 ± 3

76 ± 3

removal efficiency

/

45% ± 2%

46% ± 2%

SCOD

(mg·L−1)

110 ± 3

71 ± 3

70 ± 3

removal efficiency

/

35% ± 3%

36% ± 3%

DOC

(mg-C·L−1)

35 ± 2

26 ± 2

25 ± 2

removal efficiency

/

26% ± 3%

29% ± 3%

BOD5

(mg·L−1)

3 ± 1

1 ± 1

2 ± 1

removal efficiency

/

67% ± 33%

33% ± 33%

TN

(mg-N·L−1)

48 ± 2

47 ± 2

46 ± 2

removal efficiency

/

2% ± 2%

4% ± 2%

NH3-N

(mg-N·L−1)

0.04 ± 0.01

0.03 ± 0.01

0.02 ± 0.01

removal efficiency

/

25% ± 25%

50% ± 25%

TP

(mg-P·L−1)

4.19 ± 0.05

1.14 ± 0.05

1.21 ± 0.05

removal efficiency

/

73% ± 1%

71% ± 1%

Inhibitory effect (%)

51

31

30

  1. Experimental conditions: H2O2 dosage = 128 mg·L−1, [H2O2]:[Fe2+] mole ratio = 1:2, reaction time = 24 s, pH = 3–4.