Table 1 Parameters of isotherm models and kinetic models in batch adsorption studies of MSRH.

From: Purification of Dye-stuff Contained Wastewater by a Hybrid Adsorption-Periphyton Reactor (HAPR): Performance and Mechanisms

Isotherm model

Langmuir model

Freundlich model

q m,cal (mg g−1)

K L (L mg−1)

R 2

n

K F

R 2

  
 

272

0.034

0.979

1.76

18.66

0.906

  

Kinetic model

Initial concentration (mg L −1 )

Shaking Speeds (rpm)

Pseudo-second-order kinetic model

Intraparticle diffusion model

q e,cal (mg g −1 )

k 2 (×10 −3gmg −1 min −1 )

R 2

k id (mg g −1 min −0.5)

C (mg g −1)

R 2

200

160

96

85.0

1.000

8.5

74

0.882

300

160

145

16.2

0.999

7.9

118

0.894

400

160

186

21.8

0.999

10.8

116

0.961

400

60

185

9.2

0.999

19.9

151

0.942