Table 5 Conditions for absorption experiments for adsorption of phenol on activated carbon along with the calculated intraparticle diffusivities, and film mass transfer coefficients.

From: Kinetic similarity as a scaling strategy for batch adsorption reactors to ensure efficient decolorization of sugar syrup on a larger scale

Experiment no.

1

2

3

The volume of liquid (L)

2

20

200

Weight of adsorbent (g)

1.2

12

120

Equal Impeller Reynolds Number

The rotational speed of impeller (RPM)

500

278

108

60

65

Optimum diffusivity of resin

DS×10−8 (cm2/sec)

9

9

9

9

9

Optimum film mass transfer coefficient

k ×10−3 (cm/sec)

5.5

5.7

4.5

4.8

2.7

Equal Power to Volume Ratio (P/V)

The rotational speed of impeller (RPM)

543

195

325

60

180

Optimum diffusivity of resin

DS×10−8 (cm2/sec)

9

9

9

9

9

Optimum film mass transfer coefficient

k ×10−3 (cm/sec)

5.3

5.6

5.3

5.6

5.3