No.

Description

No.

Author

6.1

K-values (K = y/x) in light-hydrocarbon systems, low-temperature range

Fig 13-14a

Perry

6.2

K-values (K = y/x) in light-hydrocarbon systems, high-temperature range

Fig 13-14b

Perry

6.3

Graphical Representation of Fenske-Underwood-Gilliland procedure

Fig 8-5

Chopey

6.4

Minimum Reflux at infinite theoretical plates

Fig 8-5B

Ludwig

6.5

Comparison of rigorous calculations with Gilliland correlation

Fig 13-41

Perry

6.6

Approximate solution for N and L/D in distillation of ideal binary mixtures

Fig 8-5A

Ludwig

6.7

Empirical correlations of overall efficiencies for fractionation and absorption

Fig 8-11

Ludwig

6.8

Separation operations related to distillation

Fig 13-7

Perry

6.9

Corresponding dimensionless groups of mass and heat transfer

Table 3-2

Treybal

6.10

Packed Column performance nomograph

Fig 9-11C

Ludwig

6.11

Packing factors for use with Fig 9-11D

Fig 9-12D

Ludwig

6.12

Mass transfer for simple situations

Table 3.3

Treybal

6.13

Number of overall gas-phase mass-transfer units in a packed absorption tower for constant mG_M/L_M; solution of Equation 14.88

Fig 14-9

Perry

6.14

Absorption and Stripping Factors

Fig 13-43

Perry

6.15

Generalized pressure-drop correlation for packed towers

Fig 8-18

Chopey

6.16

Generalized flooding and pressure drop correlation for packings

Fig 18-38

Perry

6.17

Packing Factors for Column Packings

Table 8-2

Chopey