ULTRAFILTRATION AND MICROFILTRATION HANDBOOK
TYPOS and CORRECTIONS
UPDATE  APRIL 2002
Page 
Location 
As written presently 
Correction 
129 
9th line from bottom 
....the ratio of momentum transfer of mass transfer. 
....the ratio of momentum transfer to mass transfer. 
383 
Figure 8.28 legend 
(... Cheryan and Bogush 1955) 
(.... Cheryan and Bogush 1995) 
UPDATE  AUGUST 2001
Page 308: Last sentence: As a first approximation, the average flux (J_{av}) during concentration can be estimated using one of the following equations: J_{av} = 0.5 (J_{i} + J_{f} ) (7.23a) J_{av} = J_{f} + 0.33(J_{i}  J_{f}) (7.23b) Use equation 7.23a for a gradual decline in flux with concentration and/or for small values of VCR. Use equation 7.23b for sharp declines in flux or large concentration factors. Page 313: 5th line from bottom: 1. Batch: From Equation (7.23a), average flux …….

UPDATE  AUGUST 2000
Page 
Location 
As written presently 
Correction 
19 
Equation (1.25) 
p = RT ln X_{1}/V_{i} 
p =  RT ln X_{1}/V_{i} 
249 
4th line from bottom 
Section 6.C.2. 
Section 6.D.2. 
UPDATE  May 2000
[The corrections shown below are already incorporated in copies purchased after July
2001]
Page 
Location 
As written presently 
Correction 
44 
Line 11 
3. CA membranes relatively easy.. 
3. CA membranes are relatively easy... 
45 
Last line of 2.C.2. 
(Section 2.E.) 
(Section 2.D.) 
109 
2nd para, last line 
(see Section 8.B.3 and Figures ...) 
(see Section 8.B.5 and Figures ...) 
132 
Line 3 of text 
1.12 x 10^{3}; 
1.12 x 10^{3} 
137 
Line 3 of text 
The slope of a plot of log J versus log of the concentration ... 
The slope of a plot of J versus log of the concentration... 
221 
Line 10, 2nd para 
...designs such as the 2" and 8" modules in Figure 5.34), 
...designs such as the 2" and 12" modules in Figure 5.34), 
264 
Line 5, 3rd para 
As discussed in Section 4.I.3. and 4.J.1., Brownian ... 
As discussed in Section 4.I.3. and 4.J., Brownian ... 
316 
Line 1, last para 
Diafiltration is conducted in batch plant... 
Diafiltration is conducted in a batch plant... 
320 
Equation 7.34, denominator 
(J_{av})_{CD}.A 
C_{B}.(J_{av})_{CD}.A 
321 
Equation 7.36, denominator, second term 
(J_{av})_{CD}.A 
C_{B}.(J_{av})_{CD}.A 
329 
Table 7.9 
kPa L/h LMH m^{2}; kJ/m^{3} 47,994 kPa L/h LMH m^{2}; kWh/m^{3 } 13.33 
kPa L/h LMH m^{2}; kJ/m^{3} 1 kPa L/h LMH m^{2}; kWh/m^{3 } 2.78 x 10^{4} 
330 
Table 7.10 
kPa L/h m^{2}; kWh/m^{2} 1.333 x 10^{2} 
kPa L/h m^{2}; kWh/m^{2} 2.78 x 10^{7} 
401 
Xaxis of Figure 8.38 
1 1.5 2 3 10 30 
1 1.5 2 5 10 30 
479 
Line 8 of text 
Inital flux was 50 LMH .... 
Initial flux was 50 LMH .... 
522 
"Pall"index 
....208, 230, 374, 500 
....208, 230, 375, 500 