chemical engineering vol 5 coulson & richardson''s
chemical engineering vol 5 coulson & richardson's
... d
1
(mm)
n
1
nd
1
nd
2
1
nd
3
1
nd
4
1
6.00
5. 00 0.26 1.3 6 .5 32 .5 162 .5
4.00
3.00 0.18 0 .54 1.62 4.86 14 .58
2.00
1.3 75 0.23 0.316 0.4 35 0 .59 8 0.822
0. 75
0.67 0.08 0. 053 6 0.0 359 0.0241 0.0161
0 .50
0.37 0.17 0.0629 0.0233 ... mm to the follow-
ing product:
Size (mm) Amount of product (per cent)
12 .5 0 .5
7 .5 7 .5
5.0 45. 0
2 .5 19.0
1 .5 16.0
0. 75 8.0
0.40 3.0...
coulson & richardson’s - chemical engineering volume 6 (solution)
... -1400 900
80 +900 -2300 0
65 0 -2300 0
60 -55 0 -1 750 55 0
55 -12 25 -52 5 17 75
50 -400 -1 25 21 75
25 7 25 - 850 1 450
20 5 - 855 14 45
C
C
C
H
H
H
4
5
6
3
1
2
(
)
(
)
(
)
TCCH
H
p
C
p
Δ−=Δ
∑∑
...
5 =
outint
TT (hot)
Stream Type T
act
T
int
1 C 20 50 25 55
2 H 70 60 65 55
3 H 65 55 60 50
4 C 85 87 90 92
5 C 75 77 80 82
6 H...
coulson and richardson - chemical engineering vol. 2 particle technology and separation processes (5th ed)
... 54 0
10.8. REFERENCES 54 0
10.9. NOMENCLATURE 54 0
11 Distillation 54 2
11.1. INTRODUCTION 54 2
11.2. VAPOUR LIQUID EQUILIBRIUM 54 2
11.3. METHODS OF DISTILLATION TWO
COMPONENT MIXTURES 55 5 ... 827
15. 1. INTRODUCTION 827
15. 2. CRYSTALLISATION FUNDAMENTALS 828
15. 3. CRYSTALLISATION FROM SOLUTIONS 853
15. 4. CRYSTALLISATION FROM MELTS 868
15. 5. CRYSTALLISATION FROM...
coulson & richardson_s chemical engineering. vol. 6 chemical engineering design 4th ed
... correlation 55 2
11.10.4 AIChE method 55 3
11.10 .5 Entrainment 55 6
11.11 Approximate column sizing 55 7
11.12 Plate contactors 55 7
11.12.1 Selection of plate type 56 0
11.12.2 Plate construction 56 1
11.13 ... distillation 50 1
11 .5 Design methods for binary systems 50 3
11 .5. 1 Basic equations 50 3
11 .5. 2 McCabe-Thiele method 50 5
11 .5. 3 Low product concentrations 50 7...
chemical engineering vol 2 particle technology and separation processes 5ed
... 0.0138 350
52 0.0116 2 95 50 0.0100 254 48 0.0116 2 95 40 0.01 65 420
40 0.01 25 347 42 0.0133 351 35 0.0197 50 0
44 0.0139 353 35 0.0164 417 30 0.0232 59 0
36 0.0166 422 30 0.0166 422 32 0.01 95 4 95
30 ... 0.0474 1204 12 0.0416 1 056 14 0.0460 1168 16 0.0469 1190
12 0. 055 3 14 05 10 0. 050 0 1270 12 0. 055 0 1397
10 0.0660 1676 8 0.0620 157 4 10 0.0 650 1 651 14 0. 055 5 1410
8...
coulson & richardson - solutions to the problems in chemical engineering volume 2 & 3
... d
1
(mm)
n
1
nd
1
nd
2
1
nd
3
1
nd
4
1
6.00
5. 00 0.26 1.3 6 .5 32 .5 162 .5
4.00
3.00 0.18 0 .54 1.62 4.86 14 .58
2.00
1.3 75 0.23 0.316 0.4 35 0 .59 8 0.822
0. 75
0.67 0.08 0. 053 6 0.0 359 0.0241 0.0161
0 .50
0.37 0.17 0.0629 0.0233 ... mm to the follow-
ing product:
Size (mm) Amount of product (per cent)
12 .5 0 .5
7 .5 7 .5
5.0 45. 0
2 .5 19.0
1 .5 16.0
0. 75 8.0
0.40 3.0...
albright's chemical engineering handbook
... 3 85 992.18 0. 051 242 167 .53 257 3 .5 0 .57 24 8. 255 5
45 0.009 59 5 990.17 0.0 65 5 65 188.43 258 2.4 0.6386 8.1633
50 0.012 352 988.00 0.083 147 209.34 259 1.3 0.7038 8.0748
55 0.0 15 762 9 85. 66 0.104 56 ... 253 7.4 0.29 65 8.6660
25 0.003 170 997.00 0.023 0 75 104.83 254 6 .5 0.3672 8 .55 66
30 0.004 247 9 95. 61 0.030 4 15 1 25. 73 255 5 .5 0.4368 8. 452 0
35 0.0...
coulson richardsons chemical engineering volume 1 solutions
... or:
1 .5 D 2.0
n
and n D ln 1 .5/ ln 2.0 D 0 .58 5.
Also: h
2
/h
1
D
2
/
1
0 .58 5
When
2
/
1
D 1 .50 , h
2
/h
1
D 1 .50
0 .58 5
D 1.27 and the coefficient is increased by 27%
8 CHEMICAL ENGINEERING ... Richardson
Chemical Engineering, Volume 5, Second edition
Solutions to the Problems in Volumes 2 and 3
J. R. Backhurst and J. H. Harker
Chemical Engineering, Volume...
Từ khóa: