coulson & richardson’s - chemical engineering volume 6 (solution)

... 2H 2 O -7 4. 86 0 -3 93.77 -2 42.00 ΔH R = [-3 93.77 + 2 (-2 42.00)] – (-7 4. 86) = -8 02.91 kJ mol -1 CH 4 4. C 2 H 6 + 3½O 2 → 2CO 2 + 3H 2 O -8 4.74 0 -3 93.77 -2 42.00 ΔH R = [2 (-3 93.77) + 3 (-2 42.00)] ... kmol -1 C -1 The specific heat capacity of the nitrobenzene gas: a b x 10 2 c x 10 4 d x 10 6 HC -6 .1010 8.0 165...

Ngày tải lên: 01/04/2014, 11:16

... 1.4. The specific volume, v 1 D 22.4/29290/2730.1013/5 D 0.0 166 m 3 /kg. ∴ W D [5 ð 10 6 ð 0.0 166 /0.4][0.1013/5 0.4/1.4  1] D0.139 ð10 6 J/kg Mass of gas D 0.1/0.0 166  D 6. 02 kg ∴ U ... 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 6, Thi...

Ngày tải lên: 01/04/2014, 11:16

... nd 2 nd 3 1 2000 2000 2000 3 60 0 5400 16, 200 6 140 5040 30,240 10 40 4000 40,000 14 15 2940 41, 160 18 5 162 0 29, 160 22 2 968 21,2 96  = 21, 968  = 180,0 56 Thus: d s = (180,0 56/ 21, 968 ) = 8.20 µm This is ... 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 1.375 0.23 0.3 16 0.435 0.598 0.822 0.75 0 .6...

Ngày tải lên: 01/04/2014, 11:15

... nd 2 nd 3 1 2000 2000 2000 3 60 0 5400 16, 200 6 140 5040 30,240 10 40 4000 40,000 14 15 2940 41, 160 18 5 162 0 29, 160 22 2 968 21,2 96  = 21, 968  = 180,0 56 Thus: d s = (180,0 56/ 21, 968 ) = 8.20 µm This is ... 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 1.375 0.23 0.3 16 0.435 0.598 0.822 0.75 0 .6...

Ngày tải lên: 04/06/2014, 13:18

... drop 66 1 12.7.5 Fluid physical properties 66 1 12.8 Tube-side heat-transfer coefficient and pressure drop (single phase) 66 2 12.8.1 Heat transfer 66 2 12.8.2 Tube-side pressure drop 66 6 12.9 Shell-side ... (capacity) 60 2 11.14.5 Column internals 60 9 11.14 .6 Wetting rates 61 6 11.15 Column auxiliaries 61 6 11. 16 Solvent extraction (liquid liquid extraction) 61 7 11. 16. 1 Ext...

Ngày tải lên: 01/04/2014, 11:15

... 712.14 46. 168 1345.0 2749 .6 3.2552 5.7059 310 9. 865 1 69 0 .67 54.541 1402.2 2727.9 3.3510 5 .62 44 320 11.284 66 7.09 64 .63 8 1 462 .2 2700 .6 3.4494 5.5372 330 12.858 64 0.77 77.050 1525.9 266 6.0 3.5518 ... 23.712 1135.0 27 96. 6 2.8849 6. 00 16 270 5.5030 767 . 46 28.073 1185.3 2789.7 2.9 765 5.9304 280 6. 4 166 750.28 33. 165 12 36. 9 2779.9 3. 068 5 5.8579 290 7.4418 731.9...

Ngày tải lên: 01/04/2014, 10:12

... Cooling Towers Symbols 61 8 Problems 61 9 References 62 1 20 Equilibrium-Stage Operations 62 2 Equipment for Stage Contacts 62 2 Principles of Stage Processes 62 5 Equilibrium-Stage Calculations for ... 86 Symbols 590 Problems 592 References 594 19 Humidification Operations 5 96 Definitions 5 96 Humidity Chart 60 0 Wet-Bulb Temperature 60 4 Cooling Towers 60 8 Theory of Counterflow ....

Ngày tải lên: 01/04/2014, 11:53

... McGraw-Hill for their individual course preparation. If you are a student using this Manual, you are using it without permission. Page 16 - 1 PROPRIETARY MATERIAL. © The McGraw-Hill ... McGraw-Hill for their individual course preparation. If you are a student using this Manual, you are using it without permission. Page 26 - 1 PROPRIETARY MATERIAL. © The McGraw-Hi...

Ngày tải lên: 01/04/2014, 11:53