Page 13 - Chemical Process Equipment - Selection and Design

X LIST OF EXAMPLES

13.13 Trays and Transfer Units for an Absorption Process 403 15.2 Adsorption of n-hexane from a Natural Gas with Silica
13.14 Representation of a Petroleum Fraction by an Equivalent Gel 505
Number of Discrete Components 413 15.3 Sue of an Ion Exchanger for Hard Water 513
13.15 Comparison of Diameters of Sieve, Valve, and Bubblecap 16.1 Design of a Crystallizing Plant 524
Trays for the Same Service 431 16.2 Using the Phase Diagrams of Figure 16.2 528
13.16 Performance of a Packed Tower by Three Methods 441 16.3 Heat Effect Accompanying the Cooling of a Solution of
13.17 Tray Efficiency for the Separation of Acetone and MgSO, 529
Benzene 451 16.4 Deductions from a Differential Distribution Obtained at a
14.1 The Equations for Tieline Data 465 Known Residence Time 533
14.2 Tabulated Tieline and Distribution Data for the System 16.5 Batch Crystallization with Seeded Liquor 534
A = 1-Hexene, B = Tetramethylene Sulfone, C = Benzene, 16.6 Analysis of Size Distribution Data Obtained in a
Represented in Figure 14.1 466 CSTC 537
14.3 Single Stage and Cross Current Extraction of Acetic Acid 16.7 Crystallization in a Continuous Stirred Tank with Specified
from Methylisobutyl Ketone with Water 468 Predominant Crystal Size 538
14.4 Extraction with an Immiscible Solvent 469 16.8 Crystallization from a Ternary Mixture 544
14.5 Countercurrent Extraction Represented on Triangular and 18.1 Separation of Oil and Water 614
Rectangular Distribution Diagrams 470 18.2 Quantity of Entrainment on the Basis of Sieve Tray
14.6 Stage Requirements for the Separation of a Type I and a Correlations 61 7
Type I1 System 471 18.3 Liquid Knockout Drum (Empty) 618
14.7 Countercurrent Extraction Employing Extract Reflux 472 18.4 Knockout Drum with Wire Mesh Deentrainer 620
14.8 Leaching of an Oil-Bearing Solid in a Countercurrent 18.5 Size and Capacity of Cyclone Separators 621
Battery 472 18.6 Dimensions and Weight of a Horizontal Pressure
14.9 Trial Estimates and Converged Flow Rates and Drum 628
Compositions in all Stages of an Extraction Battery for a 19.1 Applications of the Equation for Osmotic Pressure 633
Four-Component Mixture 476 19.2 Concentration of a Water/Ethanol Mixture by Reverse
14.10 Sizing of Spray, Packed, or Sieve Tray Towers 486 Osmosis 642
14.11 Design of a Rotating Disk Contactor 488 20.1 Installed Cost of a Distillation Tower 663
15.1 Application of Ion Exchange Selectivity Data 503 20.2 Purchased and Installed Cost of Some Equipment 663