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COURSE INTRODUCTION
CHAPTER 2. HEAT EXCHANGE EQUIPMENT
DOUBLE-PIPE HXER
SHELL-AND-TUBE HXER
CHAPTER 3. FUNDAMENTALS OF HEAT TRANSFER
DOUBLE-PIPE HXER
SHELL-AND-TUBE HXER
CHAPTER 3. FUNDAMENTALS OF HEAT TRANSFER: REVIEW
LOG-MEAN D1UVNG FORCE
RESISTANCES N SERIES
FOULNG FACTORS
CORRELATIONS TO ESTIMATE h’S
h for Turbulent Flow In Long Pipes
CHAPTER 4. SHELL-AND-TUBE HEAT EXCHANGERS
IDEAL B NARY MixmREs
XYANDTXYDL4GRAMS
NONIDEAL BEHAVIOR
CHAPTER 7. FLASH DISTILLATION
APPROXIMATE SOLUTION
Inverse Lever-Arm Rule on Txy Diagram
RIGOROUS SOLUTION
Inverse Lever-Arm Rule on Hxy Diagram
BATCH (DIFFERENTIAL) DISTILLATION
CHAPTER 8. MULTISTAGE OPERATIONS
COUNTER-CURRENT CASCADE
CHAPTER 9. EQUIPMENT FOR TRAY TOWERS
CHAPTER 10. PERFORMANCE OF A C-C CASCADE
ANALYSIS OF A C-C CASCADE
CONSTANT MOLAL OVERFLOW
A RECTIFYNG CASCADE
A STRIPPNG CASCADE
STEAM DISTILLATION
CHAPTER 11. MCCABE-THIELE METHOD
LOCATION OF FEED PLATE
CONVERGENCE OF OPERATNG LNE AND EQUILIBRIUM CURVE
CHOOSNG THE REFLUX RATIO
1) Existence of Rmin
2) Total Reflux: R—*cx gives Minimum Stages
CALCULATNG FLOWRATES AND CONDENSER/REBOILER HEAT DUTIES
ROLE OF Q-LNE
PLATE EFFICIENCY
DETERMNNG NUMBER OF REAL STAGES
CHAPTER 12. MULTI-COMPONENT DISTILLATION
PRODUCT DISTRIBUTION FOR A SHARP SPLIT
MNIMUM NUMBER OF TRAYS
MNIMUM REFLUX RATIO
Method]) Psuedo-Binaiy Method
Method 2) Underwood’s Method
NUMBER OF IDEAL PLATES AT OPERATNG REFLUX
Method]) Underwood’s method
Method 2) Gilliland correlation
Method 3) Rigorous Solution of MESH Equations
CHAPTER 13. COMPUTER SIMULATION OF DISTILLATION
SOME PRELIMNARY STEPS
LOADNG A FILE (PROBLEM)
PLOTTNG THE MCCABE-THIELE DIAGRAM
PRNTNGTHEGRAPHS
TESTNG THE MCCABE-THIELE METHOD
THE TEMPERATURE PROFILE
DEGREES OF FREEDOM
CHAPTER 14. GAS ABSORPTION/STRIPPING
EQUIPMENT FOR ABSORPTION/STRIPPING
A TYPICAL ABSORBER DESIGN PROBLEM
Solution Overview:
Detailed Solution:
EQUILIBRIUM CURVE
OPERATING LINE
Approx. #1: Only One Transferable Component
Approx. #2: Dilute Solution
INTERFACIAL MASS TRANSFER: REVIEW
Definitions of Transfer Coefficients
Determining the Interfacial Concentrations: (x,yj)
Equimolar Counter-Diffusion vs. Diffusion through Stagnant
HEIGHT OF A PACKED TOWER
TRANSFERUNIT
EVALUATION OFNTUS
Special Case: Ya<<j with concave downwardEC
ANALOGY WITH DOUBLE-PIPE HXER
RELATIONSHIPS AMONG Hox, H0, Hx AND HY
PRESSURE DROP IN PACK BEDS
TOWER DIAMETER
CHAPTER 15. MEMBRANE SEPARATION
EXAMPLES
Gases
Liquids
EQUIPMENT
SEPARATION OF GASES
Porous Membranes
Nonporous Polymer Membranes
EXAMPLE: PRODUCTION OF ENRICHED AIR
Stage Cut
CHAPTER 16. LIQUID-LIQUID EXTRACTION
EQUIPMENT
TRIANGLE DIAGRAMS
NOMENCLATURE
RECTANGULAR DIAGRAMS
FLASH MIXING OF TWO LIQUIDS
SINGLE-STAGE EXTRACTOR
MULTI-STAGE EXTRACTOR
DIFFERENCE-POINT METHOD
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