Unit Operations of Chemical Engineering

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Unit Operations of Chemical Engineering​

by Dennis C. Prieve​

Department of Chemical Engineering
Carnegie Mellon University​

لینک دانلود:​

http://rapidshare.com/files/1112907...Taghdim_be_aezaye_mohtarame_Iran-eng.com_.zip​

مباحثی هم که بصورت مختصر و مفید داخلش اومده عبارت است از:​

COURSE INTRODUCTION​

CHAPTER 2. HEAT EQUIPMENT​

DOUBLE-PIPE HXER​

SHELL-AND-TUBE HXER​

CHAPTER 3. FUNDAMENTALS OF​

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​

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. COMUTER 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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Unit Operations of Chemical Engineering

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