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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 Pittsburgh, PA 15213 this book contain: 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< 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 http://rapidshare.com/files/57171627/UNIT_OPERATIONS_OF_CHEMICAL_ENGINEERING.pdf_tsid_20070921-040229-442de61d [ Last edited by darliu on 2007-9-22 at 21:40 ] |
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