{"product_id":"petroleum-refining-design-and-applications-handbook-volume-3-mechanical-separations-distillation-packed-towers-liquid-liquid-extraction-process-safety-incidents-hardback-9781119794868","title":"Petroleum Refining Design and Applications Handbook, Volume 3; Mechanical Separations, Distillation, Packed Towers, Liquid-Liquid Extraction, Process Safety Incidents (Hardback) 9781119794868","description":"\u003cfont face=\"Georgia\"\u003e\r\n\u003cp\u003e\u003cfont size=\"6\"\u003ePetroleum Refining Design and Applications Handbook, Volume 3\u003c\/font\u003e\u003cbr\u003e\r\n\u003cfont size=\"5\"\u003eMechanical Separations, Distillation, Packed Towers, Liquid-Liquid Extraction, Process Safety Incidents\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\r\n\r\n\r\n\u003cp\u003e\u003cfont size=\"4\"\u003eA. Kayode Coker (Edited by), AK Coker (Author)\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003e9781119794868, Wiley\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003eHardback, published 1 September 2022\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003e1216 pages\u003cbr\u003e1 x 1 x 1 cm, 0.454 kg\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\r\n\r\n\r\n\r\n\u003cp align=\"justify\"\u003e\u003cstrong\u003e\u003cfont size=\"3\"\u003e\u003cb\u003ePETROLEUM REFINING\u003c\/b\u003e \u003cp\u003e\u003cb\u003eThe third volume of a multi-volume set of the most comprehensive and up-to-date coverage of the advances of petroleum refining designs and applications, written by one of the world’s most well-known process engineers, this is a must-have for any chemical, process, or petroleum engineer. \u003c\/b\u003e \u003c\/p\u003e\n\u003cp\u003eThis volume continues the most up-to-date and comprehensive coverage of the most significant and recent changes to petroleum refining, presenting the state-of-the-art to the engineer, scientist, or student.  \u003c\/p\u003e\n\u003cp\u003e This book provides the design of process equipment, such as vessels for the separation of two-phase and three-phase fluids, using Excel spreadsheets, and extensive process safety investigations of refinery incidents, distillation, distillation sequencing, and dividing wall columns. It also covers multicomponent distillation, packed towers, liquid-liquid extraction using UniSim design software, and process safety incidents involving these equipment items and pertinent industrial case studies.  \u003c\/p\u003e\n\u003cp\u003e Useful as a textbook, this is also an excellent, handy go-to reference for the veteran engineer, a volume no chemical or process engineering library should be without. Written by one of the world’s foremost authorities, this book sets the standard for the industry and is an integral part of the petroleum refining renaissance. It is truly a must-have for any practicing engineer or student in this area.  \u003c\/p\u003e\n\u003cp\u003e\u003cb\u003eThis groundbreaking new volume: \u003c\/b\u003e  \u003c\/p\u003e\n\u003cul\u003e\n\u003cli\u003eAssists engineers in rapidly analyzing problems and finding effective design methods and select mechanical specifications  \u003c\/li\u003e\n\u003cli\u003eProvides improved design manuals to methods and proven fundamentals of process design with related data and charts \u003c\/li\u003e \u003cli\u003eCovers a complete range of basic day–to–day petroleum refining operations topics with new materials on significant industry changes \u003c\/li\u003e \u003cli\u003eIncludes extensive Excel spreadsheets for the design of process vessels for mechanical separation of two-phase and three-phase fluids \u003c\/li\u003e \u003cli\u003eProvides UniSim ®-based case studies for enabling simulation of key processes outlined in the book \u003c\/li\u003e \u003cli\u003eHelps achieve optimum operations and process conditions and shows how to translate design fundamentals into mechanical equipment specifications \u003c\/li\u003e \u003cli\u003eHas a related website that includes computer applications along with spreadsheets and concise applied process design flow charts and process data sheets \u003c\/li\u003e \u003cli\u003eProvides various case studies of process safety incidents in refineries and means of mitigating these from investigations by the US Chemical Safety Board \u003c\/li\u003e \u003cli\u003eIncludes a vast Glossary of Petroleum and Technical Terminology \u003c\/li\u003e\n\u003c\/ul\u003e\u003c\/font\u003e\u003c\/strong\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003e\u003cp\u003ePreface xxii\u003c\/p\u003e \u003cp\u003eAcknowledgments xxiv\u003c\/p\u003e \u003cp\u003e\u003cb\u003e18 Mechanical Separations 1\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e18.1 Particle Size 1\u003c\/p\u003e \u003cp\u003e18.2 Preliminary Separator Selection 6\u003c\/p\u003e \u003cp\u003e18.3 Gravity Settlers 16\u003c\/p\u003e \u003cp\u003e18.4 Terminal Velocity 19\u003c\/p\u003e \u003cp\u003e18.5 Alternate Terminal Velocity Calculation 24\u003c\/p\u003e \u003cp\u003e18.6 American Petroleum Institute’s Oil Field Separators 28\u003c\/p\u003e \u003cp\u003e18.7 Liquid\/Liquid, Liquid\/Solid Gravity Separations, Decanters, and Sedimentation Equipment 28\u003c\/p\u003e \u003cp\u003e18.8 Horizontal Gravity Settlers or Decanters, Liquid\/Liquid 29\u003c\/p\u003e \u003cp\u003e18.9 Modified Method of Happel and Jordan 33\u003c\/p\u003e \u003cp\u003e18.10 Decanter 36\u003c\/p\u003e \u003cp\u003e18.11 Impingement Separators 42\u003c\/p\u003e \u003cp\u003e18.12 Centrifugal Separators 68\u003c\/p\u003e \u003cp\u003eReferences 246\u003c\/p\u003e \u003cp\u003e\u003cb\u003e19 Distillation 249\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e19.1 Distillation Process Performance 249\u003c\/p\u003e \u003cp\u003e19.2 Equilibrium Basic Considerations 252\u003c\/p\u003e \u003cp\u003e19.3 Vapor–Liquid Equilibria 253\u003c\/p\u003e \u003cp\u003e19.4 Activity Coefficients 262\u003c\/p\u003e \u003cp\u003e19.5 Excess Gibbs Energy—G\u003csup\u003eE\u003c\/sup\u003e 263\u003c\/p\u003e \u003cp\u003e19.6 K-Value 264\u003c\/p\u003e \u003cp\u003e19.7 Ideal Systems 266\u003c\/p\u003e \u003cp\u003e19.8 Henry’s Law 268\u003c\/p\u003e \u003cp\u003e19.9 K-Factor Hydrocarbon Equilibrium Charts 269\u003c\/p\u003e \u003cp\u003e19.10 Non-Ideal Systems 277\u003c\/p\u003e \u003cp\u003e19.11 Thermodynamic Simulation Software Programs 280\u003c\/p\u003e \u003cp\u003e19.12 Vapor Pressure 283\u003c\/p\u003e \u003cp\u003e19.13 Azeotropic Mixtures 296\u003c\/p\u003e \u003cp\u003e19.14 Bubble Point of Liquid Mixture 311\u003c\/p\u003e \u003cp\u003e19.15 Equilibrium Flash Computations 316\u003c\/p\u003e \u003cp\u003e19.16 Degrees of Freedom 325\u003c\/p\u003e \u003cp\u003e19.17 UniSim (Honeywell) Software 326\u003c\/p\u003e \u003cp\u003e19.18 Binary System Material Balance: Constant Molal Overflow Tray to Tray 333\u003c\/p\u003e \u003cp\u003e19.19 Determination of Distillation Operating Pressures 343\u003c\/p\u003e \u003cp\u003e19.20 Condenser Types From a Distillation Column 344\u003c\/p\u003e \u003cp\u003e19.21 Effect of Thermal Condition of Feed 348\u003c\/p\u003e \u003cp\u003e19.22 Effect of Total Reflux, Minimum Number of Plates in a Distillation Column 352\u003c\/p\u003e \u003cp\u003e19.23 Relative Volatility α Separating Factor in a Vapor–Liquid System 355\u003c\/p\u003e \u003cp\u003e19.24 Rapid Estimation of Relative Volatility 366\u003c\/p\u003e \u003cp\u003e19.25 Estimation of Relative Volatilities Under 1.25 (α \u0026lt; 125) by Ryan 367\u003c\/p\u003e \u003cp\u003e19.26 Estimation of Minimum Reflux Ratio: Infinite Plates 368\u003c\/p\u003e \u003cp\u003e19.27 Calculation of Number of Theoretical Trays at Actual Reflux 370\u003c\/p\u003e \u003cp\u003e19.28 Identification of “Pinch Conditions” on an x-y Diagram at High Pressure 373\u003c\/p\u003e \u003cp\u003e19.29 Distillation Column Design 376\u003c\/p\u003e \u003cp\u003e19.30 Simulation of a Fractionating Column 378\u003c\/p\u003e \u003cp\u003e19.31 Determination of Number of Theoretical Plates in Fractionating Columns by the Smoker Equations at Constant Relative Volatility (α = constant) 396\u003c\/p\u003e \u003cp\u003e19.32 The Jafarey, Douglas, and McAvoy Equation: Design and Control 401\u003c\/p\u003e \u003cp\u003e19.33 Number of Theoretical Trays at Actual Reflux 411\u003c\/p\u003e \u003cp\u003e19.34 Estimating Tray Efficiency in a Distillation Column 413\u003c\/p\u003e \u003cp\u003e19.35 Steam Distillation 422\u003c\/p\u003e \u003cp\u003e19.36 Distillation with Heat Balance of Component Mixture 432\u003c\/p\u003e \u003cp\u003e19.37 Multicomponent Distillation 453\u003c\/p\u003e \u003cp\u003e19.38 Scheibel–Montross Empirical: Adjacent Key Systems: Constant or Variable Volatility 494\u003c\/p\u003e \u003cp\u003e19.39 Minimum Number of Trays: Total Reflux−Constant Volatility 497\u003c\/p\u003e \u003cp\u003e19.40 Smith–Brinkley (SB) Method 512\u003c\/p\u003e \u003cp\u003e19.41 Retrofit Design of Distillation Columns 514\u003c\/p\u003e \u003cp\u003e19.42 Tray-by-Tray for Multicomponent Mixtures 517\u003c\/p\u003e \u003cp\u003e19.43 Tray-by-Tray Calculation of a Multicomponent Mixture Using a Digital Computer 531\u003c\/p\u003e \u003cp\u003e19.44 Thermal Condition of Feed 532\u003c\/p\u003e \u003cp\u003e19.45 Minimum Reflux-Underwood Method, Determination of α\u003csub\u003eAvg\u003c\/sub\u003e for Multicomponent Mixture 533\u003c\/p\u003e \u003cp\u003e19.46 Heat Balance-Adjacent Key Systems with Sharp Separations, Constant Molal Overflow 539\u003c\/p\u003e \u003cp\u003e19.47 Stripping Volatile Organic Chemicals (VOC) from Water with Air 542\u003c\/p\u003e \u003cp\u003e19.48 Rigorous Plate-to-Plate Calculation (Sorel Method) 547\u003c\/p\u003e \u003cp\u003e19.49 Multiple Feeds and Side Streams for a Binary Mixture 551\u003c\/p\u003e \u003cp\u003e19.50 Chou and Yaws Method 558\u003c\/p\u003e \u003cp\u003e19.51 Optimum Reflux Ratio and Optimum Number of Trays Calculations 561\u003c\/p\u003e \u003cp\u003e19.52 Tower Sizing for Valve Trays 574\u003c\/p\u003e \u003cp\u003e19.53 Troubleshooting, Predictive Maintenance, and Controls for Distillation Columns 589\u003c\/p\u003e \u003cp\u003e19.54 Distillation Sequencing with Columns Having More than Two Products 622\u003c\/p\u003e \u003cp\u003e19.55 Heat Integration of Distillation Columns 630\u003c\/p\u003e \u003cp\u003e19.56 Capital Cost Considerations for Distillation Columns 634\u003c\/p\u003e \u003cp\u003e19.57 The Pinch Design Approach to Inventing a Network 644\u003c\/p\u003e \u003cp\u003e19.58 Appropriate Placement and Integration of Distillation Columns 644\u003c\/p\u003e \u003cp\u003e19.59 Heat Integration of Distillation Columns: Summary 645\u003c\/p\u003e \u003cp\u003e19.60 Common Installation Errors in Distillation Columns 645\u003c\/p\u003e \u003cp\u003eReferences 693\u003c\/p\u003e \u003cp\u003eBibliography 699\u003c\/p\u003e \u003cp\u003e\u003cb\u003e20 Packed Towers and Liquid–Liquid Extraction 703\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e20.1 Shell 707\u003c\/p\u003e \u003cp\u003e20.2 Random Packing 708\u003c\/p\u003e \u003cp\u003e20.3 Packing Supports 709\u003c\/p\u003e \u003cp\u003e20.4 Liquid Distribution 734\u003c\/p\u003e \u003cp\u003e20.5 Packing Installation 739\u003c\/p\u003e \u003cp\u003e20.6 Contacting Efficiency, Expressed as K\u003csub\u003ega\u003c\/sub\u003e, HTU, HETP 755\u003c\/p\u003e \u003cp\u003e20.7 Packing Size 756\u003c\/p\u003e \u003cp\u003e20.8 Pressure Drop 757\u003c\/p\u003e \u003cp\u003e20.9 Materials of Construction 759\u003c\/p\u003e \u003cp\u003e20.10 Particle versus Compact Preformed Structured Packings 759\u003c\/p\u003e \u003cp\u003e20.11 Minimum Liquid Wetting Rates 760\u003c\/p\u003e \u003cp\u003e20.12 Loading Point Loading Region 761\u003c\/p\u003e \u003cp\u003e20.13 Flooding Point 772\u003c\/p\u003e \u003cp\u003e20.14 Foaming Liquid Systems 773\u003c\/p\u003e \u003cp\u003e20.15 Surface Tension Effects 773\u003c\/p\u003e \u003cp\u003e20.16 Packing Factors 773\u003c\/p\u003e \u003cp\u003e20.17 Recommended Design Capacity and Pressure Drop 776\u003c\/p\u003e \u003cp\u003e20.18 Pressure Drop Design Criteria and Guide: Random Packings Only 778\u003c\/p\u003e \u003cp\u003e20.19 Effects of Physical Properties 781\u003c\/p\u003e \u003cp\u003e20.20 Performance Comparisons 784\u003c\/p\u003e \u003cp\u003e20.21 Capacity Basis for Design 784\u003c\/p\u003e \u003cp\u003e20.22 Proprietary Random Packing Design Guides 796\u003c\/p\u003e \u003cp\u003e20.23 Liquid Hold-Up 822\u003c\/p\u003e \u003cp\u003e20.24 Packing Wetted Area 824\u003c\/p\u003e \u003cp\u003e20.25 Effective Interfacial Area 826\u003c\/p\u003e \u003cp\u003e20.26 Entrainment from Packing Surface 827\u003c\/p\u003e \u003cp\u003e20.27 Structured Packing 830\u003c\/p\u003e \u003cp\u003e20.28 Structured Packing: Technical Performance Features 849\u003c\/p\u003e \u003cp\u003e20.29 New Generalized Pressure Drop Correlation Charts 855\u003c\/p\u003e \u003cp\u003e20.30 Mass and Heat Transfer in Packed Tower 855\u003c\/p\u003e \u003cp\u003e20.31 Number of Transfer Units, N\u003csub\u003eOG\u003c\/sub\u003e, N\u003csub\u003eOL\u003c\/sub\u003e 856\u003c\/p\u003e \u003cp\u003e20.32 Gas and Liquid-Phase Coefficients, k\u003csub\u003eG\u003c\/sub\u003e and k\u003csub\u003eL\u003c\/sub\u003e 868\u003c\/p\u003e \u003cp\u003e20.33 Height of a Transfer Unit, H\u003csub\u003eOG\u003c\/sub\u003e, H\u003csub\u003eOL\u003c\/sub\u003e, HTU 869\u003c\/p\u003e \u003cp\u003e20.34 Distillation in Packed Towers 874\u003c\/p\u003e \u003cp\u003e20.35 Liquid–Liquid Extraction 893\u003c\/p\u003e \u003cp\u003e20.36 Process Parameters 908\u003c\/p\u003e \u003cp\u003e20.37 Solvents Selection for the Extraction Unit 911\u003c\/p\u003e \u003cp\u003e20.38 Phenol Extraction Process of Lubes 913\u003c\/p\u003e \u003cp\u003e20.39 Furfural Extraction Process 914\u003c\/p\u003e \u003cp\u003e20.40 Dispersed-Phase Droplet Size 916\u003c\/p\u003e \u003cp\u003e20.41 Theory 920\u003c\/p\u003e \u003cp\u003e20.42 Nernst’s Distribution Law 921\u003c\/p\u003e \u003cp\u003e20.43 Tie Lines 921\u003c\/p\u003e \u003cp\u003e20.44 Phase Diagrams 929\u003c\/p\u003e \u003cp\u003e20.45 Countercurrent Extractors 931\u003c\/p\u003e \u003cp\u003e20.46 Extraction Equipment 935\u003c\/p\u003e \u003cp\u003eReferences 956\u003c\/p\u003e \u003cp\u003eGlossary 961\u003c\/p\u003e \u003cp\u003eAppendix D 1087\u003c\/p\u003e \u003cp\u003eAppendix F 1163\u003c\/p\u003e \u003cp\u003eAbout the Author 1179\u003c\/p\u003e \u003cp\u003eIndex 1181\u003c\/p\u003e\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003eSubject Areas: Energy technology \u0026amp; engineering [\u003ca title=\"See our other books on Energy technology \u0026amp; engineering\" href=\"https:\/\/freshlyprintedbooks.co.uk\/search?q=%22Energy%20technology%20\u0026amp;%20engineering%20%5BTH%5D%22\"\u003eTH\u003c\/a\u003e]\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\r\n\u003c\/font\u003e","brand":"Wiley-Scrivener","offers":[{"title":"Brand New","offer_id":52430965932312,"sku":"9781119794868","price":181.88,"currency_code":"GBP","in_stock":true}],"thumbnail_url":"\/\/cdn.shopify.com\/s\/files\/1\/0730\/2037\/5320\/files\/9781119794868.jpg?v=1784766496","url":"https:\/\/freshlyprintedbooks.co.uk\/products\/petroleum-refining-design-and-applications-handbook-volume-3-mechanical-separations-distillation-packed-towers-liquid-liquid-extraction-process-safety-incidents-hardback-9781119794868","provider":"Freshly Printed Books","version":"1.0","type":"link"}