{"product_id":"chemical-process-engineering-volume-1-design-analysis-simulation-integration-and-problem-solving-with-microsoft-excel-unisim-software-for-chemical-engineers-computation-physical-property-fluid-flow-equipment-and-instrumen-hardback-9781119510185","title":"Chemical Process Engineering Volume 1; Design, Analysis, Simulation, Integration, and Problem Solving with Microsoft Excel-UniSim Software for Chemical Engineers Computation, Physical Property, Fluid Flow, Equipment and Instrumen… (Hardback) 9781119510185","description":"\u003cfont face=\"Georgia\"\u003e\r\n\u003cp\u003e\u003cfont size=\"6\"\u003eChemical Process Engineering Volume 1\u003c\/font\u003e\u003cbr\u003e\r\n\u003cfont size=\"5\"\u003eDesign, Analysis, Simulation, Integration, and Problem Solving with Microsoft Excel-UniSim Software for Chemical Engineers Computation, Physical Property, Fluid Flow, Equipment and Instrument Sizing\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\r\n\r\n\r\n\u003cp\u003e\u003cfont size=\"4\"\u003eRahmat Sotudeh-Gharebagh (Author), A. Kayode Coker (Author)\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003e9781119510185, Wiley\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003eHardback, published 17 May 2022\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003e544 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\u003cp\u003e\u003cb\u003eWritten by two of the most prolific and respected chemical engineers in the world, this groundbreaking two-volume set is the “new standard” in the industry, offering engineers and students alike the most up-do-date, comprehensive, and state-of-the-art coverage of processes and best practices in the field today. \u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eThis first new volume in a two-volume set explores and describes integrating new tools for engineering education and practice for better utilization of the existing knowledge on process design. Useful not only for students, professors, scientists and practitioners, especially process, chemical, mechanical and metallurgical engineers, it is also a valuable reference for other engineers, consultants, technicians and scientists concerned about various aspects of industrial design.\u003c\/p\u003e \u003cp\u003eThe text can be considered as a complementary text to process design for senior and graduate students as well as a hands-on reference work or refresher for engineers at entry level. The contents of the book can also be taught in intensive workshops in the oil, gas, petrochemical, biochemical and process industries.\u003c\/p\u003e \u003cp\u003eThe book provides a detailed description and hands-on experience on process design in chemical engineering, and it is an integrated text that focuses on practical design with new tools, such as Excel spreadsheets and UniSim simulation software.\u003c\/p\u003e \u003cp\u003eWritten by two industry and university’s most trustworthy and well-known authors, this book is the new standard in chemical, biochemical, pharmaceutical, petrochemical and petroleum refining. Covering design, analysis, simulation, integration, and, perhaps most importantly, the practical application of Microsoft Excel-UniSim software, this is the most comprehensive and up-to-date coverage of all of the latest developments in the industry. It is a must-have for any engineer or student’s library.\u003c\/p\u003e\u003c\/font\u003e\u003c\/strong\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003e\u003cp\u003ePreface xvii\u003c\/p\u003e \u003cp\u003eAcknowledgments xix\u003c\/p\u003e \u003cp\u003eAbout the Authors xxi\u003c\/p\u003e \u003cp\u003e\u003cb\u003e1 Computations with Excel Spreadsheet-UniSim Design Simulation 1\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eSection I - Numerical Analysis 1\u003c\/p\u003e \u003cp\u003eIntroduction 1\u003c\/p\u003e \u003cp\u003eExcel Spreadsheet 1\u003c\/p\u003e \u003cp\u003eFunctions 2\u003c\/p\u003e \u003cp\u003eTrendline Coefficients 2\u003c\/p\u003e \u003cp\u003eGoal Seek 5\u003c\/p\u003e \u003cp\u003eSolver 6\u003c\/p\u003e \u003cp\u003eLinear Regression 7\u003c\/p\u003e \u003cp\u003eMeasuring Regression Quality 9\u003c\/p\u003e \u003cp\u003eMultiple Regression 9\u003c\/p\u003e \u003cp\u003ePolynomial Regression 11\u003c\/p\u003e \u003cp\u003eSimultaneous Linear Equations 11\u003c\/p\u003e \u003cp\u003eNonlinear Equations 12\u003c\/p\u003e \u003cp\u003eInterpolations 13\u003c\/p\u003e \u003cp\u003eIntegrations 14\u003c\/p\u003e \u003cp\u003eThe Trapezoidal Rule 14\u003c\/p\u003e \u003cp\u003eSimpson’s 1\/3 Rule 15\u003c\/p\u003e \u003cp\u003eSimpson’s 3\/8 Rule 15\u003c\/p\u003e \u003cp\u003eDifferential Equations 15\u003c\/p\u003e \u003cp\u003eN\u003csup\u003eth\u003c\/sup\u003e Order Ordinary Differential Equations 15\u003c\/p\u003e \u003cp\u003eSolution of First-Order Ordinary Differential Equations 15\u003c\/p\u003e \u003cp\u003eRunge-Kutta Methods 16\u003c\/p\u003e \u003cp\u003eExamples and Solutions 17\u003c\/p\u003e \u003cp\u003eSection II – Process Simulation 28\u003c\/p\u003e \u003cp\u003eIntroduction 28\u003c\/p\u003e \u003cp\u003eThermodynamics for Process Simulators 29\u003c\/p\u003e \u003cp\u003eUNISIM Design Software 30\u003c\/p\u003e \u003cp\u003eExamples and Solutions 31\u003c\/p\u003e \u003cp\u003eReferences 78\u003c\/p\u003e \u003cp\u003e\u003cb\u003e2 Physical Property of Pure Components and Mixtures 81\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003ePure Components 81\u003c\/p\u003e \u003cp\u003eDensity of Liquid 82\u003c\/p\u003e \u003cp\u003eViscosity of Liquid 83\u003c\/p\u003e \u003cp\u003eHeat Capacity of Liquid 85\u003c\/p\u003e \u003cp\u003eThermal Conductivity of Liquid 87\u003c\/p\u003e \u003cp\u003eVolumetric Expansion Rate 90\u003c\/p\u003e \u003cp\u003eVapor Pressure 91\u003c\/p\u003e \u003cp\u003eViscosity of Gas 93\u003c\/p\u003e \u003cp\u003eThermal Conductivity of Gas 94\u003c\/p\u003e \u003cp\u003eHeat Capacity of Gases 95\u003c\/p\u003e \u003cp\u003eMixtures 97\u003c\/p\u003e \u003cp\u003eSurface Tensions 98\u003c\/p\u003e \u003cp\u003eViscosity of Gas Mixture 99\u003c\/p\u003e \u003cp\u003eEnthalpy of Formation 101\u003c\/p\u003e \u003cp\u003eEnthalpy of Vaporization 103\u003c\/p\u003e \u003cp\u003eGibbs Energy of Reaction 105\u003c\/p\u003e \u003cp\u003eHenry’s Law Constant for Gases in Water 107\u003c\/p\u003e \u003cp\u003eCoefficient of Thermal Expansion of Liquid 108\u003c\/p\u003e \u003cp\u003eDiffusion Coefficients 109\u003c\/p\u003e \u003cp\u003eGas-Phase Diffusion Coefficients 109\u003c\/p\u003e \u003cp\u003eLiquid-Phase Diffusion Coefficients 110\u003c\/p\u003e \u003cp\u003eCompressibility Z-factor 111\u003c\/p\u003e \u003cp\u003eSolubility and Adsorption 116\u003c\/p\u003e \u003cp\u003eSolubility of Hydrocarbons in Water 116\u003c\/p\u003e \u003cp\u003eSolubility of Gases in Water 117\u003c\/p\u003e \u003cp\u003eSolubility of Sulfur and Nitrogen Compounds in Water 118\u003c\/p\u003e \u003cp\u003eAdsorption on Activated Carbon 119\u003c\/p\u003e \u003cp\u003eReferences 119\u003c\/p\u003e \u003cp\u003e\u003cb\u003e3 Fluid Flow 121\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eIntroduction 121\u003c\/p\u003e \u003cp\u003eFlow of Fluids in Pipes 121\u003c\/p\u003e \u003cp\u003eEquivalent Length of Various Fittings and Valves 123\u003c\/p\u003e \u003cp\u003eExcess Head Loss 123\u003c\/p\u003e \u003cp\u003ePipe Reduction and Enlargement 124\u003c\/p\u003e \u003cp\u003ePressure Drop Calculations for Single-phase Incompressible Fluids 124\u003c\/p\u003e \u003cp\u003eFriction Factor 127\u003c\/p\u003e \u003cp\u003eOverall Pressure Drop 128\u003c\/p\u003e \u003cp\u003eNomenclature 130\u003c\/p\u003e \u003cp\u003eCompressible Fluid Flow in Pipes 130\u003c\/p\u003e \u003cp\u003eMaximum Flow and Pressure Drop 131\u003c\/p\u003e \u003cp\u003eCritical or Sonic Flow and the Mach Number 131\u003c\/p\u003e \u003cp\u003eMach Number 132\u003c\/p\u003e \u003cp\u003eMathematical Model of Compressible Isothermal Flow 134\u003c\/p\u003e \u003cp\u003eFlow Rate Through Pipeline 136\u003c\/p\u003e \u003cp\u003ePipeline Pressure Drop 138\u003c\/p\u003e \u003cp\u003eNomenclature 139\u003c\/p\u003e \u003cp\u003eSubscripts 139\u003c\/p\u003e \u003cp\u003eTwo-phase Flow in Process Piping 139\u003c\/p\u003e \u003cp\u003eFlow Patterns 140\u003c\/p\u003e \u003cp\u003eFlow Regimes 142\u003c\/p\u003e \u003cp\u003ePressure Drop 142\u003c\/p\u003e \u003cp\u003eErosion-Corrosion 145\u003c\/p\u003e \u003cp\u003eNomenclature 145\u003c\/p\u003e \u003cp\u003eVapor-liquid Two-phase Vertical Downflow 146\u003c\/p\u003e \u003cp\u003eThe Equations 147\u003c\/p\u003e \u003cp\u003eThe Algorithm 147\u003c\/p\u003e \u003cp\u003eNomenclature 147\u003c\/p\u003e \u003cp\u003eLine Sizes for Flashing Steam Condensate 148\u003c\/p\u003e \u003cp\u003eThe Equations 148\u003c\/p\u003e \u003cp\u003eNomenclature 149\u003c\/p\u003e \u003cp\u003eFlow Through Packed Beds 150\u003c\/p\u003e \u003cp\u003eThe Equations 151\u003c\/p\u003e \u003cp\u003eNomenclature 152\u003c\/p\u003e \u003cp\u003eExamples and Solutions 152\u003c\/p\u003e \u003cp\u003eReferences 162\u003c\/p\u003e \u003cp\u003e\u003cb\u003e4 Equipment Sizing 165\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eIntroduction 165\u003c\/p\u003e \u003cp\u003eSizing of Vertical and Horizontal Separators 166\u003c\/p\u003e \u003cp\u003eVertical Separators 166\u003c\/p\u003e \u003cp\u003eCalculation Method for a Vertical Drum 168\u003c\/p\u003e \u003cp\u003eCalculation Method for a Horizontal Drum 170\u003c\/p\u003e \u003cp\u003eLiquid Holdup and Vapor Space Disengagement 171\u003c\/p\u003e \u003cp\u003eWire Mesh Pad 171\u003c\/p\u003e \u003cp\u003eStandards for Horizontal Separators 172\u003c\/p\u003e \u003cp\u003ePiping Requirements 172\u003c\/p\u003e \u003cp\u003eNomenclature 172\u003c\/p\u003e \u003cp\u003eSizing of Partly Filled Vessels and Tanks 173\u003c\/p\u003e \u003cp\u003eThe Equations 173\u003c\/p\u003e \u003cp\u003eNomenclature 175\u003c\/p\u003e \u003cp\u003ePreliminary Vessel Design 176\u003c\/p\u003e \u003cp\u003eNomenclature 177\u003c\/p\u003e \u003cp\u003eCyclone Design 178\u003c\/p\u003e \u003cp\u003eIntroduction 178\u003c\/p\u003e \u003cp\u003eCyclone Design Procedure 178\u003c\/p\u003e \u003cp\u003eThe Equations 179\u003c\/p\u003e \u003cp\u003eSaltation Velocity 180\u003c\/p\u003e \u003cp\u003ePressure Drop 181\u003c\/p\u003e \u003cp\u003eTroubleshooting Cyclone Maloperations 182\u003c\/p\u003e \u003cp\u003eCyclone Collection Efficiency 182\u003c\/p\u003e \u003cp\u003eCyclone Design Factor 182\u003c\/p\u003e \u003cp\u003eCyclone Design Procedure 183\u003c\/p\u003e \u003cp\u003eNomenclature 183\u003c\/p\u003e \u003cp\u003eGas Dryer Design 184\u003c\/p\u003e \u003cp\u003eThe Equations 186\u003c\/p\u003e \u003cp\u003ePressure Drop 187\u003c\/p\u003e \u003cp\u003eDesiccant Reactivation 188\u003c\/p\u003e \u003cp\u003eNomenclature 188\u003c\/p\u003e \u003cp\u003eExamples and Solutions 189\u003c\/p\u003e \u003cp\u003eReferences 194\u003c\/p\u003e \u003cp\u003e\u003cb\u003e5 Instrument Sizing 195\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eIntroduction 195\u003c\/p\u003e \u003cp\u003eVariable-Head Meters 195\u003c\/p\u003e \u003cp\u003eMacroscopic Mechanical Energy Balance 196\u003c\/p\u003e \u003cp\u003eVariable-Head Meters 196\u003c\/p\u003e \u003cp\u003eOrifice Sizing for Liquid and Gas Flows 200\u003c\/p\u003e \u003cp\u003eOrifice Sizing for Liquid Flows 201\u003c\/p\u003e \u003cp\u003eOrifice Sizing for Gas Flows 202\u003c\/p\u003e \u003cp\u003eOrifice Sizing for Liquid Flow 204\u003c\/p\u003e \u003cp\u003eOrifice Sizing for Gas Flow 204\u003c\/p\u003e \u003cp\u003eTypes of Restriction Orifice Plates 205\u003c\/p\u003e \u003cp\u003eCase Study 1 205\u003c\/p\u003e \u003cp\u003eNomenclature 212\u003c\/p\u003e \u003cp\u003eControl Valve Sizing 221\u003c\/p\u003e \u003cp\u003eIntroduction 221\u003c\/p\u003e \u003cp\u003eControl Valve Characteristics 223\u003c\/p\u003e \u003cp\u003ePressure Drop for Sizing 224\u003c\/p\u003e \u003cp\u003eChoked Flow 224\u003c\/p\u003e \u003cp\u003eFlashing and Cavitation 224\u003c\/p\u003e \u003cp\u003eControl Valve Sizing for Liquid, Gas, Steam and Two-Phase Flows 225\u003c\/p\u003e \u003cp\u003eLiquid Sizing 226\u003c\/p\u003e \u003cp\u003eGas Sizing 227\u003c\/p\u003e \u003cp\u003eCritical Condition 227\u003c\/p\u003e \u003cp\u003eSteam Sizing 227\u003c\/p\u003e \u003cp\u003eTwo-Phase Flow 228\u003c\/p\u003e \u003cp\u003eInstallation 229\u003c\/p\u003e \u003cp\u003eNoise 229\u003c\/p\u003e \u003cp\u003eControl Valve Sizing Criteria 230\u003c\/p\u003e \u003cp\u003eValve Sizing Criteria 230\u003c\/p\u003e \u003cp\u003eSelf-Acting Regulators 231\u003c\/p\u003e \u003cp\u003eTypes of Self-Acting Regulators 231\u003c\/p\u003e \u003cp\u003eCase Study 2 233\u003c\/p\u003e \u003cp\u003eRules of Thumb 246\u003c\/p\u003e \u003cp\u003eNomenclature 246\u003c\/p\u003e \u003cp\u003eReferences 247\u003c\/p\u003e \u003cp\u003e\u003cb\u003e6 Pumps and Compressors Sizing 249\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003ePumps 249\u003c\/p\u003e \u003cp\u003eIntroduction 249\u003c\/p\u003e \u003cp\u003ePumping of Liquids 249\u003c\/p\u003e \u003cp\u003ePump Design Standardization 252\u003c\/p\u003e \u003cp\u003eBasic Parts of a Centrifugal Pump 253\u003c\/p\u003e \u003cp\u003eImpellers 253\u003c\/p\u003e \u003cp\u003eCasing 253\u003c\/p\u003e \u003cp\u003eShaft 254\u003c\/p\u003e \u003cp\u003eCentrifugal Pump Selection 255\u003c\/p\u003e \u003cp\u003eSingle-Stage (Single Impeller) Pumps 256\u003c\/p\u003e \u003cp\u003eHydraulic Characteristics for Centrifugal Pumps 260\u003c\/p\u003e \u003cp\u003eFriction Losses Due to Flow 269\u003c\/p\u003e \u003cp\u003eVelocity Head 269\u003c\/p\u003e \u003cp\u003eFriction 271\u003c\/p\u003e \u003cp\u003eNet Positive Suction Head (npsh) and Pump Suction 271\u003c\/p\u003e \u003cp\u003eGeneral Suction System 277\u003c\/p\u003e \u003cp\u003eReductions in NPSH\u003csub\u003eR\u003c\/sub\u003e 279\u003c\/p\u003e \u003cp\u003eCorrections to NPSH\u003csub\u003eR\u003c\/sub\u003e for Hot Liquid Hydrocarbons and Water 279\u003c\/p\u003e \u003cp\u003eCharting NPSH\u003csub\u003eR\u003c\/sub\u003e Values of Pumps 280\u003c\/p\u003e \u003cp\u003eNet Positive Suction Head (NPSH) 280\u003c\/p\u003e \u003cp\u003eSpecific Speed 282\u003c\/p\u003e \u003cp\u003e“Type Specific Speed” 285\u003c\/p\u003e \u003cp\u003eRotative Speed 286\u003c\/p\u003e \u003cp\u003ePumping Systems and Performance 286\u003c\/p\u003e \u003cp\u003eSystem Head Using Two Different Pipe Sizes in Same Line 288\u003c\/p\u003e \u003cp\u003ePower Requirements for Pumping Through Process Lines 291\u003c\/p\u003e \u003cp\u003eHydraulic Power 292\u003c\/p\u003e \u003cp\u003eRelations Between Head, Horsepower, Capacity, Speed 293\u003c\/p\u003e \u003cp\u003eBrake Horsepower (BHP) Input at Pump 293\u003c\/p\u003e \u003cp\u003eAffinity Laws 296\u003c\/p\u003e \u003cp\u003ePump Parameters 298\u003c\/p\u003e \u003cp\u003eSpecific Speed, Flowrate and Power Required by a Pump 299\u003c\/p\u003e \u003cp\u003ePump Sizing of Gas-Oil 301\u003c\/p\u003e \u003cp\u003eDebutanizer Unit 303\u003c\/p\u003e \u003cp\u003eCentrifugal Pump Efficiency 306\u003c\/p\u003e \u003cp\u003eCentrifugal Pump Specifications 311\u003c\/p\u003e \u003cp\u003ePump Specifications 311\u003c\/p\u003e \u003cp\u003eSteps in Pump Sizing 312\u003c\/p\u003e \u003cp\u003eReciprocating Pumps 313\u003c\/p\u003e \u003cp\u003eSignificant Features in Reciprocating Pump Arrangements 314\u003c\/p\u003e \u003cp\u003eApplication 316\u003c\/p\u003e \u003cp\u003ePerformance 316\u003c\/p\u003e \u003cp\u003eDischarge Flow Patterns 317\u003c\/p\u003e \u003cp\u003eHorsepower 318\u003c\/p\u003e \u003cp\u003ePump Selection 318\u003c\/p\u003e \u003cp\u003eSelection Rules-of-Thumb 318\u003c\/p\u003e \u003cp\u003eA Case Study 321\u003c\/p\u003e \u003cp\u003ePump Simulation on a PFD 321\u003c\/p\u003e \u003cp\u003eVariables Descriptions 322\u003c\/p\u003e \u003cp\u003eSimulation Algorithm 322\u003c\/p\u003e \u003cp\u003eProblem 323\u003c\/p\u003e \u003cp\u003eDiscussion 324\u003c\/p\u003e \u003cp\u003ePump Cavitation 332\u003c\/p\u003e \u003cp\u003eFactors in Pump Selection 333\u003c\/p\u003e \u003cp\u003eCompressors 334\u003c\/p\u003e \u003cp\u003eIntroduction 334\u003c\/p\u003e \u003cp\u003eGeneral Application Guide 334\u003c\/p\u003e \u003cp\u003eSpecification Guides 337\u003c\/p\u003e \u003cp\u003eGeneral Considerations for Any Type of Compressor Flow Conditions 337\u003c\/p\u003e \u003cp\u003eFluid Properties 338\u003c\/p\u003e \u003cp\u003eCompressibility 338\u003c\/p\u003e \u003cp\u003eCorrosive Nature 338\u003c\/p\u003e \u003cp\u003eMoisture 339\u003c\/p\u003e \u003cp\u003eSpecial Conditions 339\u003c\/p\u003e \u003cp\u003eSpecification Sheet 339\u003c\/p\u003e \u003cp\u003ePerformance Considerations 339\u003c\/p\u003e \u003cp\u003eCooling Water to Cylinder Jackets 339\u003c\/p\u003e \u003cp\u003eHeat Rejected to Water 339\u003c\/p\u003e \u003cp\u003eDrivers 340\u003c\/p\u003e \u003cp\u003eIdeal Pressure – Volume Relationship 341\u003c\/p\u003e \u003cp\u003eActual Compressor Diagram 343\u003c\/p\u003e \u003cp\u003eDeviations From Ideal Gas Laws: Compressibility 343\u003c\/p\u003e \u003cp\u003eAdiabatic Calculations 346\u003c\/p\u003e \u003cp\u003eCharles’ Law at Constant Pressure 346\u003c\/p\u003e \u003cp\u003eAmonton’s Law at Constant Volume 346\u003c\/p\u003e \u003cp\u003eCombined Boyle’s and Charles’ Laws 346\u003c\/p\u003e \u003cp\u003eEntropy Balance Method 347\u003c\/p\u003e \u003cp\u003eIsentropic Exponent Method 347\u003c\/p\u003e \u003cp\u003eCompression Ratio 354\u003c\/p\u003e \u003cp\u003eHorsepower 356\u003c\/p\u003e \u003cp\u003eSingle Stage 356\u003c\/p\u003e \u003cp\u003eTheoretical H\u003csub\u003ep\u003c\/sub\u003e 356\u003c\/p\u003e \u003cp\u003eActual Brake Horsepower, Bhp 356\u003c\/p\u003e \u003cp\u003eActual Brake Horsepower, Bhp (Alternate Correction for Compressibility) 361\u003c\/p\u003e \u003cp\u003eTemperature Rise – Adiabatic 363\u003c\/p\u003e \u003cp\u003eTemperature Rise – Polytropic 365\u003c\/p\u003e \u003cp\u003eA Case Study Using Unisim Design R460.1 Software for a Two–stage Compression 365\u003c\/p\u003e \u003cp\u003eCase Study 2 365\u003c\/p\u003e \u003cp\u003eSolution 365\u003c\/p\u003e \u003cp\u003e1. Starting UniSim Design Software 366\u003c\/p\u003e \u003cp\u003e2. Creating a New Simulation 366\u003c\/p\u003e \u003cp\u003eSaving the Simulation 367\u003c\/p\u003e \u003cp\u003e3. Adding Components to the Simulation 367\u003c\/p\u003e \u003cp\u003e4. Selecting a Fluids Package 368\u003c\/p\u003e \u003cp\u003e5. Select the Units for the Simulation 369\u003c\/p\u003e \u003cp\u003e6. Enter Simulation Environment 369\u003c\/p\u003e \u003cp\u003eAccidentally Closing the PFD 371\u003c\/p\u003e \u003cp\u003eObject Palette 371\u003c\/p\u003e \u003cp\u003e7. Adding Material Streams 371\u003c\/p\u003e \u003cp\u003e8. Specifying Material Streams 372\u003c\/p\u003e \u003cp\u003e9. Adding A Compressor 374\u003c\/p\u003e \u003cp\u003eSpecifications 381\u003c\/p\u003e \u003cp\u003eCompression Process 385\u003c\/p\u003e \u003cp\u003eAdiabatic 385\u003c\/p\u003e \u003cp\u003eIsothermal 385\u003c\/p\u003e \u003cp\u003ePolytropic 385\u003c\/p\u003e \u003cp\u003eEfficiency 388\u003c\/p\u003e \u003cp\u003eHead 390\u003c\/p\u003e \u003cp\u003eAdiabatic Head Developed Per Single-stage Wheel 390\u003c\/p\u003e \u003cp\u003ePolytropic Head 391\u003c\/p\u003e \u003cp\u003ePolytropic 391\u003c\/p\u003e \u003cp\u003eBrake Horsepower 393\u003c\/p\u003e \u003cp\u003eSpeed of Rotation 396\u003c\/p\u003e \u003cp\u003eTemperature Rise During Compression 397\u003c\/p\u003e \u003cp\u003eSonic or Acoustic Velocity 399\u003c\/p\u003e \u003cp\u003eMach Number 402\u003c\/p\u003e \u003cp\u003eSpecific Speed 402\u003c\/p\u003e \u003cp\u003eCompressor Equations in Si Units 403\u003c\/p\u003e \u003cp\u003ePolytropic Compressor 405\u003c\/p\u003e \u003cp\u003eAdiabatic Compressor 408\u003c\/p\u003e \u003cp\u003eEfficiency 409\u003c\/p\u003e \u003cp\u003eMass Flow Rate, w 409\u003c\/p\u003e \u003cp\u003eMechanical Losses 410\u003c\/p\u003e \u003cp\u003eEstimating Compressor Horsepower 411\u003c\/p\u003e \u003cp\u003eMultistage Compressors 412\u003c\/p\u003e \u003cp\u003eMulticomponent Gas Streams 414\u003c\/p\u003e \u003cp\u003eAffinity Laws 422\u003c\/p\u003e \u003cp\u003eSpeed 423\u003c\/p\u003e \u003cp\u003eImpeller Diameters (Similar) 423\u003c\/p\u003e \u003cp\u003eImpeller Diameter (Changed) 424\u003c\/p\u003e \u003cp\u003eEffect of Temperature 424\u003c\/p\u003e \u003cp\u003eAffinity Law Performance 425\u003c\/p\u003e \u003cp\u003eTroubleshooting of Centrifugal and Reciprocating Compressors 425\u003c\/p\u003e \u003cp\u003eNomenclature 429\u003c\/p\u003e \u003cp\u003eGreek Symbols 431\u003c\/p\u003e \u003cp\u003eSubscripts 432\u003c\/p\u003e \u003cp\u003eNomenclature 432\u003c\/p\u003e \u003cp\u003eSubscripts 434\u003c\/p\u003e \u003cp\u003eGreek Symbols 434\u003c\/p\u003e \u003cp\u003eReferences 434\u003c\/p\u003e \u003cp\u003ePumps 434\u003c\/p\u003e \u003cp\u003eBibliography 435\u003c\/p\u003e \u003cp\u003eReferences 435\u003c\/p\u003e \u003cp\u003eCompressors 435\u003c\/p\u003e \u003cp\u003eBibliography 436\u003c\/p\u003e \u003cp\u003e\u003cb\u003e7 Mass Transfer 437\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eIntroduction 437\u003c\/p\u003e \u003cp\u003eVapor Liquid Equilibrium 437\u003c\/p\u003e \u003cp\u003eBubble Point Calculation 441\u003c\/p\u003e \u003cp\u003eDew Point Calculation 442\u003c\/p\u003e \u003cp\u003eEquilibrium Flash Composition 442\u003c\/p\u003e \u003cp\u003eFundamental 443\u003c\/p\u003e \u003cp\u003eThe Equations 444\u003c\/p\u003e \u003cp\u003eThe Algorithm 445\u003c\/p\u003e \u003cp\u003eNomenclature 446\u003c\/p\u003e \u003cp\u003eTower Sizing for Valve Trays 446\u003c\/p\u003e \u003cp\u003eIntroduction 446\u003c\/p\u003e \u003cp\u003eThe Equations 448\u003c\/p\u003e \u003cp\u003eNomenclature 452\u003c\/p\u003e \u003cp\u003eGreek Letters 465\u003c\/p\u003e \u003cp\u003ePacked Tower Design 466\u003c\/p\u003e \u003cp\u003eIntroduction 466\u003c\/p\u003e \u003cp\u003ePressure Drop 466\u003c\/p\u003e \u003cp\u003eFlooding 466\u003c\/p\u003e \u003cp\u003eOperating and Design Conditions 468\u003c\/p\u003e \u003cp\u003eDesign Equations 471\u003c\/p\u003e \u003cp\u003ePacked Towers versus Trayed Towers 473\u003c\/p\u003e \u003cp\u003eEconomic Trade-Offs 473\u003c\/p\u003e \u003cp\u003eNomenclature 474\u003c\/p\u003e \u003cp\u003eGreek Letters 474\u003c\/p\u003e \u003cp\u003eDetermination of Plates in Fractionating Columns By the Smoker Equations 474\u003c\/p\u003e \u003cp\u003eIntroduction 474\u003c\/p\u003e \u003cp\u003eThe Equations 474\u003c\/p\u003e \u003cp\u003eApplication to a Distillation Column 475\u003c\/p\u003e \u003cp\u003eRectifying Section: 475\u003c\/p\u003e \u003cp\u003eStripping Section: 476\u003c\/p\u003e \u003cp\u003eNomenclature 476\u003c\/p\u003e \u003cp\u003eMulticomponent Distribution and Minimum Trays In Distillation Columns 477\u003c\/p\u003e \u003cp\u003eIntroduction 477\u003c\/p\u003e \u003cp\u003eKey Components 477\u003c\/p\u003e \u003cp\u003eEquations Surveyed 477\u003c\/p\u003e \u003cp\u003eFractionating Tray Stability Diagrams 479\u003c\/p\u003e \u003cp\u003eAreas of Unacceptable Operation 479\u003c\/p\u003e \u003cp\u003eFoaming 480\u003c\/p\u003e \u003cp\u003eFlooding 480\u003c\/p\u003e \u003cp\u003eEntrainment 480\u003c\/p\u003e \u003cp\u003eWeeping\/Dumping 480\u003c\/p\u003e \u003cp\u003eFractionation Problem Solving Considerations 481\u003c\/p\u003e \u003cp\u003eMathematical Modeling 481\u003c\/p\u003e \u003cp\u003eThe Fenske’s Method for Total Reflux 483\u003c\/p\u003e \u003cp\u003eThe Gilliland Method for Number of Equilibrium Stages 484\u003c\/p\u003e \u003cp\u003eThe Underwood Method 485\u003c\/p\u003e \u003cp\u003eEquations for Describing Gilliland’s Graph 486\u003c\/p\u003e \u003cp\u003eKirkbride’s Feed Plate Location 487\u003c\/p\u003e \u003cp\u003eNomenclature 487\u003c\/p\u003e \u003cp\u003eGreek Letters 488\u003c\/p\u003e \u003cp\u003eExamples and Solutions 488\u003c\/p\u003e \u003cp\u003eReferences 499\u003c\/p\u003e \u003cp\u003eIndex 501\u003c\/p\u003e\u003c\/font\u003e\u003c\/p\u003e\r\n\r\n\u003cp\u003e\u003cfont size=\"3\"\u003eSubject Areas: Industrial chemistry \u0026amp; manufacturing technologies [\u003ca title=\"See our other books on Industrial chemistry \u0026amp; manufacturing technologies\" href=\"https:\/\/freshlyprintedbooks.co.uk\/search?q=%22Industrial%20chemistry%20\u0026amp;%20manufacturing%20technologies%20%5BTD%5D%22\"\u003eTD\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":52428612206872,"sku":"9781119510185","price":149.76,"currency_code":"GBP","in_stock":true}],"thumbnail_url":"\/\/cdn.shopify.com\/s\/files\/1\/0730\/2037\/5320\/files\/9781119510185.jpg?v=1784681524","url":"https:\/\/freshlyprintedbooks.co.uk\/products\/chemical-process-engineering-volume-1-design-analysis-simulation-integration-and-problem-solving-with-microsoft-excel-unisim-software-for-chemical-engineers-computation-physical-property-fluid-flow-equipment-and-instrumen-hardback-9781119510185","provider":"Freshly Printed Books","version":"1.0","type":"link"}