MARC Record from marc_columbia

LEADER: 18796cam a2200589 i 4500
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006 m o d
007 cr cnu|||unuuu
008 171101t20182018ne ad obf 001 0 eng d
035 $a(OCoLC)on1008868058
035 $a(NNC)13083221
040 $aN$T$beng$erda$epn$cN$T$dN$T$dCNCGM$dOCLCF$dYDX$dOPELS$dUAB$dSTF$dMERER$dD6H$dKNOVL$dERL$dDKU$dOCLCQ$dCEF$dINT$dOCLCQ$dU3W$dOCLCQ$dLVT$dOCLCQ$dCOO$dOCLCO$dZCU$dOCLCA$dOCLCQ$dOCLCO$dCUT$dS2H$dVT2$dOCLCQ
019 $a1086999777$a1235825953
020 $a9780128110386$q(electronic book)
020 $a0128110384$q(electronic book)
020 $a9780128110379$q(electronic book)
020 $a0128110376$q(electronic book)
020 $z9780128110379$q(print)
020 $z0128110376$q(print)
035 $a(OCoLC)1008868058$z(OCoLC)1086999777$z(OCoLC)1235825953
050 4 $aTP151
072 7 $aTEC$x009010$2bisacsh
072 7 $aSCI$x013060$2bisacsh
082 04 $a660$223
049 $aZCUA
100 1 $aHall, Stephen$q(Stephen M.),$eauthor.
245 10 $aRules of thumb for chemical engineers /$cStephen M. Hall.
250 $aSixth edition.
264 1 $aAmsterdam, Netherlands ;$aOxford, United Kingdom ;$aCambridge, MA :$bElsevier,$c[2018]
264 4 $c©2018
300 $a1 online resource (xiii, 502 pages) :$billustrations, charts
336 $atext$btxt$2rdacontent
337 $acomputer$bc$2rdamedia
338 $aonline resource$bcr$2rdacarrier
385 $aChemical engineers$2lcdgt
504 $aIncludes bibliographical references and index.
588 0 $aOnline resource; title from PDF title page (EBSCO, viewed November 1, 2017).
520 $a"Rules of Thumb for Chemical Engineers, Sixth Edition, is the most complete guide for chemical and process engineers who need reliable and authoritative solutions to on-the-job problems. The text is comprehensively revised and updated with new data and formulas. The book helps solve process design problems quickly, accurately and safely, with hundreds of common sense techniques, shortcuts and calculations. Its concise sections detail the steps needed to answer critical design questions and challenges. The book discusses physical properties for proprietary materials, pharmaceutical and biopharmaceutical sector heuristics, process design, closed-loop heat transfer systems, heat exchangers, packed columns and structured packings. This book will help you: save time you no longer have to spend on theory or derivations; improve accuracy by exploiting well tested and accepted methods culled from industry experts; and save money by reducing reliance on consultants. The book brings together solutions, information and work-arounds from engineers in the process industry."--Provided by publisher
505 00 $gMachine generated contents note:$g1.$tSafety --$tIntroduction --$tProcess Safety Management (PSM) --$tProcess Hazard Analysis (PHA) --$tSafe Design Practices --$tEmergency Vent Systems --$tFire Outside the Vessel --$tRunaway Reaction --$tBlocked-In Line --$tFlash Point of Binary Mixtures --$tDeflagration Prevention or Control --$tPrevent Backflow --$tEquipment Purging --$tDilution Purging --$tDisplacement Purging --$tPressure-Cycle Purging --$tEvacuation-Replacement Purging --$tElectrical Area Classification --$tCauses for Loss of Containment --$tDust Explosion Hazards --$tReferences --$tFurther Reading --$g2.$tProcess Evaluation --$tIntroduction --$tAccuracy of Cost Estimates --$tDefinition of Scope --$tTreatment of Uncertainty and Contingency --$tUser Requirements --$tBlock Diagrams --$tProcess Flow Diagrams (PFDs) --$tBasis of Design (BOD) --$tBlock-Sequential Diagrams --$tPiping & Instrumentation Diagrams (P & IDs) --$tFactory Assembled Skids and Modules --$tData Sheets and Specifications --$tCapital Cost Estimates --$tOrganization of a Cost Estimate --$tExample of a Screening Estimate for a Refinery --$tEngineering --$tReference --$g3.$tProcess Modeling --$tIntroduction --$tConcepts and Terminology --$tEquipment Design --$tMass and Energy Transfer --$tFlow Sheet Simulation -- Continuous Process --$tFlow Sheet Simulation -- Dynamic Process --$tDiscrete Process Simulation --$tGeneral Purpose Simulation Environments --$tSoftware List --$tReferences --$g4.$tFluid Flow --$tIntroduction --$tData Required --$tDesign Documents --$tMaterial and Energy Balance --$tPhysical Properties of the Materials --$tGeneral Procedure --$tRecommended Velocity --$tCompressible Flow of a Gas --$tOil/Gas Mixtures --$tCheck Valves --$tEquivalent Length --$tShortcut Equation for Pressure Drop Due to Friction --$tReynolds Number --$tFriction Factor --$tSurface Roughness --$tIncompressible Flow --$tCompressible Flow -- Isothermal --$tCompressible Flow -- Transmission Equations --$tWeymouth Equation --$tPanhandle A Equation --$tPanhandle B Equation --$tCompressible Flow -- Adiabatic --$tVisual Basic Subroutines for Pressure Drop Due to Friction --$tReynolds Number --$tDarcy Friction Factor --$tPressure Drop Due to Friction --$tOrifices --$tIncompressible Flow (Liquids) --$tCompressible Flow (Gases) --$tControl Valves --$tWater Hammer --$tPartially Full Horizontal Pipes --$tTwo-Phase Flow --$tLockhart-Martinelli --$tHomogeneous Model --$tSplit Bounds Model --$tAsymptotic Model --$tComparison of the Two-Phase Models --$tReferences --$tFurther Reading --$g5.$tVessels --$tIntroduction --$tCost Considerations --$tSafety Considerations --$tGeneral Rules of Thumb for Vessels --$tAtmospheric Storage Tanks --$tPressure Vessels and Reactors --$tTank Dimensions --$tLiquid Volume at Any Fill Height --$tTime to Drain a Tank --$tEmissions From Storage Tanks --$tLoad Cells --$tLiquid-Liquid Separators --$tVapor-Liquid Separators --$tLiquid Surge Volume --$tVapor Velocity in the Disengagement Section --$tVapor-Liquid Separator Size --$tVertical Separator --$tHorizontal Separator --$tHorizontal Drum With Water Separation --$tVessel Specifications --$tGood Engineering Practices for Storage Tank and Vent Relief Design --$tReferences --$tFurther Reading --$g6.$tBlending and Agitation --$tIntroduction --$tSafety Considerations --$tBasics --$tImpeller Types --$tDimensional Analysis --$tReynolds Number and Turbulence --$tPumping Number --$tPower and Power Number --$tBlending --$tNewtonian Fluids in Turbulent or Transitional Flow --$tShear-Thinning Fluids --$tLaminar Flow Regime --$tSolids Suspension --$tTerminal Settling Velocity --$tScale of Agitation --$tNumber and Location of Impellers --$tImpeller Speed and Agitator Power --$tGas Dispersion --$tIn-Line Mixers --$tHigh-Shear Mixers --$tMixing Solids --$tMechanical Design --$tTorque --$tShaft Diameter --$tImpeller Weight --$tCritical Speed --$tReferences --$tFurther Reading --$g7.$tPumps --$tIntroduction --$tSafety Considerations --$tPump Types and Selection --$tCentrifugal Pumps --$tPositive Displacement Pumps --$tPump Specification Checklist --$tGood Design Practice --$tPump Testing --$tSystem Curves --$tSensitivity --$tOperating Point-and-Pump Selection --$tFlow Control With Throttling Valve --$tControl Valve --$tCharting Control Characteristics --$tFlow Control by Changing the Pump Speed --$tAffinity Laws --$tPower --$tMinimum Flow --$tTemperature Rise --$tSuction System NPSH Available --$tSuction System NPSH for Studies --$tMultiple Centrifugal Pumps in Parallel or Series --$tReferences --$tFurther Reading --$g8.$tFans, Blowers, and Compressors --$tIntroduction --$tSafety Considerations --$tRules of Thumb --$tRules of Thumb (Compressors) --$tGood Engineering Practice --$tCompressed Air Systems --$tFans --$tFan Noise --$tBlower Types --$tCompressor Types --$tSurge Control --$tPerformance Calculations --$tDefinitions --$tAffinity Laws --$tPower -- Fan --$tPower -- Reciprocating Compressor --$tPower -- Centrifugal Compressor --$tComparison With Manufacturer's Data --$tPower With P-E Diagram --$tCost of Compressed Air --$tReceiver Volume --$tTime to Pump System to Pressure --$tReferences --$tFurther Reading --$g9.$tVacuum Systems --$tIntroduction --$tSafety Considerations --$tVacuum Units --$tConversion Between Mass Flow, Actual Volume Flow, and Standard Volume Flow --$tComparison of Vacuum Equipment --$tVacuum Jets --$tLiquid-Ring Vacuum Pumps --$tCorrecting for Seal Liquid Temperature and Composition --$tDry Vacuum Pumps --$tTypical Jet Systems --$tSteam Supply --$tMeasuring Air Leakage --$tTime to Evacuate --$tInstrumentation and Controls --$tReferences --$tFurther Reading --$g10.$tPneumatic Conveying --$tIntroduction --$tSafety Considerations --$tFlow Regimes --$tTypes of Systems --$tSystem Design Procedure --$tSaltation Velocity --$tPressure Drop --$tPressure Drop of Carrier Gas --$tAcceleration of Solids --$tFriction of Solids in Straight Pipe --$tFriction of Solids in Elbows --$tLifting of Solids Through Vertical Sections --$tMiscellaneous Factors --$tPrime Movers --$tFeed Systems --$tSilos --$tConveyor Piping --$tDisengagement --$tReferences --$g11.$tFiltration --$tIntroduction --$tBasket Strainers --$tCartridge Filters --$tVacuum Drum Filters --$tFilter Presses --$tMembrane Filters --$tReferences --$g12.$tHeat Exchangers --$tIntroduction --$tSafety Considerations --$tTEMA --$tSelection Guides --$tShell-and-Tube Heat Exchangers --$tPlate-and-Frame Heat Exchangers --$tSpiral Heat Exchangers --$tHelical Coil Heat Exchangers --$tDesign Recommendations --$tProcess Data --$tHeat Exchanger Configuration and Area --$tDetermining the LMTD Configuration Correction Factor --$tTube Side Pressure Drop --$tTube Side Film Coefficient --$tShell Diameter --$tIdeal Shell Side Film Coefficient --$tShell Side Film Coefficient Correction Factors --$tBaffle Cut and Spacing, Jc --$tBaffle Leakage Effects, Jl --$tBundle and Partition Bypass Effects, Jb --$tVariations in Baffle Spacing, Js --$tTemperature Gradient for Laminar Flow Regime, Jr. --$tOverall Heat Transfer Coefficient --$tShell Side Pressure Drop --$tHeat Transfer Coefficients --$tFouling Resistances --$tInstallation Recommendations --$tThermal Conductivity of Metals --$tVacuum Condensers --$tAir-cooled Heat Exchangers: Forced vs.
505 00 $tInduced Draft --$tAir-Cooled Heat Exchangers: Air Data --$tAir-Cooled Heat Exchangers: Thermal Design --$tAir-Side Heat Transfer Coefficient --$tAir-cooled Heat Exchangers: Pressure Drop, Air Side --$tAir-Cooled Heat Exchangers: Temperature Control --$tReferences --$tFurther Reading --$g13.$tClosed-Loop Heat Transfer Systems --$tIntroduction --$tSafety Considerations --$tSelecting the Heat Transfer Fluid --$tTypes of Heat Transfer Fluids --$tHeat Transfer Coefficient --$tSystem Design --$tTemperature Control --$tCase 1: Single-Temperature Central System --$tCase 2: Dual-Temperature Central System --$tCase 3: Three-Temperature Central System --$tPhysical Properties of Commercial Heat Transfer Fluids --$tReferences --$g14.$tFractionators --$tIntroduction --$tSafety Considerations --$tSeparation Factor --$tRelative Volatility --$tVapor-Liquid Equilibrium (VLE) --$tActivity Coefficients --$tSources for Activity Coefficients --$tEstablishing the Column Pressure --$tMinimum Reflux -- Binary --$tBubble Point Liquid Feed --$tDew Point Vapor Feed --$tMinimum Reflux -- Multicomponent --$tMinimum Stages --$tRelationship of Theoretical Stages to Reflux Ratio --$tFeed Location --$tReflux-to-Feed Ratio --$tActual Trays --$tGraphical Methods -- The McCabe-Thiele Diagram --$tPlotting With Murphree Tray Efficiency --$tTray Efficiency Rules of Thumb --$tUsing the McCabe-Thiele Plot --$tColumn Internals -- Trays and Packing --$tColumn Tray Spacing --$tTower Diameter -- Souders-Brown Correlation --$tPressure Drop -- Trays --$tControl Schemes --$tFlow --$tColumn Pressure --$tLevel in the Overhead Receiver --$tLevel in the Bottom of the Tower --$tComposition Control --$tConstraints --$tReboilers --$tPacked Columns --$tReferences --$tFurther Reading --$g15.$tAbsorbers --$tIntroduction --$tSafety Considerations --$tHydrocarbon Absorber Design --$tInorganic Absorbers --$tPacking Height for Mass Transfer in Packed Columns --$tOverall Mass Transfer Coefficient --$tReferences --$tFurther Reading --$g16.$tControls --$tIntroduction --$tBasic Nomenclature --$tDefinitions of Control Modes --$tProportional Control --$tIntegral (Reset) Control --$tDerivative Control --$tCascade Control --$tSpecifying Instruments to Measure Values --$tControl Ranges --$tDrawing Conventions --$tArtistic Expression --$tSafety Instrumented Systems.
505 00 $gNote continued:$tEnclosures: NEMA and IP --$tReferences --$tFurther Reading --$g17.$tBiopharmaceutical Systems --$tIntroduction --$tFacility Design and Sterilization Best Practices --$tGeneral Design Considerations --$tSystem Design Considerations --$tCIP System Design Considerations --$tSterilize (or Sanitize)-in Place (SIP) System Design Considerations --$tDisposable Systems --$tDisposable System Economic Evaluation --$tDisposable System Environmental Life Cycle Assessment --$tOpen or Closed? --$tContamination Root Causes --$tDesign and Sterile Boundary Faults --$tEquipment Faults --$tHuman Error (Procedures, Execution) --$tContamination Investigation and Recovery --$tTime Is of the Essence --$tGo for Data --$tWiden the Search --$tGet Hands-On --$tTime to Open Up --$tExperimental --$tMicrobiology Investigation --$tRisk Assessment --$tValidation --$tReferences --$tFurther Reading --$g18.$tBioprocessing --$tIntroduction --$tBioreactor Systems --$tTypical Geometric and Engineering Parameters --$tBioreactor Controllers --$tClean Gas Supply to Bioreactors --$tOxygen Transfer --$tHeat Transfer --$tpH Control --$tDownstream Processes --$tChromatography Purification --$tBuffer Prep --$tLiquid Waste Inactivation --$tReferences --$g19.$tEnergy Conservation --$tIntroduction --$tCalculating Steam Cost --$tSteam System Rules of Thumb --$tEquivalent Cost of Fuels --$tSteam Traps --$tEnergy Efficient Design for Fractionators --$tPinch Analysis --$tInsulation --$tReferences --$g20.$tDrivers --$tIntroduction --$tElectric Motors --$tMotor Voltages --$tMotors: Efficiency --$tMotors: Starter Sizes --$tMotors: Useful Equations --$tMotors: Overloading --$tAir-Driven Motors --$tHydraulic Motors --$tSteam Turbines: Steam Rate --$tSteam Turbines: Efficiency --$tGas Turbines: Performance --$tInternal Combustion Engines: Fuel Rates --$tGas Expanders: Available Energy --$tReferences --$g21.$tBoilers --$tIntroduction --$tBoiler Horsepower --$tTypes of Packaged Boilers --$tPower Plants --$tControls --$tThermal Efficiency --$tStack Gas Enthalpy --$tSteam Drum Stability --$tDeaerator Venting --$tWater Alkalinity --$tSource Water Impurities --$tConductivity Versus Dissolved Solids --$tSilica in Steam --$tCaustic Embrittlement --$tWaste Heat --$tBoiler Feedwater --$tBlowdown Control --$tBest Practices -- Burner System Piping --$tReferences --$tFurther Reading --$g22.$tCooling Towers --$tIntroduction --$tSafety Considerations --$tMechanical Draft Cooling Towers --$tMaterial and Energy Balance Calculations --$tRating Nomenclature --$tPerformance Calculations --$tOperations and Accessories --$tWater Quality Guidelines --$tScale Prevention --$tReferences --$g23.$tRefrigeration --$tIntroduction --$tSpecifications --$tIndirect and Direct System Design --$tHorsepower Per Ton --$tRefrigerants --$tRefrigerant Containment --$tSteam Jet Ejectors --$tAmmonia Absorption Utilities Requirements --$tAmmonia Heat Transfer Coefficient --$tReferences --$g24.$tReliability --$tIntroduction --$tInitial Design --$tRisk Analysis --$tSustainable Practices --$tReferences --$tFurther Reading --$g25.$tMetallurgy --$tIntroduction --$tCost Comparison --$tEmbodied Energy --$tEmbrittlement --$tStress-Corrosion Cracking --$tHydrogen Attack --$tPitting Corrosion --$tCreep and Creep-Rupture Life --$tNaphthenic Acid Corrosion --$tThermal Fatigue --$tAbrasive Wear --$tPipeline Toughness --$tCommon Corrosion Mistakes --$tReferences --$tFurther Reading --$g26.$tTroubleshooting --$tIntroduction --$tGeneral Troubleshooting Approach --$tDiagnostic Tools --$tInstruments --$tControl Valves (Process Control) --$tShell-and-Tube Heat Exchangers --$tPlate-and-Frame Heat Exchangers (PHEs) --$tFractionation Towers --$tFractionation Case Histories --$tPinch --$tKey Components --$tProfiles --$tTroubleshooting Technique --$tCutting Corners --$tTrapped Water --$tCocurrent --$tFoaming --$tStacking Packing --$tTray Supports --$tBoilup Control --$tCondenser Velocity --$tBlind Blind --$tTemperature Control of Both Ends --$tNozzle Bottleneck --$tHatless Riser --$tTilted Distributor --$tHammer --$tAeration --$tSiphoning --$tHot-Vapor Rules Bypassed --$tTrapped --$tCentrifugal Pumps --$tCompressors --$tSteam Jet Vacuum Systems --$tRefrigeration --$tReferences --$tFurther Reading --$g27.$tStartup --$tIntroduction --$tStartup Management --$tChange Control During Startup --$tStartup Cost --$tSystems Approach --$tConstruction Quality --$tStartup Checklists --$tOperating Modes --$tNormal Startup --$tNormal Operation --$tNormal Shutdown --$tEmergency Shutdown --$tProlonged Shutdown --$tReferences --$g28.$tConversion Factors and Constants --$tSignificant Figures and Rounding --$tGas Constant --$tStandard Gas Volume --$tAtmospheric Pressure --$tIrrigation Conversion --$tReferences --$g29.$tProperties --$tIntroduction --$tApproximate Physical Properties --$tVapor-Pressure Equation --$tLiquid Viscosity --$tDynamic (or Absolute) Viscosity --$tKinematic Viscosity --$tViscosity of Mixtures --$tEmulsions --$tSaybolt Universal Seconds --$tRelative Humidity --$tNomenclature --$tSurface Tension --$tThermodynamic Properties of Water and Steam --$tGas Diffusion Coefficients --$tBulk Modulus --$tWater and Hydrocarbons --$tWater in Natural Gas --$tHydrocarbons in Water --$tMethanol Injection --$tCompressibility Factor --$tInorganic Gases in Petroleum --$tFoam Density --$tEquivalent Diameter --$tEstimating Equivalent Diameter of Solids --$tProperties Data Sheet --$tReferences --$tFurther Reading.
650 0 $aChemical engineering$vHandbooks, manuals, etc.
650 7 $aSCIENCE$xChemistry$xIndustrial & Technical.$2bisacsh
650 7 $aTECHNOLOGY & ENGINEERING$xChemical & Biochemical.$2bisacsh
650 7 $aChemical engineering.$2fast$0(OCoLC)fst00852893
655 4 $aElectronic books.
655 7 $aHandbooks and manuals.$2fast$0(OCoLC)fst01423877
655 7 $aHandbooks and manuals.$2lcgft
776 08 $iPrint version:$aHall, Stephen (Stephen M.).$tRules of thumb for chemical engineers.$bSixth edition.$dAmsterdam, Netherlands ; Oxford, United Kingdom ; Cambridge, MA : Elsevier, [2018]$z9780128110379$w(DLC) 2017957000$w(OCoLC)1014498564
856 40 $uhttp://www.columbia.edu/cgi-bin/cul/resolve?clio13083221$zACADEMIC - Chemistry & Chemical Engineering
852 8 $blweb$hEBOOKS