LEADER 05299nam 2200673Ia 450 001 9910455673903321 005 20200520144314.0 010 $a1-281-03387-1 010 $a9786611033873 010 $a0-08-052369-2 035 $a(CKB)111056552532096 035 $a(EBL)317078 035 $a(OCoLC)191803208 035 $a(SSID)ssj0000071951 035 $a(PQKBManifestationID)11123245 035 $a(PQKBTitleCode)TC0000071951 035 $a(PQKBWorkID)10093758 035 $a(PQKB)11093557 035 $a(MiAaPQ)EBC317078 035 $a(Au-PeEL)EBL317078 035 $a(CaPaEBR)ebr10206495 035 $a(CaONFJC)MIL103387 035 $a(OCoLC)437191568 035 $a(EXLCZ)99111056552532096 100 $a20011211d1995 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 10$aFluid flow for chemical engineers$b[electronic resource] /$fF.A. Holland, R. Bragg 205 $a2nd ed. 210 $aLondon $cEdward Arnold$d1995 215 $a1 online resource (375 p.) 300 $aPrevious ed.: 1973. 300 $aIncludes index. 311 $a0-340-61058-1 327 $aFront Cover; Fluid Flow for Chemical Engineers; Copyright Page; Contents; List of examples; Preface to the second edition; Nomenclature; Chaptre 1. Fluids in motion; 1.1 Units and dimensions; 1.2 Description of fluids and fluid flow; 1.3 Types of flow; 1.4 Conservation of mass; 1.5 Energy relationships and the Bernoulli equation; 1.6 Momentum of a flowing fluid; 1.7 Stress in fluids; 1.8 Sign conventions for stress; 1.9 Stress components; 1.10 Volumetric flow rate and average velocity in a pipe; 1.11 Momentum transfer in laminar flow; 1.12 Non-Newtonian behaviour 327 $a1.13 Turbulence and boundary layersChapter 2. Flow of incompressible Newtonian fluids in pipes and channels; 2.1 Reynolds number and flow patterns in pipes and tubes; 2.2 Shear stress in a pipe; 2.3 Friction factor and pressure drop; 2.4 Pressure drop in fittings and curved pipes; 2.5 Equivalent diameter for non-circular pipes; 2.6 Velocity profile for laminar Newtonian flow in a pipe; 2.7 Kinetic energy in laminar flow; 2.8 Velocity distribution for turbulent flow in a pipe; 2.9 Universal velocity distribution for turbulent flow in a pipe; 2.10 Flow in open channels 327 $aChapter 3. Flow of incompressible non-Newtonian fluids in pipes3.1 Elementary viscometry; 3.2 Rabinowitsch-Mooney equation; 3.3 Calculation of flow rate-pressure drop relationship for laminar flow using t-y data; 3.4 Wall shear stress-flow characteristic curves and scale-up for laminar flow; 3.5 Generalized Reynolds number for flow in pipes; 3.6 Turbulent flow of inelastic non-Newtonian fluids in pipes; 3.7 Power law fluids; 3.8 Pressure drop for Bingham plastics in laminar flow; 3.9 Laminar flow of concentrated suspensions and apparent slip at the pipe wall; 3.10 Viscoelasticity 327 $aChapter 4. Pumping of liquids4.1 Pumps and pumping; 4.2 System heads; 4.3 Centrifugal pumps; 4.4 Centrifugal pump relations; 4.5 Centrifugal pumps in series and in parallel; 4.6 Positive displacement pumps; 4.7 Pumping efficiencies; 4.8 Factors in pump selection; Chapter 5. Mixing of liquids in tanks; 5.1 Mixers and mixing; 5.2 Small blade high speed agitators; 5.3 Large blade low speed agitators; 5.4 Dimensionless groups for mixing; 5.5 Power curves; 5.6 Scale-up of liquid mixing systems; 5.7 The purging of stirred tank systems; Chapter 6. Flow of compressible fluids in conduits 327 $a6.1 Energy relationships6.2 Equations of state; 6.3 Isothermal flow of an ideal gas in a horizontal pipe; 6.4 Non-isothermal flow of an ideal gas in a horizontal pipe; 6.5 Adiabatic flow of an ideal gas in a horizontal pipe; 6.6 Speed of sound in a fluid; 6.7 Maximum flow rate in a pipe of constant cross-sectional area; 6.8 Adiabatic stagnation temperature for an ideal gas; 6.9 Gas compression and compressors; 6.10 Compressible flow through nozzles and constrictions; Chapter 7. Gas-liquid two-phase flow; 7.1 Flow patterns and flow regime maps; 7.2 Momentum equation for two-phase flow 327 $a7.3 Flow in bubble columns 330 $aThis major new edition of a popular undergraduate text covers topics of interest to chemical engineers taking courses on fluid flow. These topics include non-Newtonian flow, gas-liquid two-phase flow, pumping and mixing. It expands on the explanations of principles given in the first edition and is more self-contained. Two strong features of the first edition were the extensive derivation of equations and worked examples to illustrate calculation procedures. These have been retained. A new extended introductory chapter has been provided to give the student a thorough basis to understand the me 606 $aFluid dynamics$xMathematics 606 $aChemical engineering 608 $aElectronic books. 615 0$aFluid dynamics$xMathematics. 615 0$aChemical engineering. 676 $a532/.051 700 $aHolland$b F. A$0913964 701 $aBragg$b R$0913965 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910455673903321 996 $aFluid flow for chemical engineers$92047717 997 $aUNINA