LEADER 05452nam 2200649Ia 450 001 9911006654003321 005 20200520144314.0 010 $a1-281-03489-4 010 $a9786611034894 010 $a0-08-051724-2 035 $a(CKB)1000000000350817 035 $a(EBL)313758 035 $a(OCoLC)476103580 035 $a(SSID)ssj0000246164 035 $a(PQKBManifestationID)12075649 035 $a(PQKBTitleCode)TC0000246164 035 $a(PQKBWorkID)10181159 035 $a(PQKB)10793119 035 $a(MiAaPQ)EBC313758 035 $a(PPN)197766633 035 $a(EXLCZ)991000000000350817 100 $a19990819d1999 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 10$aSimulation of industrial processes for control engineers /$fPhilip Thomas 210 $aOxford ;$aBoston $cButterworth-Heinemann$d1999 215 $a1 online resource (415 p.) 300 $aDescription based upon print version of record. 311 $a0-7506-4161-4 320 $aIncludes bibliographical references and index. 327 $aFront Cover; Simulation of Industrial Processes for Control Engineers; Copyright Page; Contents; Foreword; Notation; Chapter 1. Introduction; Chapter 2. Fundamental concepts of dynamic simulation; 2.1 Introduction; 2.2 Building up a model of a simple process-plant unit: tank liquid level; 2.3 The general form of the simulation problem; 2.4 The state vector; 2.5 Model complexity; 2.6 Distributed systems: partial differential equations; 2.7 The problem of stiffness; 2.8 Tackling stiffness in process simulations: the properties of a stiff integration algorithm 327 $a2.9 Tackling stiffness in process simulations by modifications to the model2.10 Solving nonlinear simultaneous equations in a process model: iterative method; 2.11 Solving nonlinear simultaneous equations in a process model: the Method of Referred Derivatives; 2.12 Bibliography; Chapter 3. Thermodynamics and the conservation equations; 3.1 Introduction; 3.2 Thermodynamic variables; 3.3 Specific heats of gases; 3.4 Conservation of mass in a bounded volume; 3.5 Conservation of energy in a fixed volume; 3.6 Effect of volume change on the equation for the conservation of energy 327 $a3.7 Conservation of energy equation for a rotating component3.8 Conservation of mass in a pipe; 3.9 Conservation of energy in a pipe; 3.10 Conservation of momentum in a pipe; 3.11 Bibliography; Chapter 4. Steady-state incompressible flow; 4.1 Introduction; 4.2 The energy equation for general steady-state flow; 4.3 Incompressible flow; 4.4 Magnitude of the Fanning friction factor, f; 4.5 Frictionally resisted, incompressible flow through a real pipe; 4.6 Pressure drop due to level difference; 4.7 Frictional pressure drop; 4.8 Pressure drop due to bends and fittings 327 $a4.9 Pressure drop at pipe outlet4.10 Pressure drop at pipe inlet; 4.11 Overall relationship between mass flow and pressure difference; 4.12 Bibliography; Chapter 5. Flow through ideal nozzles; 5.1 Introduction; 5.2 Steady-state flow in a nozzle; 5.3 Maximum mass flow for a polytropic expansion; 5.4 Sonic flow; 5.5 Comparison between flow formulae; 5.6 Bibliography; Chapter 6. Steady-state compressible flow; 6.1 Introduction; 6.2 General overview of compressible pipe-flow; 6.3 Frictionally resisted, adiabatic flow inside the pipe; 6.4 Solution sequence for compressible flow through a pipe 327 $a6.5 Determination of the friction factor, f6.6 Determination of the effective length of the pipe; 6.7 Sample calculation; 6.8 Explicit calculation of compressible flow; 6.9 Example using the long-pipe approximation; 6.10 Bibliography; Chapter 7. Control valve liquid flow; 7.1 Introduction; 7.2 Types of control valve; 7.3 Pressure distribution through the valve; 7.4 Liquid flow through the valve; 7.5 Cavitation and choking in liquid flow; 7.6 Relationship between valve capacity at part open and capacity at full open; 7.7 The valve characteristic; 7.8 Velocity-head loss across the valve 327 $a7.9 Bibliography 330 $aComputer simulation is the key to comprehending and controlling the full-scale industrial plant used in the chemical, oil, gas and electrical power industries. Simulation of Industrial Processes for Control Engineers shows how to use the laws of physics and chemistry to produce the equations to simulate dynamically all the most important unit operations found in process and power plant.The book explains how to model chemical reactors, nuclear reactors, distillation columns, boilers, deaerators, refrigeration vessels, storage vessels for liquids and gases, liquid and gas flow t 606 $aProcess control$xComputer simulation 606 $aManufacturing processes$xComputer simulation 606 $aProcess control$xMathematical models 606 $aManufacturing processes$xMathematical models 615 0$aProcess control$xComputer simulation. 615 0$aManufacturing processes$xComputer simulation. 615 0$aProcess control$xMathematical models. 615 0$aManufacturing processes$xMathematical models. 676 $a621.4021 700 $aThomas$b Philip$0736296 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9911006654003321 996 $aSimulation of industrial processes for control engineers$94388188 997 $aUNINA