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A B C D E F G H I J K L M N O P
Packaged units, specification of, Packing characteristic, in cooling towers, Packings, for cooling towers Packings, for fixed beds: Packinox heat exchanger, Paints, spectral characteristics of reflectance of surfaces treated with, Palen, J W Panchal, C B, Paraffins, normal and isonormal: Paraldehyde: Parallel channel instability, in condensers, Partial boiling in subcooled forced convective heat transfer, Participating media, radiation interaction in, Particle convective component, in heat transfer from fluidized beds, Particle emissivity, Particle Reynolds number in fixed beds, Particles: Particulate fluidization, Particulate fouling, Pass arrangements, in plate heat exchangers, Passes, tube side, Passive methods, for augmentation of heat transfer, passive systems for: PD5500 mechanical design of shell-and-tube heat exchangers to, Peacock, D K, Pearson number, Peclet number Peng-Robinson equation of state, application to hydrocarbons, Penner's rule, in absorption of radiation by gases, Pentachloroethane (Refrigerant 120): Pentadecane: Pentadecene: Pentadiene 1, 2: Pentadiene 1, trans 3: Pentadiene 1, 4: Pentadiene 2-3: Pentafluoroethane (Refrigerant 125) Pentamethylbenzene: Pentane: Pentanoic acid: 1-Pentanol: 1-Pentene: cis-2-Pentene: trans-2-Pentene: Pentylacetate: Pentylbenzene: Pentylcyclohexane: Pentylcyclopentane: Pentylcyclopropane, liquid properties, Perforated fins, in plate fin heat exchangers, Perforated plates, loss coefficients in, Periodic operation, of regenerator, Periodic variations in temperature, thermal conduction in bodies with, PFR correlation, for heat transfer in high fin tube banks, Pharmaceutical industry, fouling of heat exchangers in, Phase change materials, in augmentation of heat transfer, Phase change number, Phase equilibrium: Phase inversion Phase separation, as source of corrosion problems, Phenol: Phenols: Phenylhydrazine: Phonons, in thermal conductivity of solids, Phosgene: Physical properties: Pi theorum, in dimensional analysis, Pinch analysis, for heat exchanger network design, Pioro, I L Pioro, LS, Pipe leads, Piperidine: Pipes, circular: Pipes, noncircular: Piping components: Pitting corrosion, in stainless steels, Planck's constant, Planck's law, for spectral distribution of blackbody radiation, Plane shells, steady-state thermal conduction in, Plastic deformation Plate fin heat exchangers Plate fins, efficiency, Plate heat exchangers: Plate evaporator Plates: Plug flow: Plug flow model, for furnaces, Pneumatic conveyance, Pneumatic conveying dryer, P-NTU method: Polarization, of thermal radiation, Polyglycols, as heat transfer media, Polymers: Pool boiling, Porous surfaces: Port arrangements, in plate heat exchangers, Portable fouling unit, Poskas, P, Postdryout heat transfer: Powders: Power law fluid (non-Newtonian), Power plant: Prandtl number Precipitation (crystallization) fouling, Precipitation hardening, of stainless steels, Pressure coefficient: Pressure control of condensers, Pressure drop: Pressure gradient: Pressure, specification of in mechanical design to EN13445, Pressure testing, Pressure vessels, principle codes for, Pressurised water reactor, fouling in, Printed circuit heat exchanger, Problem table algorithm, in pinch analysis, Process heaters: Progressive plastic deformation Prolate spheroids, free convective heat transfer from, Promoters, in dropwise condensation, Propadiene: Propane: 1-Propanol: 2-Propanol: Propeller agitator, Property ratio method, for temperature dependent physical property Propionaldehyde: Propionic acid: Propionic anhydride: Proprionitrile: Propyl acetate: Propylamine: Propylbenzene: Propylcyclohexane: Propylcyclopentane: Propylene: 1,3-Propylene glycol: Propylene oxide: Propyl formate: Propyl propionate: Pseudo-boiling in supercritical fluids, Pseudo-film boiling in supercritical fluids, Pseudocritical pressure, Pseudocritical tempertaure, Pugh, S F Pulp and paper industry, fouling of heat exchangers in, Pulsations, use in augmentation of heat transfer, Pulverized fuel water-tube boiler, Pumping, lost work in, Pushkina and Sorokin correlation, for flooding in vertical tubes, Pyramid, free convective heat transfer from, Pyridine:
Q R S T U V W X Y Z

Flow and Pressure Drop in Annular Ducts with One Rotating Surface

DOI 10.1615/hedhme.a.000151

2.2.9 Flow and pressure drop in annular ducts with one rotating surface

A. Introduction

Situations in which flows occur between a rotating inner cylinder and a stationary outer cylinder are found widely in industry (e.g. in motor shafts, in vehicle transmissions, in oil drilling operations etc.). The presence of rotation may have a large effect on the flow and heat transfer. Flow effects are discussed in this present section and the associated heat transfer behavior is discussed in Section 183.

The flow between concentric cylinders with rotation of inner one can be considered a composition of three basic flows: Couette, Poiseuille and Taylor, which can be either laminar or turbulent. As illustrated in Figure 1, the Couette flow is caused by rotation of inner cylinder and the Poiseuille flow takes place due to pressure difference between channel inlet and outlet. Taylor flow appears due to centrifugal forces after a critical rotation condition is achieved and is characterized by a sequence of toroidal vortices, which are distributed tangentially and with alternate directions.

Figure 1 Schematic illustration of possible flow types inside of annular channels with rotation of the inner cylinder: a) Couette flow, b) Taylor flow and c) Poiseuille flow

Kaye and Elgar (1957) show experimentally that, depending on axial and tangential velocities, these basic flows will form four different regimes: laminar, laminar with Taylor vortices, turbulent and turbulent with Taylor vortices [see Figure 2(a)]. When the flow is laminar, the axial and tangential components of the fluid velocity are independent of each other. In this case, it is clear that rotation will not influence axial friction losses. On the other hand, when the Taylor vortices appear in the flow due to centrifugal forces — after a critical rotation — or when the flow is turbulent, these fluid velocity components are not independent anymore. Consequently, in these regimes the rotation of the inner cylinder is expected to influence axial friction losses. Actually, several authors confirmed the influence of rotation on friction factor. Yamada (1962), for instance, shows that there is an increase in the friction factor as rotation rate, which is represented by Taylor number, is increased. In Figure 2(b), horizontal lines represent friction factor values obtained with usual channel flow channel flow correlations. When the flow is laminar [Rez = 1000, Figure 2(b)] there is a sudden increase at a certain critical tangential velocity. At this point — that corresponds to the appearance of Taylor vortices — the velocity components abruptly stop being independent of each other and the rotation of inner cylinder becomes important. For turbulent flow, velocity components are always dependent of each other and, therefore, the rotation influence is less important than in laminar case. The higher is the axial velocity the lower is the influence of the rotation.

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