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Flow state

To fuUy understand the mechanics of flow, the following definitions explain the behavior of various types of fluids in both their static and flowing states. [Pg.883]

A study of how a sohd dries may be based on the internal mechanism of liquid flow or on the effec t of the external conditions of temperature, humidity, air flow, state of subdivision, etc., on the diying rate of the sohds. The former procedure generally requires a fundamental study of the internal condition. The latter procedure, although less fundamental, is more generally used because the results have greater immediate application in equipment design and evaluation. [Pg.1179]

External Conditions The principal external variables involved in any drying study are temperature, humidity, air flow, state of subdivision of the solid, agitation of the solid, method of supporting the solid, and contact between hot surfaces and wet solid. Alf these variables will not necessarily occur in one problem. [Pg.1179]

Thus, it can be concluded that in the present iono-mer system, zinc stearate plays a dual role. First, below its melting point it reinforces the matrix and strengthens the ionic aggregates and, second, at a higher temperature it results in solvation of the ionic aggregates and plasticizes the system, thus, facilitating the transition from the rubbery state to the viscous flow state [23]. [Pg.444]

EPDM-ZnO-stearic acid systems could not be extruded even at 190°C. This is not unexpected since the material, in the absence of zinc stearate, shows no transition from the rubbery state to the viscous flow state (Fig. 1). In the presence of 10 phr of zinc stearate, the m-EPDM-ZnO-stearic acid system could be extruded but melt fracture occurred at a lower temperature (150°C) at all shear rates. At 160°C and 170°C, however, the extrudates showed melt fracture only at high shear conditions. At 20 phr loading of zinc stearate, melt fracture of the extrudate occurred at high shear conditions at 150°C, but at higher temperatures no melt fracture occurred and the extrusion was smooth under all shear conditions. At 30 and 40 phr loadings of zinc stearate, the extrudates were smooth under all shear conditions at all temperatures. [Pg.445]

Organisation, steady development or cyclic flowing states (Living systems)... [Pg.85]

The goal of sympathomimetic therapy is to augment both coronary and cerebral perfusion pressures during the low-flow state associated with CPR. These agents increase systemic arteriolar vasoconstriction, thereby improving coronary and cerebral perfusion pressure. They also maintain vascular tone, decrease arteriolar collapse, and shunt blood to the heart and brain. [Pg.92]

Diffusion flames can best be described as the combustion state controlled by mixing phenomena—that is, the diffusion of fuel into oxidizer, or vice versa—until some flammable mixture ratio is reached. According to the flow state of the individual diffusing species, the situation may be either laminar or turbulent. It will be shown later that gaseous diffusion flames exist, that liquid burning proceeds by a diffusion mechanism, and that the combustion of solids and some solid propellants falls in this category as well. [Pg.261]

A characteristic quantity describing the viscous flow state is the dimensionless Reynolds number Re. [Pg.15]

Assume that the water contains a radioactive substance that causes internal volumetric heat generation q (W/m3). With the objective of deriving a total energy equation for the annular flow, state the first law. Be careful with the signs and the definitions of positive heat transfer and work. [Pg.198]

The very first experiments in extension of polymers in the viscous flow state n 12,15) demonstrated that ct/x const, as it is the case in Newtonian media. The relationship a/ep = 3n, true in the linear area under arbitrary conditions of tensile strain1314 , does not hold true in the area of significant elastic deformations 11,12>. [Pg.6]

Granulation with screw mixer-granulators requires fairly simple equipment. However, stringent requirements are placed on source material, as regards increased duration of a viscous-flow state at moulding temperatures and the need to rigidly maintain predetermined temperature conditions in all zones of the operating equipment. [Pg.173]

Fig. 1.19.2. Isoplethal section of the solid-liquid state diagram for R = 0.1. Section fields 1, solution (viscous-flow state) 2, ice 3, ice and amorphous phase (mechanical properties... Fig. 1.19.2. Isoplethal section of the solid-liquid state diagram for R = 0.1. Section fields 1, solution (viscous-flow state) 2, ice 3, ice and amorphous phase (mechanical properties...
This equation means that the change in M with t depends on N further, the difference in the flow state in the vessel that is controlled by the discharge flow rate from the impeller affects the change in mixedness with time. [Pg.49]

Flow state fully developed turbulent flow. [Pg.50]

After confirming that the flow state in a circular pipe becomes steady, the three-dimensional movement of water, which is represented by the movement of the tracer particles, is measured by recording their movement on video. The local mixing capacity M0 and MI based on the outflow and inflow, respectively, of each radial region as the distributor and blender, respectively, is calculated by using Eq. (2.27). [Pg.65]

The stirred vessel that involves fixed solid particles and ion exchange water is placed in a square water tank. After the flow state in the stirred vessel becomes steady under a fixed impeller rotational speed, images... [Pg.78]

Figure 5.3 Flow states controlled by stirring and aeration. Figure 5.3 Flow states controlled by stirring and aeration.
Polymer Density in flow state, g cm-3 Transition temperature, crystal °C glass Me... [Pg.15]

The representation for a total flowsheet is handled similarly by AIDES and BALTAZAR. Their view is to transform streams defined by temperature, pressure, total flow, state, chemical species and their mole fractions by applying a sequence of tasks such as temperature changing (heaters, coolers), pressure changing (valves, pumps, compressors), composition and flow changing (separators, mixters, splitters) and kind of species (reactors). [Pg.75]

In the conception of model experiments we first regard a general flow state and will only later presuppose the creeping flow. [Pg.65]

Pi-numbers which describe the general flow state (8.41) can be split into three groups ... [Pg.65]

A further exceedingly important mixing operation consists of whirling up solid particles ( suspension of solids ) to obtain their surfaces completely accessible to the surrounding liquid (dissolution of salts, solid catalyzed reactions in a S/L/G system, and so on). To work out the criteria important for this task, research concentrated on measuring the critical stirrer speed necessary for the flow state in which no particle lingered longer than 1 second on the bottom of the vessel. [Pg.86]

The data presented in Fig. 77 deal with flow states, these being far more complicated than those encountered in the ventilation technique. It would certainly be of interest to examine which tips and statements can be delivered here by the Computational Fluid Dynamics (CFD) ... [Pg.165]


See other pages where Flow state is mentioned: [Pg.443]    [Pg.694]    [Pg.296]    [Pg.447]    [Pg.277]    [Pg.469]    [Pg.99]    [Pg.103]    [Pg.72]    [Pg.25]    [Pg.56]    [Pg.696]    [Pg.232]    [Pg.71]    [Pg.25]    [Pg.3]    [Pg.169]    [Pg.33]    [Pg.288]    [Pg.137]    [Pg.137]    [Pg.186]    [Pg.105]    [Pg.188]    [Pg.273]    [Pg.206]   
See also in sourсe #XX -- [ Pg.221 ]




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Anisotropy in a Simple Steady-State Shear Flow

Batch or Steady-State Plug-Flow Reactor

Channel flow steady state

Continuous flow reactor steady state, mixtures with

Continuous flow reactors steady state

Continuous steady-state flow

Continuous steady-state flow process

Cross-flow solid state electrochemical

Electrochemical reactors, cross-flow solid state

Energy Balances for Steady-State Flow Processes

Energy equation for general steady-state flow

Flow diagram and stationary states

Flow diagram of continuous solid state polymerisation

Flow processes, steady-state

Flow rate steady-state behavior

Flow reactors multiple steady states

Flow steady state temperature profiles

Flow system steady-state, pressure

Flow temperatures of transition from anisotropic to isotropic state

Flow without transition to the solid state

Heat steady-state tubular flow

Isentropic steady-state flow

Kinetic measurement steady-state flow experiments

Kinetic steady-state flow conditions

Material Functions for Steady-State Elongational Flow

Material Functions for Steady-State Shear Flow

Modeling and Simulation of Unsteady-state-operated Trickle-flow Reactors

Momentum steady-state flow

Multiple steady states plug flow

Non-Steady-State Shear Flow

Non-stationary states of flow

Non-steady state diffusional flow

Normal stress differences in steady-state shear flow

Perfectly mixed flow reactors steady-state reactor design

Plug flow reactors steady state

Quality of the Joule steady-state flow process

Quasi-steady-state-flow

Second-Law Relation for Steady-State Flow Processes

Semi-steady state flow

Stationary states and flow diagrams with exponential approximation

Stationary-state relationship and flow diagram

Steady State of Flow

Steady state diffusional flow

Steady-State Maxwell Orthogonal Rheometer Flow

Steady-State Mixed Flow Reactors

Steady-State Saturated Flow — Single Fluid

Steady-State Shear Flow Measurement

Steady-State Simple Shear Flow

Steady-State Tubular Flow with Heat Loss

Steady-state analysis load-flow calculation

Steady-state cocurrent flow

Steady-state cocurrent flow observation

Steady-state compressible flow

Steady-state elongational flow field

Steady-state flow

Steady-state flow experiments

Steady-state flow in a nozzle

Steady-state flow processes irreversibility

Steady-state flow reactors

Steady-state flow systems

Steady-state flow through a nozzle with constant specific volume

Steady-state flow, definition

Steady-state flows in straight pipes regular head loss

Steady-state incompressible flow

Steady-state molar flow rates

Steady-state shear flow

Steady-state shear flow field

Steady-state substrate flow in a facilitated transport

Stopped-flow methods, transient-state kinetic

Stress Relaxation after Cessation of Steady-State Non-Newtonian Flow

Stress relaxation after cessation of steady-state flow

Superposition of Steady-State Shear Flow and Small-Amplitude Oscillations

The Diffusivity Tensor for Steady-State Shear and Elongational Flows

The Heat-Flux Vector in Steady-State Shear and Elongational Flows

The energy equation for general steady-state flow

The flow state

Thermodynamic Analysis of Steady-State Flow Processes

Transient Mass Transfer in Steady-State Translational and Shear Flows

Unsteady state flow

Unsteady-State Flows in Fixed-Bed Reactors

Unsteady-state flow reactor

Unsteady-state-flow processes

Viscoelastic state rubbery flow

Viscous-flow state

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