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Viscosity physical mechanism

Almost any known polymer or polymer mixture can be used in the capacity of a polymer matrix various additives may be introduced in the matrix to reduce melt viscosity, increase thermal stability of the composition or its plasticity, etc. A choice of a matrix is determined mainly by the operating conditions of a material and the desired physical-mechanical properties of a composite. One may state rather confidently that, other things being equal, the value of the CPCM conductivity does not depend on a choice of a polymer matrix [3]. [Pg.127]

The physical mechanism of viscosity is one of momentum exchange. Consider the laminar-flow situation. Molecules may move from one lamina to another, carrying with them a momentum corresponding to the velocity of the flow. There is a net momentum transport from regions of high velocity to regions of low velocity, thus creating a force in the direction of the flow. This force is the viscous-shear stress which is calculated with Eq. (5-1). [Pg.209]

The physical mechanism of heat transfer in turbulent flow is quite similar to that in laminar flow the primary difference is that one must deal with the eddy properties instead of the ordinary thermal conductivity and viscosity. The main difficulty in an analytical treatment is that these eddy properties vary across the boundary layer, and the specific variation can be determined only from experimental data. This is an important point. All analyses of turbulent... [Pg.237]

Thin solid films of polymeric materials used in various microelectronic applications are usually commercially produced the spin coating deposition (SCD) process. This paper reports on a comprehensive theoretical study of the fundamental physical mechanisms of polymer thin film formation onto substrates by the SCD process. A mathematical model was used to predict the film thickness and film thickness uniformity as well as the effects of rheological properties, solvent evaporation, substrate surface topography and planarization phenomena. A theoretical expression is shown to provide a universal dimensionless correlation of dry film thickness data in terms of initial viscosity, angular speed, initial volume dispensed, time and two solvent evaporation parameters. [Pg.261]

The basic theory of the evolution of an accretion disk can be derived by assuming that there is some physical mechanism operating that results in an effective viscosity of the gas. Because the intrinsic molecular viscosity of hydrogen gas is far too small... [Pg.71]

In microcarrier cultures, cell injury is due to the interactions (collisions) between microcarrier beads on which cells are attached, interactions between microcarriers and small turbulent eddies and interactions between microcarriers and bioreactor internals, such as the impeller and various probes (Papoutsakis, 1991a). To protect cells against injury in microcarrier bioreactors, an increased medium viscosity has been the only documented and studied medium alteration (Croughan et ai, 1989 Papoutsakis, 1991a Lakhotia Papoutsakis, 1992). Dextran (Sigma) has been used to increase the medium viscosity as discussed below. This is a purely physical mechanism of protection. [Pg.211]

Physical Mechanisms. The simplest interpretation of these results is that the transport coefficients, other than the thermal conductivity, of the water are decreased by the hydration interaction. The changes in these transport properties are correlated the microemulsion with compositional phase volume 0.4 (i.e. 60% water) exhibits a mean dielectric relaxation frequency one-half that of the pure liquid water, and ionic conductivity and water selfdiffusion coefficient one half that of the bulk liquid. In bulk solutions, the dielectric relaxation frequency, ionic conductivity, and self-diffusion coefficient are all inversely proportional to the viscosity there is no such relation for the thermal conductivity. The transport properties of the microemulsions thus vary as expected from simple changes in "viscosity" of the aqueous phase. (This is quite different from the bulk viscosity of the microemulsion.)... [Pg.283]

The result obtained from the film theory is that the mass transfer coefficient is directly proportional to the diffusion coefficient. However, the experimental mass transfer data available in the literature [6], for gas-liquid interfaces, indicate that the mass transfer coefficient should rather be proportional with the square root of the diffusion coefficient. Therefore, in many situations the film theory doesn t give a sufficient picture of the mass transfer processes at the interfaces. Furthermore, the mass transfer coefficient dependencies upon variables like fluid viscosity and velocity are not well understood. These dependencies are thus often lumped into the correlations for the film thickness, 1. The film theory is inaccurate for most physical systems, but it is still a simple and useful method that is widely used calculating the interfacial mass transfer fluxes. It is also very useful for analysis of mass transfer with chemical reaction, as the physical mechanisms involved are very complex and the more sophisticated theories do not provide significantly better estimates of the fluxes. Even for the description of many multicomponent systems, the simplicity of the model can be an important advantage. [Pg.614]

Low specific mass, high physic-mechanical characteristics (impact viscosity, resistance to multiple bending, wear resistance), satisfactory thermal, chemical and water resistance, low resistance to frost and oxidation, good dielectric properties. [Pg.28]

The gas emitted from coal wall inrush into topcarving area continuously. So the process can be seen as a process of diffusion of gas and air. For the low air-speed, gas can not be driven out from top-carving area, which methane cluster formed. Finally, the distribution and concentration of gas and air is interaction of field of air and gas concentration. For top-carving area is place gas accumulated with high concentration, which the existence of gas changed the physical mechanical property of air flow, the concentration of mixed air, kinematic viscosity and flow-speed should be the weighted mean of two kind. [Pg.964]

There are two different ways of accounting for y or Vjy. The first consists of postulating a physical mechanism, which in this case is the effect of the presence of minute quantities of surface active impurities. The second is to define an effective surface viscosity, a matter considered further in Section 8. [Pg.407]

Table 1 lists suppliers for PVB resins, commercial trade names, and reported 1999 plant capacities (49). The only major manufacturer of PVF resins is Chisso Corp. in Japan (trade name Vinylec). Chisso purchased Monsanto s PVF Formvar business in 1992. Wacker no longer manufactures PVF Pioloform F resins, only PVB Pioloform B resins. Table 2 lists reported properties of Vinylec PVF resins (21). The physical, mechanical, and thermal properties of various grades of Solu-tia s Butvar resins are listed in Table 3 (19). In general, resin melt and solution viscosity increase with increasing molecular weight and vinyl alcohol content, whereas the tensile strength of materials made from PVB increases with vinyl alcohol content for a given molecular weight. Table 1 lists suppliers for PVB resins, commercial trade names, and reported 1999 plant capacities (49). The only major manufacturer of PVF resins is Chisso Corp. in Japan (trade name Vinylec). Chisso purchased Monsanto s PVF Formvar business in 1992. Wacker no longer manufactures PVF Pioloform F resins, only PVB Pioloform B resins. Table 2 lists reported properties of Vinylec PVF resins (21). The physical, mechanical, and thermal properties of various grades of Solu-tia s Butvar resins are listed in Table 3 (19). In general, resin melt and solution viscosity increase with increasing molecular weight and vinyl alcohol content, whereas the tensile strength of materials made from PVB increases with vinyl alcohol content for a given molecular weight.
This research note focuses on process characteristics of pol5nner solutions, such as viscosity and electrical conductivity, as well as the parameters of electrospinning using poly-3-hydroxybutyrate modified by titanium dioxide nanoparticles, which have been optimized. The structure of materials has been examined by means of X-ray diffraction, differential scanning calorimetry, IR-spectroscopy, and physical-mechanical testing. [Pg.188]

The kinetics of these electronic-energy transfer processes are thus deceptively similar to those of encounter-controlled bimolecular chemical reactions, and their rates are related to viscosity in the same way as those of difhisional collision processes in which kinetic energy only is transferred. The physical mechanisms, however, must be very different. Chemical reactions that occur at every encounter require only that the reactants come into close contact and remain so for a sufficient time. Electronic energy will be transferred during an encounter only if, in addition, it is allowed by the spin-momentum rules, i.e., if there is sufficient spin-orbital coupling between D and A for the exchange of electrons to occur... [Pg.170]


See other pages where Viscosity physical mechanism is mentioned: [Pg.451]    [Pg.34]    [Pg.271]    [Pg.523]    [Pg.548]    [Pg.312]    [Pg.451]    [Pg.212]    [Pg.263]    [Pg.253]    [Pg.537]    [Pg.72]    [Pg.918]    [Pg.286]    [Pg.176]    [Pg.4]    [Pg.217]    [Pg.318]    [Pg.16]    [Pg.188]    [Pg.559]    [Pg.243]    [Pg.23]    [Pg.76]    [Pg.312]    [Pg.618]    [Pg.267]    [Pg.137]    [Pg.26]    [Pg.19]    [Pg.15]    [Pg.113]    [Pg.117]    [Pg.58]   
See also in sourсe #XX -- [ Pg.209 ]




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