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Fluid polymer layer

The solid polymer layer In this layer, the solid, polymer-rich phase undergoes continuous desolvation, and the system composition changes from D to B. It is the shrinkage or syneresis of the solid polymer accompanying this composition change that produces stresses in the polymer. Because the polymer is solid, these stresses cannot be as easily relieved by bulk movement of polymer as in the fluid polymer layer. Instead, the polymer... [Pg.185]

Results indicated that poly(DADMAC) will reduce damage caused by contact of low salinity fluid lost from the cement slurry with swelling clays present in the formation. An increase in poly (DADMAC) molecular weight from 600,000 to 2.6 X 10 daltons resulted in a decreased polymer effectiveness. The test columns were of relatively high permeability so the thickness of the adsorbed polymer layer, predicted to be greater for the higher molecular weight polymer, would have little effect on the observed flow rates. [Pg.216]

The substantial thickness of adsorbed polymer layers has important consequences for many systems that contain macromolecular components. When adsorbed, e.g., on the particles of fluid dis-... [Pg.150]

In summary, the lag time of drug release may be controlled by the rate at which water penetrates through the coating or shell, the rate of fluid absorption of the polymer layer, the osmotic activity of salts and osmopolymers, the erosion and dissolution rate of the polymer layers and the thickness of the layers or coatings. [Pg.167]

Good quality RO membranes can reject >95-99% of the NaCl from aqueous feed streams (Baker, Cussler, Eykamp et al., 1991 Scott, 1981). The morphologies of these membranes are typically asymmetric with a thin highly selective polymer layer on top of an open support structure. Two rather different approaches have been used to describe the transport processes in such membranes the solution-diffusion (Merten, 1966) and surface force capillary flow model (Matsuura and Sourirajan, 1981). In the solution-diffusion model, the solute moves within the essentially homogeneously solvent swollen polymer matrix. The solute has a mobility that is dependent upon the free volume of the solvent, solute, and polymer. In the capillary pore diffusion model, it is assumed that separation occurs due to surface and fluid transport phenomena within an actual nanopore. The pore surface is seen as promoting preferential sorption of the solvent and repulsion of the solutes. The model envisions a more or less pure solvent layer on the pore walls that is forced through the membrane capillary pores under pressure. [Pg.351]

The absorbents and filmated products have been described. The simplest sleeved pads contain cotton, viscose, or cellulose fiber with an outer sleeve of gauze or non-woven material. Those with a multilayer core have an outer sleeve of cotton, viscose, or non-woven fabric that may have been treated with a polymer such as polypropylene to reduce adherence. Delayed strike through is facilitated by using a fluid retardant layer within the upper and outer sleeve that encourages lateral movement of fluid within the pad. [Pg.1027]

Our restriction to simple fluids was meant to emphasize general laws and phenomena. For this reason, we did not discuss theories of the surface tension of solids, for which a variety of models have been elaborated. One of the considerations for omitting these was that such tensions cannot be measured, so that a check of the quality is edso impossible. We also consciously excluded the surface tensions of liquid metals, liquid crystals, molten crystals and polymer melts. However, spread and adsorbed polymer layers will be considered in chapter 3 and 4, respectively. For similar reasons, and because most practical applications involve ambient temperatures, we did not extensively discuss critical phenomena, notwithstanding their Intrinsic Interest. Under critical conditions the surface energy - surface entropy balance differs considerably from that at lower temperatures, emphasized in this chapter. [Pg.199]

The concentration gradients in an asymmetric membrane are complex because the driving force for diffusion in the skin layer is the concentration gradient of gas dissolved in the dense polymer, and the driving force in the porous support layer is a concentration or pressure gradient in the gas-filled pore. When the porous layer is thick, diffusion does not contribute very much to the flux, and gas flows by laminar flow in the tortuous pores. For high-flux membranes, there may also be significant mass-transfer resistances in the fluid boundary layers on both sides. [Pg.843]

For sterically stabilized suspensions, the polymer thickness A changes with the medium temperature and shear rate. It can be said that the effective polymer thickness decreases with compression pressure exerted on the polymer chain. In other words, for the same suspension, when the volume fraction is low, the polymer layer thickness is likely to have more effect on the steady shear viscosity than when the volume fraction is high. However, when the ratio of the polymer thickness to the particle diameter is large, the suspending fluid inside the polymer layer can reduce the effect of the attached polymer. [Pg.139]

Substrate passivation during coating formation is achieved by treating the surface being covered with special technological fluids, i.e. passivators. The passivation operation precedes the application of the polymer layer to the substrate. [Pg.190]

The first thing that strikes you is the high viscosity. It is normally much higher than for water. The physical cause of viscosity is internal friction. This acts between adjacent layers of the flowing fluid. Thus, we can say that internal friction in fluid polymers is greater than in water. [Pg.239]

Nanofillers. Nanofillers are extremely fine particles, under a micron in size. The most successful ones have been made by intercalating quaternary ammonium surfactants between the layers of montmorillonite clay, followed by fluid polymer, to exfoliate them down to 1-nm platelets with aspect ratio of 1000/1. When these are dispersed in nylon at low concentrations of 2 to 10 percent, the tremendous numbers of plate-like particles can produce easy processing, high modulus and strength, heat deflection temperature, trans-... [Pg.336]


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See also in sourсe #XX -- [ Pg.30 ]




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Polymer layers

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