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Adsorption prevention

The physical significance of these studies can be discussed qualitatively within the frame of the established theoretical concepts of adsorption phenomena on single crystal metal surfaces. The approximations and assumptions inherent in the present theory of adsorption prevent a quantitative application of the theory. [Pg.109]

The results of the adsorption of N2, SO2, CH3OH and H2O (polarities of 0,1.6,1.7,1.8 D, respectively) on activated carbon (from peach stones) using DR plots for analyses are in Figure 4.35. The polarity of the adsorptive prevents the filling of the micropores at low relative pressures (high values of log p /p) as noted by the increase in the ratio of slopes from... [Pg.192]

The second detergent function is to prevent formation of varnishes that come from polymerization of deposits on hot surfaces of the cylinder and the piston. Finally, by adsorption on metallic surfaces, these compounds have anti-corrosion effects. [Pg.360]

Dehydration can be performed by a number of methods cooling, absorption and adsorption. Water removal by cooling is simply a condensation process at lower temperatures the gas can hold less water vapour. This method of dehydration is often used when gas has to be cooled to recover heavy hydrocarbons. Inhibitors such as glycol may have to be injected upstream of the chillers to prevent hydrate formation. [Pg.250]

An additional method for increasing particle size deserves mention. When a precipitate s particles are electrically neutral, they tend to coagulate into larger particles. Surface adsorption of excess lattice ions, however, provides the precipitate s particles with a net positive or negative surface charge. Electrostatic repulsion between the particles prevents them from coagulating into larger particles. [Pg.242]

Xylene Isomerization. After separation of the preferred xylenes, ie, PX or OX, using the adsorption or crystallization processes discussed herein, the remaining raffinate stream, which tends to be rich in MX, is typically fed to a xylenes isomerization unit in order to further produce the preferred xylenes. Isomerization units are fixed-bed catalytic processes that are used to produce a close-to-equiUbrium mixture of the xylenes. To prevent the buildup of EB in the recycle loop, the catalysts are also designed to convert EB to either xylenes, benzene and lights, or benzene and diethylbenzene. [Pg.421]

A recently developed drying appHcation for zeoHtes is the prevention of corrosion in mufflers (52,55). Internal corrosion in mufflers is caused primarily by the condensation of water and acid as the system cools. A unique UOP zeoHte adsorption system takes advantage of the natural thermal cycling of an automotive exhaust system to desorb the water and acid precursors. [Pg.280]

Sweetening. Another significant purification appHcation area for adsorption is sweetening. Hydrogen sulfide, mercaptans, organic sulfides and disulfides, and COS need to be removed to prevent corrosion and catalyst poisoning. They ate to be found in H2, natural gas, deethanizer overhead, and biogas. Often adsorption is attractive because it dries the stream as it sweetens. [Pg.280]

Flow Sheet. Most purge-swing appHcations use two fixed-bed adsorbers to provide a continuous flow of feed and product (Fig. 16). Single beds are used when the flow to be treated is intermittent or cycHc. Because the purge flow is invariably greater than that of adsorption, purge is carried out in the down-flow direction to prevent bed lifting, and adsorption is up-flow. [Pg.284]

Water and Waste Water Treatment. PAG products are used in water treatment for removal of suspended soHds (turbidity) and other contaminants such as natural organic matter from surface waters. Microorganisms and colloidal particles of silt and clay are stabilized by surface electrostatic charges preventing the particles from coalescing. Historically, alum (aluminum sulfate hydrate) was used to neutralize these charges by surface adsorption of Al cations formed upon hydrolysis of the alum. Since 1983 PAG has been sold as an alum replacement in the treatment of natural water for U.S. municipal and industrial use. [Pg.180]

An inversion of these arguments indicates that release agents should exhibit several of the following features (/) act as a barrier to mechanical interlocking (2) prevent interdiffusion (J) exhibit poor adsorption and lack of reaction with at least one material at the interface (4) have low surface tension, resulting in poor wettabihty, ie, negative spreading coefficient, of the release substrate by the adhesive (5) low thermodynamic work of adhesion ... [Pg.100]

Many of these features are interrelated. Finely divided soHds such as talc [14807-96-6] are excellent barriers to mechanical interlocking and interdiffusion. They also reduce the area of contact over which short-range intermolecular forces can interact. Because compatibiUty of different polymers is the exception rather than the rule, preformed sheets of a different polymer usually prevent interdiffusion and are an effective way of controlling adhesion, provided no new strong interfacial interactions are thereby introduced. Surface tension and thermodynamic work of adhesion are interrelated, as shown in equations 1, 2, and 3, and are a direct consequence of the intermolecular forces that also control adsorption and chemical reactivity. [Pg.100]


See other pages where Adsorption prevention is mentioned: [Pg.142]    [Pg.317]    [Pg.27]    [Pg.294]    [Pg.300]    [Pg.149]    [Pg.23]    [Pg.618]    [Pg.92]    [Pg.144]    [Pg.603]    [Pg.142]    [Pg.317]    [Pg.27]    [Pg.294]    [Pg.300]    [Pg.149]    [Pg.23]    [Pg.618]    [Pg.92]    [Pg.144]    [Pg.603]    [Pg.243]    [Pg.88]    [Pg.419]    [Pg.143]    [Pg.157]    [Pg.387]    [Pg.446]    [Pg.431]    [Pg.532]    [Pg.532]    [Pg.385]    [Pg.117]    [Pg.222]    [Pg.411]    [Pg.449]    [Pg.178]    [Pg.193]    [Pg.548]    [Pg.300]    [Pg.490]    [Pg.12]    [Pg.13]    [Pg.159]    [Pg.270]    [Pg.271]    [Pg.271]   
See also in sourсe #XX -- [ Pg.443 ]




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