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Packing material energy

Adebiyi, G. A., 1991, A second law study on packed-bed energy storage systems utilizing phase change materials, ASME J. Solar Energy Eng. 113 146—156. [Pg.149]

Effect of the eluent composition could be discussed on the basis of equation (2-55). In the simple case of binary eluent (organic/water mixture), we can consider in the first approximation that Gibbs free energy of the eluent interaction with the packing material surface is a linear function of the eluent composition... [Pg.53]

At low concentrations, this model reduces to the FreimdUch isotherm. Because p < 1, this isotherm is tangent to the vertical axis, its initial slope is infinite and it is impossible to elute aU the amoxmt of sample injected out of the column in a finite time. This is not an attractive behavior for a chromatographic packing material. This model has been used in simple studies of the adsorption behavior on heterogeneous surfaces [71]. In this application, it has the major drawback of imposing a unimodal adsorption energy distribution that does not necessarily reflect the actual properties of the heterogeneous adsorbent surface studied [72]. [Pg.98]

Paper, in the form of used newspapers, packing materials, and telephone books, may be burned for energy, but it still makes up 30 percent to 45 percent of the average landfill. Landfilled paper requires decades to decay and... [Pg.1097]

General computational chemical analysis of liquid chromatographic retention is performed without solvents in the calculation. Generally, mixed solvents with and without pH-controlled ions are present as the eluent components in liquid chromatography. At present, these solvent systems cannot be handled by computational chemical calculations. The measurement of direct interactions, however, reveals the different strengths of molecular interactions between an analyte and the packing material surface. The difference in molecular interaction energy values can be used as a relative retention time. [Pg.16]

Energy balances can be formulated for both fronts. At the defrost front, heat is required to heat up the packing material from the saturation temperature (Tj) to the inlet temperature (T2). Furthermore, heat is consumed due to the (endothermic) sublimation of component i. The required energy is provided by the feed gas, which is cooled down from T2 to Tj. The energy balance results in... [Pg.19]

Proper earthing/grounding Well-connected operational energy source Removal of packing material and no physical damage Well-calibrated instruments Field devices operational Logic solver I/O operational Interface and peripherals operational... [Pg.454]


See other pages where Packing material energy is mentioned: [Pg.169]    [Pg.229]    [Pg.372]    [Pg.301]    [Pg.567]    [Pg.162]    [Pg.313]    [Pg.315]    [Pg.106]    [Pg.45]    [Pg.34]    [Pg.169]    [Pg.276]    [Pg.62]    [Pg.76]    [Pg.86]    [Pg.116]    [Pg.370]    [Pg.276]    [Pg.44]    [Pg.44]    [Pg.718]    [Pg.860]    [Pg.2985]    [Pg.111]    [Pg.255]    [Pg.3]    [Pg.130]    [Pg.443]    [Pg.18]    [Pg.77]    [Pg.115]    [Pg.149]    [Pg.157]    [Pg.13]    [Pg.136]    [Pg.252]    [Pg.6]    [Pg.372]    [Pg.7]    [Pg.88]    [Pg.226]    [Pg.444]   
See also in sourсe #XX -- [ Pg.420 , Pg.421 ]




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