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Inventory surface

Surface treatments that are intended to alter physical properties, but not intended to impart chemical reactivity results in a mixture. In this case, each of the components must be on the Inventory. Surface treatments that are intended to impart reactivity result in new chemical substances and the product must be on the Inventory. [Pg.31]

For subcooling, a liquid inventory may be maintained in the bottom end of the shell by means of a weir or a hquid-level-controUer. The subcoohng heat-transfer coefficient is given by the correlations for natural convection on a vertical surface [Eqs. (5-33 ), (5-33Z )], with the pool assumed to be well mixed (isothermal) at the subcooled condensate exit temperature. Pressure drop may be estimated by the shell-side procedure. [Pg.1042]

Heat transfer equipment has a great variation in heat transfer area per unit of material volume. Table 4.4 compares the surface compactness of a variety of heat exchanger types. Falling film evaporators and wiped film heat exchangers also reduce the inventory of material on the tube side. Process inventory can be minimized by using heat exchangers with the minimum volume of hazardous process fluid for the heat transfer area required. [Pg.71]

The surface area of a vessel exposed to fire which is effective in generating vapor is that area wetted by its internal liquid contents. The liquid contents under variable level conditions should ordinarily be taken at the average inventory, for example See note below. [Pg.452]

The global design equations for packed beds—e.g.. Equations (10.1), (10.9), (10.39), and (10.40)—all have a similar limitation to that of the axial dispersion model treated in Chapter 9. They all assume steady-state operation. Adding an accumulation term, da/dt accounts for the change in the gas-phase inventory of component A but not for the surface inventory of A in the adsorbed form. The adsorbed inventory can be a large multiple of the gas-phase inventory. [Pg.375]

Example 10.12 Estimate the surface inventory of component A for the catalytic CSTR in Example 10.9. Assume that the surface reaction is ratecontrolling and that A is the only adsorbed species. Suppose A is a moderately large molecule that occupies a site that is 1 nm by 1 nm. [Pg.376]

Th do not reach constant concentrations over any reasonable distances, Ra does over several hundred meters, and all the other radionuclides require less than a few meters. Constant concentrations are achieved when the inventories of a radionuclide in both groundwater and adsorbed on surfaces decay at the same rate at which this radionuclide is... [Pg.326]

Many rubber products require uncured components which are not rectangular in cross-section. In such cases, at least one calender bowl may have a peripheral design cut into its surface to produce the desired cross section. This method is particularly useful for long production runs, but becomes expensive in terms of bowl change and bowl inventory necessary when many different sections are required. For shorter run working, the calender bowl may consist of a heavy basic mandrel onto which may be clamped solid cylindrical or split cylindrical steel shells into which the appropriate profile design has been cut. Such calenders often have the bowls outside the frames to improve access and facilitate bowl changing. Consequently the bowls are comparatively short. [Pg.172]

Fig. 3. Soil inventory of carbon in soil organic matter (SOM) (a), A14C of SOM (b), noncrystalline minerals (c), and crystalline minerals (d) versus age of soil substrate. Filled circles, total profiles filled triangle, surface (O and A) horizons (Tom et al. 1997). Fig. 3. Soil inventory of carbon in soil organic matter (SOM) (a), A14C of SOM (b), noncrystalline minerals (c), and crystalline minerals (d) versus age of soil substrate. Filled circles, total profiles filled triangle, surface (O and A) horizons (Tom et al. 1997).
Ideally, the axial velocity through the cross-flow unit should be greater than about 4-6 m/s to minimize the boundary layer of particles near the membrane surface. The wax permeate flow from the filter is limited by a control valve actuated by a reactor-level controller. Hence, a constant inventory of slurry is maintained within the SBCR system as long as the superficial gas velocity remains constant. Changes in the gas holdup due to a variable gas velocity are calculated... [Pg.279]

Dust The role of dust grain surfaces in inducing different chemical processes enriching the ISM molecular inventory... [Pg.154]


See other pages where Inventory surface is mentioned: [Pg.392]    [Pg.10]    [Pg.223]    [Pg.227]    [Pg.423]    [Pg.424]    [Pg.458]    [Pg.1212]    [Pg.452]    [Pg.452]    [Pg.400]    [Pg.406]    [Pg.26]    [Pg.173]    [Pg.110]    [Pg.327]    [Pg.375]    [Pg.376]    [Pg.304]    [Pg.185]    [Pg.88]    [Pg.66]    [Pg.320]    [Pg.326]    [Pg.347]    [Pg.595]    [Pg.146]    [Pg.159]    [Pg.1035]    [Pg.159]    [Pg.226]    [Pg.59]    [Pg.77]    [Pg.11]    [Pg.142]    [Pg.151]    [Pg.181]    [Pg.185]   
See also in sourсe #XX -- [ Pg.375 ]




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