Sink defined

T 1 m temperature of heat source or sink defined in Section 5.4.2... 

This consists of loading a pointed diamond or a hardened steel ball and pressing it into the surface of the material to be examined. The further into the material the indenter (as it is called) sinks, the softer is the material and the lower its yield strength. The true hardness is defined as the load (F) divided by the projected area of the indent, A. (The Vickers hardness, H , unfortunately was, and still is, defined as F divided by the total surface area of the indent. Tables are available to relate H to Ff .)... 

Under low-dose conditions, forest ecosystems act as sinks for atmospheric pollutants and in some instances as sources. As indicated in Chapter 7, the atmosphere, lithosphere, and oceans are involved in cycling carbon, nitrogen, oxygen, sulfur, and other elements through each subsystem with different time scales. Under low-dose conditions, forest and other biomass systems have been utilizing chemical compounds present in the atmosphere and releasing others to the atmosphere for thousands of years. Industrialization has increased the concentrations of NO2, SO2, and CO2 in the "clean background" atmosphere, and certain types of interactions with forest systems can be defined. 

Point Sink A point sink is defined as a pcjint in space at which the fluid is continuously and uniformly drawn off. The radial velocity into the sink at a distance r from the sink is, in spherical coordinates,... 

In COMIS, source or sink strength can be defined as time dependent but not dependent on actual concentrations or temperatures. COMTAM96 includes more sophisticated models such as chemical reactions, adsorption and desorption to building materials, filtration, and deposition to surfaces. 

In air conditioning circles, the tower normally represents the final heat sink in a turnkey package which would include compressors/condensers, pipework, ducting, fans, pumps, control gear, etc. Where consultants and experienced contractors are concerned, the tower specification is well defined and the purchases based upon economics related to efficiency. 

Let us define a two-box model for a steady-stafe ocean as shown in Fig. 10-22. The two well mixed reservoirs correspond to the surface ocean and deep oceans. We assume that rivers are the only source and sediments are the only sink. Elements are also removed from the surface box by biogenic particles (B). We also assume there is mixing between the two boxes that can be expressed as a velocity Vmix = 2 m/yr and that rivers input water to the surface box at a rate of Vnv = 0.1 m/yr. The resulting ratio of F mix/V riv is 20. 

Consider a heat sink as a block containing both S and R (sample and reference). This is illustrated in the following diagram, given as 7.1.23. on the next page. In this diagram, we define three temperatures, Tb, Ts Tr, where... 

In the BBB-PAMPA lipid formulation illustrated in Fig. 3.4, the diff values, defined as the difference log Pq-log Pi, range from 2.9 (morphine) to 4.2 (warfarin), somewhat similar to the values observed in the octanol-water system. However, it is premature to propose a pdiffi-A approximation, given the limited amount of data reported. With other lipid formulations, larger differences are usually observed. In Double-Sink PAM PA, and especially in hexadecane-PAMPA, transport of ionized drugs has not been reported [84]. 

We define this permeability as apparent, to emphasize that there are important but hidden assumptions made in its derivation. This equation is popularly (if not nearly exclusively) used in culture cell in vitro models, such as Caco-2. The sink condition is maintained by periodically moving a detachable donor well to successive acceptor wells over time. At the end of the total permeation time f, the mass of solute is determined in each of the acceptor wells, and the mole sum mA (t) is used in Eq. (7.10). Another variant of this analysis is based on evaluating the slope in the early part of the appearance curve (e.g., solid curves in Fig. 7.14) ... 

A heat transfer coefficient is defined as the ratio of the area-normalized heat flow to the temperature difference between the heat source (the shelf) and the heat sink (the frozen product). For the case of vials resting directly on the freeze dryer shelf, the vial heat transfer coefficient, Kv, is defined by... 

Because of the inadequacies of the aforementioned models, a number of papers in the 1950s and 1960s developed alternative mathematical descriptions of fluidized beds that explicitly divided the reactor contents into two phases, a bubble phase and an emulsion or dense phase. The bubble or lean phase is presumed to be essentially free of solids so that little, if any, reaction occurs in this portion of the bed. Reaction takes place within the dense phase, where virtually all of the solid catalyst particles are found. This phase may also be referred to as a particulate phase, an interstitial phase, or an emulsion phase by various authors. Figure 12.19 is a schematic representation of two phase models of fluidized beds. Some models also define a cloud phase as the region of space surrounding the bubble that acts as a source and a sink for gas exchange with the bubble. 

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