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Pressure modelling

The pneumatic pump has a relatively large flow capacity but, today, is largely used for column packing and not for LC analyses. It can provide extremely high pressures and is relatively inexpensive, but the high pressure models are a little bulky. A diagram of a pneumatic pump is shown in figure 4. [Pg.128]

Au-Cu and Au-Ag alloys Isomer shift and electrical resistivity as function of alloy composition and, in CU3AU, of pressure model to describe 5 in terms of average atomic volume, of short-range parameter and alloy composition average charge density on Au... [Pg.370]

This is an example of pressure modeling done at Factory Mutual Research (FM Global) by deRis, Kanury and Yuen [17] and Alpert [8]. In pressure modeling, Gr is preserved with pyj / 3/2 along. Therefore m"//p, is also preserved and... [Pg.397]

Alpert, R. L., Pressure modeling of fires controlled by radiation, Proc. Comb. Inst., 1977, 16, pp. 1489-500. [Pg.407]

Osmotic pressure models can be developed from a very fundamental basis. For example, it is becoming possible to predict the rate of ultrafiltration of proteins starting from a knowledge of the sequence and three-dimensional structure of the molecule 19). [Pg.451]

Womans, J. G., Nakao, S. and Smolders, C. A. Journal of Membrane Science 20 (1984) 115. Flux limitation in ultrafiltration osmotic pressure model and gel layer model. [Pg.473]

There are several ways to account for variable pressures. If the total pressure of the column changes but not the pressure drop through the trays (the normal situation in heat-integrated columns, particularly with valve trays whose pressure drops are fairly constant), an approximate variable-pressure model can be used. [Pg.141]

The finite difference air pressure model was compared with the analytical solution for depths of 1.0 and 2.0 m (Figure 13). As can be seen, the model matches the analytical solution to subsurface air pressure very well, thus verifying the accuracy of the finite difference model. [Pg.329]

Considering the interfacial pressure model, the flow rates should be between the higher and lower limits. APpiow can be evaluated by considering the pressure loss in the microchannels. Assuming that the pressure at the opened outlet is atmospheric pressure, Patm, then the pressure P of each phase from the pressure loss AP is expressed as follows ... [Pg.21]

There are two approaches to ERS design. One is system modeling, which identifies the cause of a pressure rise from a hazard analysis. It uses approximate models—allvapor flow, all-liquid flow, or two-phase flow—to simulate the pressure increase of the reacting system vs. time and to determine vent size. The method is complex since it must identify the stoichiometry, the mechanism, and the kinetics of the decomposition causing the pressure rise. Two pressure models are used for vent sizing ... [Pg.89]

Low-pressure models applicable to the protection of process buildings and storage tanks ruled by the API codes. RUST s low-pressure model is usually successful for vent design of internal or external overpressure. [Pg.89]

High-pressure models applicable to pressure vessels and chemical reactors subjected to more than 15 psig... [Pg.89]

Jayjock, M.A. (1994). Back pressure modelling of indoor air concentrations from volatilizing sources, Am. Ind. Hyg. Assoc. J., 55, 230-235. [Pg.240]

Vapor-liquid mass-transfer operations, such as absorption, stripping and distillation, are carried out in packed and plate columns. The key difference is that counterflowing vapor and liquid are contacted continuously with packings, and discretely with plates. The equilibrium and operating lines of packed and plate columns are identical under the same operating conditions—feed and product flowrates and compositions, temperature and pressure. Models for the design and analysis of packed columns are based on their close analogy to plate devices. [Pg.63]

In the case of the osmotic-pressure model, the rigorous theory allowed the conclusion that at high applied transmembrane pressure, the permeate flux increased as a cube root of the pressure, so that the limiting flux was never reached ... [Pg.333]

Danckwerts P.V., Significance of liquid film coefficients in gas absorption. Industrial Engineering and Chemistry 43 1951 460-1470. Denisov C.A., Theory of concentration polarization in cross-flow ultrafiltration Cel-layer model and osmotic-pressure model. Journal of Membrane Science 91 1994 173-187. [Pg.343]

Figure 18 Complexes observed in high pressure model studies of alkoxycarbonylation (complexes in square brackets not observed) [86]... Figure 18 Complexes observed in high pressure model studies of alkoxycarbonylation (complexes in square brackets not observed) [86]...
D pressure models can be used to map pressure at specific reservoir levels. These maps can be combined with structure maps and seismic attribute maps to constrain the risks at the target level. [Pg.198]


See other pages where Pressure modelling is mentioned: [Pg.209]    [Pg.269]    [Pg.75]    [Pg.271]    [Pg.88]    [Pg.378]    [Pg.408]    [Pg.451]    [Pg.452]    [Pg.1161]    [Pg.141]    [Pg.142]    [Pg.317]    [Pg.330]    [Pg.357]    [Pg.164]    [Pg.568]    [Pg.303]    [Pg.12]    [Pg.117]    [Pg.708]    [Pg.335]    [Pg.502]    [Pg.3170]    [Pg.214]    [Pg.220]    [Pg.76]   
See also in sourсe #XX -- [ Pg.136 , Pg.137 , Pg.138 , Pg.142 , Pg.151 , Pg.152 , Pg.153 , Pg.315 ]




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High pressure modelling

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Model for pressure drop

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Models for the Pressure Drop

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Osmotic pressure model

Partial pressure distribution model

Pressurant gas model

Pressure and the Configuration Coordinate Model

Pressure drop homogenous model

Pressure drop separated flow model

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