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Robinson model

In the revised Robinson model, the skin was modeled as a two-layer laminate consisting of stratum corneum and a watery epidermal layer. Permeation through the stratum corneum was assumed to occur through two different pathways [8] ... [Pg.473]

Table 4.25 Column configuration for a five-component distillation used in the Aspen Plus simulator with the Peng-Robinson model qc= 3395.3367 kW qR = 3432.2069 kW Number of stages = 14 Location of feed stage = 7 Reflux ratio = 8.87. Table 4.25 Column configuration for a five-component distillation used in the Aspen Plus simulator with the Peng-Robinson model qc= 3395.3367 kW qR = 3432.2069 kW Number of stages = 14 Location of feed stage = 7 Reflux ratio = 8.87.
The Stokes-Robinson model was later modified by its creators for use in more concentrated solutions by accounting for dehydration equilibria (12). The original model was also modified by Nesbitt (12), who made the hydration number a decreasing function of the ionic strength. Other workers too numerous to mention here have also attempted to do something with hydration theory. [Pg.19]

Figure 7. Calculated roughness factors, B(Q)f, for (A) modestly and (B) substantially roughened surfaces for the Robinson model described by Equation (20), and for a Gaussian distribution of terrace heights. The exact form of B 2 depends on the terrace height distribution for the highly roughened surface in (B). Figure 7. Calculated roughness factors, B(Q)f, for (A) modestly and (B) substantially roughened surfaces for the Robinson model described by Equation (20), and for a Gaussian distribution of terrace heights. The exact form of B 2 depends on the terrace height distribution for the highly roughened surface in (B).
Subsequently, a number of other investigators have modified the local feedback mechanism proposed by Robinson [1975] to better describe the neural connections and firing patterns of brainstem neurons in the control of horizontal saccadic eye. In addition to the Robinson model, two other models describe a saccade generator [Scudder, 1988 Scudder et al., 2002 Enderle, 1994, 2002], AH of the models involve three types of premotor neurons burst, tonic, and pause cells, as previously described, and involve a pulse-step change in firing rate at the motoneuron during a saccadic eye movement. [Pg.267]

EF 1693 kgmol/h (48 056 kg/h) at 2056 kfti and -24.4 °C Nf =86 Methane (0.003), Ethylene (0.8388), Ethane (0.1604), Propene (0.0005) Ethylene mole fraction in Overheads = 0.999 Ethane mole fraction in bottoms = 0.995 Column top pressure = 1997 kRa Pressure drop/tray= 0.7 kPla No. of ideal trays = 125 Total condenser Peng-Robinson model... [Pg.294]

FIGURE 9.12 DCFIs for the CCI4 - Methanol system at 7 = 298.15 K using Equation 9.74 with different mixing rules. EOS calculations from Peng-Robinson model. Equation 9.75,... [Pg.255]

Concerning the ammonia/water system used for the absorption case, in the literature there are several studies [3,4] of thermodynamic equilibrium of this mixture with Peng-Robinson model. They show that the Peng Robinson property method is suitable for this system. [Pg.210]

To address these pitfalls, the VTPR (Volume-Translated Peng-Robinson) model was proposed by Abler and Gmehling in 2001. [Pg.229]

The UMR-PR (universal mixing rule-Peng Robinson) and the VTPR (volume translated Peng Robinson) models, both use the MVH-1 mixing rule. They were resp>ectively developed by (Ahlers Gmehling, 2001, 2002) and by (Voutsas et al., 2004). In both cases, the same translated form of the PR EoS is used. The Twu a(T) function is however used in the VTPR model whereas the Mathias-Copeman expression is used in the UMR-PR model. Both models incorporate the UNIFAC model in Eq. (66). However, in order to be able to properly correlate asymmetric systems, only the residual part of UNIFAC is used in the VTPR model. These authors indeed assume that the combinatorial part of UNIFAC and X -ln(fc /fc) in Eq. (66) cancel each other. In the UMR-PR model the residual part of... [Pg.95]

Positive displacement conpressors, performance curves, 632-638 Postmortem analysis, 815-816 Postrationalization, 817-818 Pot still distillation, 92 Power recovery equipment purchase cost curves, 931 table of heuristics, 376 turbines (expanders), simulating, 434 PPA (Pollution Prevention Act), 881-883 PR (Peng-Robinson) model, phase equilibria simulation, 446- 48 Predict, authenticate, reevaluate (PAR) process, 366-367 Predicting... [Pg.1006]


See other pages where Robinson model is mentioned: [Pg.473]    [Pg.570]    [Pg.406]    [Pg.19]    [Pg.168]    [Pg.388]    [Pg.132]    [Pg.406]    [Pg.293]    [Pg.294]    [Pg.294]    [Pg.254]    [Pg.255]    [Pg.1003]    [Pg.1013]   
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Modeling Phase Behavior with the Peng-Robinson Equation of State

Robinson

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