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Dynamics of Evaporation

It is useful to put in perspective the range of temperature conditions during the combustion of a liquid fuel. In increasing order  [Pg.137]

TL = flashpoint or the saturation temperature corresponding to the lower flammable [Pg.137]

autoignition temperature corresponding to the temperature that a mixture of fuel and air can self-ignite. Usually this is measured at or near a stoichiometric mixture. [Pg.137]

7f ad = adiabatic flame temperature corresponding to the maximum achievable temperature after combustion. This is usually reported for a stoichiometric mixture of fuel in air. [Pg.137]

A corresponding mass flux of fuel leaving the surface and moving by diffusion to the pure air with 7Fj00 = 0 would be given approximately as [Pg.138]


Adsorption and Desorption Dynamics of Evaporative Fuel Gas in Canister of ORVR (On-Board Refueling Vapor Recovery) System... [Pg.701]

Sharma, B (1998) Equilibrium and Dynamics of Evaporating or Condensing Thin Fluid Domains Thin Film Stability and Heterogeneous Nucleation, ACS J. Langmuir, vol. 14, pp. 4915-4928. [Pg.320]

Rate of evaporation = rate of condensation The dynamic equilibrium between liquid water and its vapor is denoted H20(l) H20(g)... [Pg.431]

FIGURE 8.2 When a liquid and its vapor are in dynamic equilibrium inside a closed container, the rate of condensation is equal to the rate of evaporation. [Pg.432]

The ORVR system is an important subsystem which reduces the contamination of evaporative fuel gas at gas station during the fueling. In this paper, a simulation model of adsoiption and desorption of evaporative fuel gas in canister of ORVR system is developed. From the comparison between the simulations and experiments, the validity of the developed model is verified and the dynamics can be predicted. This PDE model can be used to design the canister of ORVR system effectively for diverse climate and operating conditions. [Pg.704]

The easiest of the colligative properties to visualize is the effect of solute molecules on the vapor pressure exerted by a liquid. In a closed system, the solvent and its vapor reach dynamic equilibrium at a partial pressure of solvent equal to the vapor pressure. At this pressure, the rate of condensation of solvent vapor equals the rate of evaporation from the liquid. [Pg.856]

John C. Berg, Andreas Acrivos, and Michel Boudart, Evaporation Convection H. M. Tsuchiya, A. G, Fredrickson, and R. Aiis, Dynamics of Microbial Cell Populations Samuel Sideman, Direct Contact Heat Transfer between Immiscible Liquids Howard Brenner, Hydrodynamic Resistance of Particles at Small Reynolds Numbers... [Pg.343]

The system is ideal, with equilibrium described by a constant relative volatility, the liquid components have equal molar latent heats of evaporation and there are no heat losses or heat of mixing effects on the plates. Hence the concept of constant molar overflow (excluding dynamic effects) and the use of mole fraction compositions are allowable. [Pg.204]

Payer80 states that the UNSAT-H model was developed to assess the water dynamics of arid sites and, in particular, estimate recharge fluxes for scenarios pertinent to waste disposal facilities. It addresses soil-water infiltration, redistribution, evaporation, plant transpiration, deep drainage, and soil heat flow as one-dimensional processes. The UNSAT-H model simulates water flow using the Richards equation, water vapor diffusion using Fick s law, and sensible heat flow using the Fourier equation. [Pg.1077]

A dynamic equilibrium is a situation in which two (or more) opposing processes occur at the same rate so that no net change occurs. This is the kind of equilibrium that is established between two physical states of matter, e.g., between a liquid and its vapor, in which the rate of evaporation is equal to the rate of condensation in a closed container ... [Pg.202]

IV. System 2 Deformation Dynamics of Liquid Droplet in Collision with a Particle with Film-Boiling Evaporation... [Pg.27]

Fig. 6.9 shows the control algorithm and a process w/ith a phase shift of the first order and a dead time. The dynamics of the measuring device and the control elements (in our case the evaporator and the power supply) are... [Pg.130]


See other pages where Dynamics of Evaporation is mentioned: [Pg.137]    [Pg.137]    [Pg.139]    [Pg.303]    [Pg.392]    [Pg.1832]    [Pg.661]    [Pg.419]    [Pg.152]    [Pg.207]    [Pg.209]    [Pg.211]    [Pg.213]    [Pg.215]    [Pg.217]    [Pg.137]    [Pg.137]    [Pg.139]    [Pg.303]    [Pg.392]    [Pg.1832]    [Pg.661]    [Pg.419]    [Pg.152]    [Pg.207]    [Pg.209]    [Pg.211]    [Pg.213]    [Pg.215]    [Pg.217]    [Pg.2930]    [Pg.162]    [Pg.288]    [Pg.11]    [Pg.575]    [Pg.211]    [Pg.94]    [Pg.185]    [Pg.204]    [Pg.204]    [Pg.267]    [Pg.2]    [Pg.31]    [Pg.478]    [Pg.145]    [Pg.47]    [Pg.23]   


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Dynamics of Evaporators and Separators

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