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Diffusion Gases

Graham s law of diffusion This law states that the rates at which two gases diffuse are inversely proportional to their densities, i.e. [Pg.195]

Graham s Law of Diffusion. The rates at which gases diffuse under the same conditions of temperature and pressure are inverseiy proportionai to the square roots of their densities ... [Pg.530]

Numerous systems in science change with time or in space plants and bacterial colonies grow, chemicals react, gases diffuse. The conventional way to model time-dependent processes is through sets of differential equations, but if no analytical solution to the equations is known, so that it is necessary to use numerical integration, these may be computationally expensive to solve. [Pg.173]

Molecular gases, diffusion through vitreous silica, 22 422... [Pg.595]

Making a Model Acid precipitation often falls to Earth hundreds of kilometers away from where the pollutant gases enter the atmosphere because the gases diffuse through the air and are carried by the wind. In this lab, you will model the formation of acid rain to observe how the damage caused by acid varies with the distance from the source of pollution. You also will observe another factor that affects the amount of damage caused by acid rain. [Pg.103]

Gases diffuse from areas of high concentration to areas of low concentration. The speed at which diffusion occurs in the body depends on partition coefficients. The faster the concentration in the lung and brain tissues reaches the inhaled concentration of an anesthetic, the sooner a patient is induced. [Pg.371]

Another way to use silicon wafers as DLs was presented by Meyers and Maynard [77]. They developed a micro-PEMFC based on a bilayer design in which both the anode and the cathode current collectors were made out of conductive silicon wafers. Each of fhese componenfs had a series of microchannels formed on one of their surfaces, allowing fhe hydrogen and oxygen to flow through them. Before the charmels were machined, a layer of porous silicon was formed on top of the Si wafers and fhen fhe silicon material beneath the porous layer was electropolished away to form fhe channels. After the wafers were machined, the CEs were added to the surfaces. In this cell, the actual diffusion layers were the porous silicon layers located on top of the channels because they let the gases diffuse fhrough fhem toward the active sites near the membrane. [Pg.223]

Because the mucus layer or the underlying cells may serve as either final accumulation sites of toxic gases or layers through which the gases diffuse en route to the blood, we need simplified models of these layers. Altshuler et al. have developed for these layers the only available model that can be used in a comprehensive system for calculating tissue doses of inhaled irritants. It assumes that the basement membrane of the tracheobronchial region is covered with three discrete layers an inner layer of variable thickness that contains the basal, goblet, and ciliated cells a 7-Mm middle layer composed of waterlike or serous fluid and a 7-Mm outer layer of viscous mucus. Recent work by E. S. Boatman and D. Luchtel (personal communication) in rabbits supports the concept of a continuous fluid layer however, airways smaller than 1 mm in diameter do not show separate mucus and serous-fluid layers. [Pg.287]

In the first instance (1,3) two types of nickel are used on the side exposed to the gas, large pores are produced in the metal and adjacent to this structure, a network of smaller pores are produced to hold back the electrolyte. The reacting gases diffuse rapidly in the large pores and come in intimate contact with the electrolyte present in the small pores. For the electrochemical reaction po occur, a three phases contact is needed since a gaseous reactant produces a solvated reactior oro uct nd in this process an electron is given or withdrawn from a solid conducting substrate. [Pg.306]

Gases diffuse from areas of high partial pressure to areas of low partial pressure thus, the tension of anesthetic in the alveoli provides the driving force to establish brain tension. In fact, the tension of anesthetic in all body tissue will tend to rise toward the lung tension as equilibrium is approached. Consequently, factors that control or modify the rate of accumulation of anesthetic in the lung (e.g., rate of gas delivery, uptake of gas from the lung into the pulmonary circulation) will simultaneously influence the rate at which tension equilibria in other body compartments is established. [Pg.300]

The results of the delayed stress on radiation studies presented above (Figure 7) are also consistent with the mechanism of gas buildup within the polymer specimens as the cause of the accelerated creep. An additional interesting conclusion is that applied stress should increase the rate at which gases diffuse out of a polymer specimen. This is not unreasonable in view of the fact that this conclusion is reached for stress application during irradiation, when expansion of the polymer matrix by the internally generated gas would be expected to facilitate gas diffusion. (Actually, one would expect increased gas diffusion in stressed glassy polymers, even in the absence of radiation, owing to the low Poisson ratio in such materials.)... [Pg.118]

When we put two gases together, the molecules diffuse throughout the container, so that within a short time the mixture is homogeneous, or of uniform concentration throughout. Not all gases diffuse at the same rate, however the lighter the molecule, the more rapid the diffusion process. [Pg.166]

The gases diffusing through the pellet obey the ideal gas law. [Pg.510]

All gases diffuse to fill the space available. In Figure 1.13, after a day the brown-red fumes of gaseous bromine have spread evenly throughout both gas jars from the liquid present in the lower gas jar. [Pg.17]

Gases diffuse at different rates. If one piece of cotton wool is soaked in concentrated ammonia solution and another is soaked in concentrated hydrochloric acid and these are put at opposite ends of a dry glass tube, then after a few minutes a white cloud of ammonium chloride appears (Figure 1.14). This shows the position at which the two gases meet and react. The white cloud forms in the position shown because the ammonia particles are lighter and have a smaller relative molecular mass (Chapter 4, p. 62) than the hydrogen chloride particles (released from the hydrochloric acid) and so move faster. [Pg.17]

Chapter 7 covers the kinetic theory of gases. Diffusion and the one-dimensional velocity distribution were moved to Chapter 4 the ideal gas law is used throughout the book. This chapter covers more complex material. I have placed this material later in this edition, because any reasonable derivation of PV = nRT or the three-dimensional speed distribution really requires the students to understand a good deal of freshman physics. There is also significant coverage of dimensional analysis determining the correct functional form for the diffusion constant, for example. [Pg.225]

Diffusion occurs when one material spreads into or through another. Gases diffuse rapidly and move from one place to another. [Pg.77]

Consider the system shown in Fig. 11-1. A thin partition separates the two gases A and B. When the partition is removed, the two gases diffuse through each other until equilibrium is established and the concentration of the gases is uniform throughout the box. The diffusion rate is given by Fick s law of diffusion, which states that the mass flux of a constituent per unit area is proportional to the concentration gradient. Thus... [Pg.582]

Graham s Law of Effusion states that at the same temperature and pressure, gases diffuse at a rate inversely proportional to the square roots of their molecular masses. What this translates to is that lighter (less dense) gases travel faster than heavier (more dense) gases. [Pg.34]

The permeability of concrete and the rates at which ions and gases diffuse in it are of major importance for durability. We shall consider only the behaviour of cement paste. [Pg.273]


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Advective versus diffusive transfer of noble gases in basins

Air gas-diffusion electrode

Alternative Gas diffusion method

Anode gas diffusion

B Diffusion of Gas Through the Lamellae

Basic Gas-diffusion Separation Systems

Binary gas diffusion

Binary gas diffusivity

Catalyst and gas diffusion layers

Catalyst-coated gas diffusion electrode

Cathode gas diffusion layer

Cells gas diffusion

Characteristic Time for Gas-Phase Diffusion to a Particle

Coefficients Fickian diffusion, gases

Commercial, gas diffusion

Cooling Diffusivity, gases

Diffusion Behavior of Synthesis Gas

Diffusion Coefficients for Binary Ideal Gas Systems

Diffusion Equation for Two-component Gas Mixture (Without and With a Potential Field)

Diffusion and Permeability of Gases

Diffusion coefficient for gases

Diffusion coefficient in gases

Diffusion coefficients for binary gas mixtures

Diffusion coefficients gases

Diffusion gas phase

Diffusion gas transfer

Diffusion gases in water

Diffusion gases into polymers

Diffusion gases into soil

Diffusion in Ideal Gas Mixtures

Diffusion in binary gas mixtures

Diffusion in gas phase

Diffusion in gases

Diffusion in ideal gas

Diffusion of Gases in Porous Solids and Capillaries

Diffusion of Gases in Water

Diffusion of Gases through Polymers and Metals

Diffusion of Gases through Porous Solids

Diffusion of gases

Diffusion of gases and liquids

Diffusion of gases in polymers

Diffusion of ions and gases

Diffusion, gases and

Diffusivities of gases

Diffusivities of gases and vapours

Diffusivity and Solubility of Simple Gases

Diffusivity for gases

Diffusivity in gases

Diffusivity of gases

Diffusivity of gases and liquids

Dry Preparation of PTFE-Bonded Gas Diffusion Electrodes

Dusty Gas Model for Multicomponent Diffusion

Effective gas diffusivity

Electrode-Gas Diffusion Layer

Estimation of Diffusion Coefficients in Gas Mixtures

Estimation of Diffusion Coefficients in Gases

Estimation of Multicomponent Diffusion Coefficients for Gas Mixtures

Estimation of diffusivity in a gas mixture

Estimation of diffusivity in a gas mixture at low density

Estimation of diffusivity in a gas mixture at low pressure

Factors Influencing Mass Transfer in FI Gas-diffusion Separation Systems

Fuel cell gas diffusion layer

Fundamentals of Diffusion in Gases

Gas Diffusion Electrodes with Raney Nickel Catalysts

Gas Diffusion Requirement

Gas Diffusion in Glassy Polymers

Gas Diffusion in a Non-Volatile Liquid

Gas Permeation and Diffusion

Gas concentration diffusion and

Gas diffusion apparatus

Gas diffusion cathode

Gas diffusion electrode

Gas diffusion electrode assembly

Gas diffusion in and through polypropylene

Gas diffusion layer

Gas diffusion layer materials

Gas diffusion media

Gas diffusion method

Gas diffusion models

Gas diffusion process

Gas diffusion, FIA

Gas diffusivity

Gas diffusivity

Gas mixture, diffusion

Gas phase diffusion coefficients

Gas phase diffusivity

Gas translational diffusion

Gas-diffusion Membranes

Gas-diffusion Preconcentration Systems

Gas-diffusion layer durability

Gas-diffusion layer membrane

Gas-diffusion layer properties

Gas-diffusion measurements

Gas-diffusion separation systems

Gas-diffusion separators

Gas-diffusion separators system

Gas-like diffusion

Gas-liquid diffusion layer

Gas-phase diffusion limitation

Gas-solid kinetic processes diffusion control

Gases dense, diffusion coefficients

Gases diffusivities

Gases dilute, diffusion coefficients

Gases gaseous diffusion

High-Field Ion Diffusion in Gas Mixtures

Interbubble gas diffusion

Knudsen Diffusion (Gases)

M. Galinski arbon Materials for Gas Diffusion Electrodes, Metal Air ells and Batteries

Mean Free Path, Diffusion, and Effusion of Gases

Membrane gas diffusivity

Metal supported gas diffusion electrode

Molar mass gas effusion and diffusion

Molecular diffusion in gases

Molecules characterization, diffusion gases

Monatomic gases diffusion coefficient

Multiphenomena in gas diffusion layer

Ordinary Diffusion in Multicomponent Gases

Oxygen Transport Loss in the Gas Diffusion Layer

PEM fuel cell gas diffusion layer

PTFE-Bonded Gas Diffusion Electrodes

Porous gas diffusion electrodes

Prediction of diffusion coefficients in gases, liquids, amorphous solids and plastic materials using an uniform model

Properties gas diffusion coefficients

Solution of the Transient Gas-Phase Diffusion Problem Equations

Solution of the Transient Gas-Phase Diffusion Problem Equations (11.4) to

Solution-Diffusion Model for Single Gas Transport

Solution-Diffusion Model for the Transport of Binary Gas Mixtures

Solution-Diffusion for Gas Mixtures

Spectrophotometric Determination of Total Nitrogen in Soils with On-line Gas-diffusion Separation

Stagnant gases, diffusion through

Steady-State Molecular Diffusion in Gases

The Gas-Diffusion Layer

The Solution and Diffusion of Gases in Elastic Polymers

Theories of gas-diffusion electrodes

Thermal Diffusion of Gases

Thermal diffusivity in the gas phase

Types of Gas Diffusers

Unimodal unidirectional diffusion in gases

Water diffusion of gases

Water transport in gas diffusion layers

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