Defect and Diffusion Forum
Vols. 283-286
Vols. 283-286
Defect and Diffusion Forum
Vol. 282
Vol. 282
Defect and Diffusion Forum
Vols. 280-281
Vols. 280-281
Defect and Diffusion Forum
Vol. 279
Vol. 279
Defect and Diffusion Forum
Vol. 278
Vol. 278
Defect and Diffusion Forum
Vol. 277
Vol. 277
Defect and Diffusion Forum
Vols. 273-276
Vols. 273-276
Defect and Diffusion Forum
Vol. 272
Vol. 272
Defect and Diffusion Forum
Vols. 269-271
Vols. 269-271
Defect and Diffusion Forum
Vol. 268
Vol. 268
Defect and Diffusion Forum
Vol. 267
Vol. 267
Defect and Diffusion Forum
Vol. 266
Vol. 266
Defect and Diffusion Forum
Vol. 265
Vol. 265
Defect and Diffusion Forum Vols. 273-276
Paper Title Page
Abstract: In order to model the diffusion in multicomponent and multiphase systems
we define and use the volume fixed frame of reference. In this unique frame all
diffusion fluxes are expressed by the combined Darken-Nernst-Planck formulae. The
components mobility is estimated using the NIST data and Calphad approach. The
resulting CADiff method is used for the modeling (inter)diffusion process in the
multicomponent diffusion multiple. We shows results for the IN718-Rene88 terminal
compositions. Comparison of the simulation results with experimental data shows
good agreement. The presented CADiff method allows to model interdiffusion in
multicomponent non-ideal systems. When the thermodynamical data are available,
the method allows to include reactions, variable partial molar volumes and effect of
stress.
105
Abstract: Numerical simulations of evolution of the potentials and impedance spectra of ionselective
membranes (ISEs) with ionic sites are presented. The Nernst–Planck–Poisson and
continuity equations (NPP) are solved numerically by means of the finite difference method, the
Rosenbrock solver and with the use of Matlab platform. Transient solutions for ion-selective
electrodes under open- and closed-circuit conditions are computed. The potential-time response to
small-current perturbation is used for determination of complex impedances. We present
simulations of ISEs as a function of varying diffusivities and ionic concentrations in the “bathing”
solutions at interfaces. It is shown that the non-Nernstian behavior of passive membrane electrodes
is a result of kinetic constraints at the interfaces, which is manifested in the appearance of an
additional arc between the high-frequency bulk and the low-frequency (Warburg) arcs. The
presented approach directly relates the diffusivities in the membrane and the interface properties
(heterogeneous rate constants determining the transport across interfaces) to the characteristic
features of impedance spectra (dimensions and characteristic radial frequencies). NPP problem
solved on the Matlab platform allows simulating of the non-linear effects in electro-diffusion.
113
Abstract: Increase of the emission of CO2, which is mostly the result of the combusted fossil
fuels into the atmosphere, exponentially increases. Through increased energy efficiency there is
lower CO2 emission. There is a tendency to reduce exhaust gases temperatures down from their
original value referred to as “acid dew point”, 115-160°C. A result is vapor condensation of wet
flue in chimney. Condensation occurs when the surface temperature is below the dew point of the
vapor-gas mixture. Therefore, Vapor-Liquid Equilibrium models are required in order to determine
the dew point of the mixture. Wet flue gas is simulated with vapor-air mixture. A numerical model
was presented to calculate the velocity and thermal field of turbulent vapor-air mixture flow trough
a chimney. The momentum and temperature field were calculated via a finite-volume CFD code,
using the k – e turbulence model. The validation of this calculation was conducted employing an
experimental set for heat and mass transfer in vertical upward vapor-air mixture. Measurements
were done using a stainless steel tube of 13.2 mm I.D. (internal diameter) and 70 I.D. lengths. Flow
rates of steam and air were varied as the experimental parameters.
The experiment involves two-phase, two-component, heat and mass transfer. Comparisons of wall
temperature and condensate rate were made and the model was shown to give an acceptable results.
119
Abstract: A series of biodegradable superabsorbent polymers (SAP’s) based on starch grafted with
acrylic acid (AA) and crosslinked with N,N’-methylenebisacrylamide (MBIS) were obtained. The
parameters that define SAP’s properties, such as starch type, amount of initiator, acrylic acid and
crosslinker concentrations, and degree of neutralization were varied.
The dynamic swelling was interpreted in terms of both a simple power of time equation and a
more detailed model based on a coupled diffusion–relaxation mechanism. The diffusivity
coefficients calculated from diffusion–relaxation model were compared with the microimages
obtained by optical microscopic.
126
Abstract: Mass transfer around a slightly soluble cylinder, aligned with the direction of liquid flow
in a packed bed of sand particles, is analysed for transport by advection and molecular diffusion.
The theoretical analysis applies to cylinders that are large in comparison with the inert particles, so
that the bed may be treated as a continuum.
Experimental measurements of mass transfer in water were carried out at temperatures that differ
significantly from ambient value. The soluble cylinders used in the experiments were made of either
salicylic acid or cinnamic acid and the range of temperatures covered were 278 to 343 K, for the
dissolution of salicylic acid, and 278 to 328 K, for cinnamic acid in water. Using the mass transfer
theory presented in this work the molecular diffusion coefficient of the two solutes was determined,
and good agreement with literature values was found.
132
Abstract: Osmotic dehydration of pumpkin (Cucurbita pepo, L.) fruits was carried out with binary
solutions of sucrose and NaCl at different temperatures and solute concentrations. Water loss and
solids gain kinetics were experimentally determined and fitted using a diffusional model. Pumpkins
samples were considered as finite cylinders and the analytical solution of the unsteady diffusion
equation was used considering the external resistance to the mass transfer negligible. The influence
of shrinkage and temperature on the effective diffusion coefficients was also assessed in this work.
138
Abstract: This study considers numerical simulations of the combustion of propane with air, in a
burner element due to high temperature and velocity gradients in the combustion chamber. The
effects of equivalence ratio (φ) and oxygen percentage (γ) in the combustion air are investigated for
different values of φ between 0.5 and 1.0 and γ between 10 and 30%. In each case, combustion is
simulated for the fuel mass flow rate resulting in the same heat transfer rate (Q) to the combustion
chamber.
Numerical calculations are performed individually for all cases with the use of the Fluent CFD
code. The results shown that the increase of equivalence ratio corresponds to a significantly
decrease in the maximum reaction rates and the maximum temperature increase with the increases
of oxygen percentage. Mixing hydrogen with propane causes considerable reduction in temperature
levels and a consequent reduction of CO emissions.
144
Abstract: Moisture is an important factor when analyzing the behaviour of building elements and
materials. A deeper knowledge on moisture transport under transient conditions of environmental
air temperature and humidity is required. In this experimental work, the measurements of moisture
diffusion coefficients, w D , of three different types of building materials commonly used in Portugal
(gypsum plasterboard, gypsum plaster and gypsum+lime plaster) were obtained for different values
of temperature and relative humidity.
The results obtained were in good agreement with the values found in literature and show that
the increase in temperature resulted in an increase in the diffusion coefficient and an increase in
relative humidity (54% to 69%) resulted in a decrease in w D .
150
Abstract: The sorption and transport of water in two porous building materials, clay brick and
autoclaved aerated concrete, was studied in detail. The evolution of the distribution of liquid in the
porous medium was analysed in terms of the Boltzmann transform method and anomalous diffusion
equation proposed by Küntz and Lavallée [1].
The apparent moisture diffusion coefficients of water were determined from the total water
profiles using a modified Boltzmann-Matano analysis, and a good agreement with literature values
was found. The application of anomalous diffusion model to building materials indicates that the
previous 1/ 2 t relation is not entirely accurate to estimate the volume of absorbed water. This result
has particular relevance for evaluating the durability of building structures.
156
Abstract: This work describes an experimental and numerical study to determine the corresponding
detailed thermal and fluid dynamic fields developed in a burner element for domestic water heaters.
A three-dimensional burner element was designed in real scale and numerical studies using
Fluent code were carried out in steady-state conditions to allow continuous observations and
measurements of the influence of burner element geometry and fuel-air velocity on flame
characteristics, namely colour, length and stability. Air has been used as a fluid. The computational
results, specifically the velocity and flame characteristics were verified with experimental data
obtained in order to ensure a stable flame. In order to evaluate the power generated and the
emissions of CO2 and CO associated to different burner element geometries, some experiments
were performed using single burner elements with a stainless steel prismatic tank covered with
thermal insulation to minimize heat losses.
162