Master of Science / Department of Civil Engineering / Kyle Riding / Corrosion of reinforcing steel is one of the most common and serious causes of reinforced concrete deterioration. While corrosion is normally inhibited by a passive layer that develops around the reinforcing steel due to the high pH environment of the surrounding concrete, chlorides will break down this protective layer, leading to reinforcement corrosion. Decreasing the diffusivity of the concrete would slow the ingress of chlorides into concrete, and is one of the most economical ways to increase the concrete service life. Optimized concrete mixtures blending portland cement and supplementary cementing materials (SCMs) have become popular throughout the construction industry as a method of improving both fresh and long-term concrete properties such as workability, strength and porosity. It has been shown that use of Class F fly ash, silica fume and ground granulated blast furnace slag (GGBFS) in binary concrete mixture blends can result in a significant reduction in concrete diffusivity. This study investigates the ability of Class C fly ash and ternary concrete mixture blends to also aid in diffusivity reduction. In order to study the effect of incorporation of SCMs into concrete, mixtures containing Class C and Class F fly ash, silica fume and GGBFS were tested following the ASTM C 1556 procedures to measure the concrete’s apparent chloride diffusivity. Structure life cycles were modeled using the measured apparent chloride diffusivities with two finite-difference based life-cycle analysis software packages. To determine whether a correlation between diffusivity and deterioration due to freezing and thawing exists, samples were also tested for their ability to resist deterioration from freezing and thawing cycles using a modified ASTM C 666 Procedure B test. Results show that the use of Class C fly ash yields some service life improvements as compared to the portland cement control mixtures, while ternary mixture blends performed significantly better than the control mixture and equal to or better than the binary SCM mixtures tested. Freeze-thaw tests showed all mixtures to be equally resistant to deterioration due to freezing and thawing.

Le problème dans cette étude est celui de l’incorporation de la gomme Grewia mollis dans le mélange blé-taro avec pour objet d’améliorer le taux de substitution du blé par la farine de taro qui, selon la littérature, ne peut dépasser de valeurs allant de 10 à 15 % sans altérer de façon considérable la qualité de la pâte de pain. Les objectifs définis dans cette étude sont triples : (1) d’abord connaitre les propriétés de la farine de taro variété Lamba qui, avant cette étude n’a pas fait l’objet d’études antérieures. (2) Déterminer les conditions optimales d’extraction de la gomme Grewia, dont on connait de la littérature les caractéristiques physicochimiques et fonctionnelles et pas les meilleures conditions d’extraction. (3) Etudier dans un plan de mélange à trois composantes l’effet du pourcentage de gomme, de farine de taro et blé sur les propriétés rhéologiques et sensorielles de la pâte et du pain. Dans cette étude les méthodes usuelles de caractérisation ont été utilisées. Pour l’objectif 1, le dispositif expérimental prend en compte la taille du tubercule (4 modalités) comme facteurs, et les paramètres mesurés sont : la composition proximale, la granulométrie et la forme de particules, les propriétés thermiques et rhéologiques de la farine. Pour l’objectif 2, la gomme est extraite selon un plan composite centré à faces centrées avec comme facteurs le ratio volume d’eau sur masse de la poudre de l’écorce, la température et le temps d’extraction, et les réponses sont la viscosité de la solution et le taux d’extraction. Une caractérisation du profil de sucres de la gomme a été faite. Pour l’objectif 3, un plan de mélange ternaire Grewia-taro-blé à contraintes a été effectué. Le volume de pousse de la pâte, le test de double morsure, le test du fluage-recouvrement ont été mesurés sur la pâte, alors que les pains obtenus ont fait l’objet d’une analyse du test de double compression et d’acceptabilité. Les résultats de l’objectif 1 ont montré que la composition physicochimique du taro varie en fonction de la masse et du pelage, le profil en acide aminé présente une absence des acides aminés soufrés. Les résultats de l’extraction de la gomme dans l’objectif 2 ont montré que seul le ratio augmente significativement la viscosité et le rendement d’extraction de la gomme. Les conditions optimales d’extraction de la gomme Grewia mollis sont les suivantes: pH: 7,1 temps : 1h température: 73,1 °C ratio eau / poudre : 55,4 / 1, pour une viscosité de 0,98 Pa.s et un rendement de 0,32%. Les résultats de l’objectif 3 montrent que l’augmentation de la gomme Grewia mollis entraine une augmentation de la capacité d’absorption d’eau des farines mélangées, une augmentation de la viscoélasticité, du volume de pousse, du volume de pain, de l’acceptabilité générale jusqu’à un seuil de 2,5% puis une baisse est observée. Les analyses de corrélation ont montré que l’augmentation de la capacité d’absorption d’eau entraine une baisse des paramètres du fluage et du recouvrement de la pâte, du volume de pousse / The problem in this study is the incorporation of Grewia gum in the wheat-taro mixture in order to improve the level of substitution of wheat flour by taro flour which, according to the literature, cannot exceed 10-15% without deteriorating in a considerable manner the quality of the bread paste. The objective defined in this study is threefold : (1) to know the properties of the flour of taro Lamba variety which, before this study have not been the object for research (2) to determine the optimum conditions for extraction of the Grewia gum, with known physico-chemical and functional characteristics but no standard for conditions extraction. (3) To study the effect of the percentage of gum, taro flour and wheat flour on the rheological and sensory properties of the paste and the bread using a mixture designs with three components. In this study the usual methods of characterization were used. For objective 1, the experimental device takes into account sizes of tuber (4 weight) like factors, and the measured parameters are: the proximate composition, the granulometry and the shape of particles, thermal and rheological properties of the flour. For objective 2, the gum is extracted using a central composite design with faces centered with factors like the flour water ratio (w / w), the temperature, extraction time and pH, the response were the viscosity of the solution and the yield of extraction. A characterization of the sugar profile of gum was made. For objective 3, a ternary mixture design Grewia - taro-wheat with constraints was carried out. The volume of dough, the rheology of paste, the double bite test, the creep-recovering test were measured on the dough, whereas a double compression test analysis and acceptability were carried out on the bread. The results of objective 1 showed that the physico-chemical composition of the taro varies as a function of the mass and peeling type, the amino acid profile reveals the absence of sulphur amino acids. The results of the extraction of gum showed that only the ratio significantly increases the viscosity and the yield of the gum.The optimum conditions for extraction of the Grewia gum are as follows:pH: 7.1 times : 1h temperature: 73 °C water / powder ratio: 55.4 / 1, for a viscosity of 0.98 Pa.s and and yield of 0.32 %. The results of objective 3 show that the incorporation of gum increase the water absorption capacity, viscoelasticity of the dough, volume of the dough and even volume of bread. However the sensory analysis showed that the addition of gum up to 5% contributed to the rejection of the breads

The convective drying of thin layers of multicomponentliquid mixtures into an inert gas, and the influence ofdifferent process controlling mechanisms on drying selectivityis studied. Drying experiments under gas-phase-controlledconditions are performed by low intensity evaporation, fromfree liquid surfaces, of ternary mixtures without non-volatilesolutes. Liquid-side-controlled experiments are carried out bydrying a multicomponent polymeric solution containing twovolatile components, one non-volatile polymer and an optionalnonvolatile softening substance. Mathematical models to describe gas- andliquid-side-controlled drying based on interactive diffusion inboth liquid and gas phases as the main mechanisms for masstransfer are developed. For gas-phase-controlled drying, astability analysis of the ordinary differential equations thatdescribes the evaporation process is performed. Isothermal andnon-isothermal drying processes are considered in batch andcontinuous modes. The mathematical model to describe thecomposition profiles during batch drying of the polymeric film,considering liquid resistance, is solved numerically. Due tothe lack of experimental data, properties for this polymericsystem are estimated by using established methods. Ananalytical solution of the diffusion equation, by assuming anisothermal drying process and a constant matrix ofmulticomponent diffusion coefficients is developed. For thecontinuous case, liquid-side resistance is studied by modellingevaporation of a multicomponent falling liquid film into aninert gas including indirect heating. The results of the gas-phase-controlled model are in goodagreement with experimental results. For the polymeric film,the agreement is only qualitative since the model does notaccount for a membrane that develops on the film surface. Thestability analysis permits the prediction of trajectories andfinal state of a liquid mixture in a gas-phase-controlleddrying process. For isothermal evaporation of ternary mixturesinto pure gas, the solutions are trajectories in the phaseplane represented by a triangular diagram of compositions. Thepredicted ternary dynamic azeotropic points are unstable orsaddle. On the other hand, binary azeotropes are stable whenthe combination of the selectivities of the correspondingcomponents is negative. In addition, pure component singularpoints are stable when they are contained within theirrespective isolated negative selectivity zones. Undernon-isothermal conditions, maximum temperature valuescharacterise stable azeotropes. Incremental loading of the gaswith one or more of the components leads to a node-saddlebifurcation, where a saddle azeotrope and a stable azeotropecoalesce and disappear. For continuous drying, the singularpoints are infinite and represent dynamic equilibrium pointswhose stability is mainly dependent on the ratio of inletgas-to-liquid flow rates. As long as the process isgas-phasecontrolled, these results also apply to a porous solidcontaining a liquid mixture. In general, liquid-side control makes the drying processless selective but it is difficult to maintain this conditionduring the whole process. Under the influence of its owndynamics, a process starting as liquid-side-controlled tendstowards a gas-phase-controlled process. The presence ofnon-volatile components and indirect heating may delay thisdevelopment. Considering the evolution of the processcontrolling steps and its influence on selectivity, a modelaimed at describing the complete trajectory of a drying orevaporation process must include the coexistence of allrelevant mechanisms. Keywords:ternary mixture, falling film, diffusionequation, gas-phase control, liquid-phase control, selectivity,stability analysis, polymeric solution, evaporation, azeotrope,batch drying, continuous drying.

<p>The convective drying of thin layers of multicomponentliquid mixtures into an inert gas, and the influence ofdifferent process controlling mechanisms on drying selectivityis studied. Drying experiments under gas-phase-controlledconditions are performed by low intensity evaporation, fromfree liquid surfaces, of ternary mixtures without non-volatilesolutes. Liquid-side-controlled experiments are carried out bydrying a multicomponent polymeric solution containing twovolatile components, one non-volatile polymer and an optionalnonvolatile softening substance.</p><p>Mathematical models to describe gas- andliquid-side-controlled drying based on interactive diffusion inboth liquid and gas phases as the main mechanisms for masstransfer are developed. For gas-phase-controlled drying, astability analysis of the ordinary differential equations thatdescribes the evaporation process is performed. Isothermal andnon-isothermal drying processes are considered in batch andcontinuous modes. The mathematical model to describe thecomposition profiles during batch drying of the polymeric film,considering liquid resistance, is solved numerically. Due tothe lack of experimental data, properties for this polymericsystem are estimated by using established methods. Ananalytical solution of the diffusion equation, by assuming anisothermal drying process and a constant matrix ofmulticomponent diffusion coefficients is developed. For thecontinuous case, liquid-side resistance is studied by modellingevaporation of a multicomponent falling liquid film into aninert gas including indirect heating.</p><p>The results of the gas-phase-controlled model are in goodagreement with experimental results. For the polymeric film,the agreement is only qualitative since the model does notaccount for a membrane that develops on the film surface. Thestability analysis permits the prediction of trajectories andfinal state of a liquid mixture in a gas-phase-controlleddrying process. For isothermal evaporation of ternary mixturesinto pure gas, the solutions are trajectories in the phaseplane represented by a triangular diagram of compositions. Thepredicted ternary dynamic azeotropic points are unstable orsaddle. On the other hand, binary azeotropes are stable whenthe combination of the selectivities of the correspondingcomponents is negative. In addition, pure component singularpoints are stable when they are contained within theirrespective isolated negative selectivity zones. Undernon-isothermal conditions, maximum temperature valuescharacterise stable azeotropes. Incremental loading of the gaswith one or more of the components leads to a node-saddlebifurcation, where a saddle azeotrope and a stable azeotropecoalesce and disappear. For continuous drying, the singularpoints are infinite and represent dynamic equilibrium pointswhose stability is mainly dependent on the ratio of inletgas-to-liquid flow rates. As long as the process isgas-phasecontrolled, these results also apply to a porous solidcontaining a liquid mixture.</p><p>In general, liquid-side control makes the drying processless selective but it is difficult to maintain this conditionduring the whole process. Under the influence of its owndynamics, a process starting as liquid-side-controlled tendstowards a gas-phase-controlled process. The presence ofnon-volatile components and indirect heating may delay thisdevelopment. Considering the evolution of the processcontrolling steps and its influence on selectivity, a modelaimed at describing the complete trajectory of a drying orevaporation process must include the coexistence of allrelevant mechanisms.</p><p><b>Keywords:</b>ternary mixture, falling film, diffusionequation, gas-phase control, liquid-phase control, selectivity,stability analysis, polymeric solution, evaporation, azeotrope,batch drying, continuous drying.</p>

A mathematical model for the drying of particulate solids in a continuous vibrated fluidised bed dryer was developed and applied to the drying of grain wetted with a single liquid and porous particles containing multicomponent liquid mixtures. Simple equipment and material models were applied to describe the process. In the plug-flow equipment model, a thin layer of particles moving forward and well mixed in the direction of the gas flow was regarded; thus, only the longitudinal changes of particle moisture content and composition as well as temperature along the dryer were considered. Concerning the material model, mass and heat transfer in a single isolated particle was studied. For grain wetted with a single liquid, mass and heat transfer within the particles was described by effective transfer coefficients. Assuming a constant effective mass transport coefficient and effective thermal conductivity of the wet particles, analytical solutions of the mass and energy balances were obtained. The variation of both transport coefficients along the dryer was taken into account by a stepwise application of the analytical solution in space intervals with non-uniform inlet conditions and averaged coefficients from previous locations in the dryer. Calculation results were verified by comparison with experimental data from the literature. There was fairly good agreement between experimental data and simulation but the results depend strongly on the correlation used to calculate heat and mass transfer coefficients.   For the case of particles containing a multicomponent liquid mixture dried in the vibrated fluidised bed dryer, interactive diffusion and heat conduction were considered the main mechanisms for mass and heat transfer within the particles. Assuming a constant matrix of effective multicomponent diffusion coefficients and thermal conductivity of the wet particles, analytical solutions of the diffusion and conduction equations were obtained. The equations for mass transfer were decoupled by a similarity transformation and solved simultaneously with conduction equation by the variable separation method. Simulations gave a good insight into the selectivity of the drying process and can be used to find conditions to improve aroma retention during drying.   Also, analytical solutions of the diffusion and conduction equations applied to liquid-side-controlled convective drying of a multicomponent liquid film were developed. Assuming constant physical properties of the liquid, the equations describing interactive mass transfer are decoupled by a similarity transformation and solved simultaneously with conduction equation and the ordinary differential equation that describes the changes in the liquid film thickness. Variations of physical properties along the process trajectory were taken into account as in the previous cases. Simulation results were compared with experimental data from the literature and a fairly good agreement was obtained. Simulations performed with ternary liquid mixtures containing only volatile components and ternary mixtures containing components of negligible volatility showed that it is difficult to obtain an evaporation process that is completely controlled by the liquid-side mass transfer. This occurs irrespective of the initial drying conditions.   Despite simplifications, the analytical solution of the material model gives a good insight into the selectivity of the drying process and is computationally fast. The solution can be a useful tool for process exploration and optimisation. It can also be used to accelerate convergence and reduce tedious and time-consuming calculations when more rigorous models are solved numerically. / QC 20110614

This study investigated the transport coefficients involved in mass and heat transfer during the drying of a porous solid partially saturated with multicomponent mixtures.  It included the coefficients governing liquid transport through the solid, the matrix of multicomponent diffusion coefficients in the liquid phase, and the effective thermal conductivity.  As it is not possible to determine these coefficients by theoretical considerations alone and considerable experimental work is required to determine them in a broad range of process conditions, the principle of this study has been the use of mathematical models complemented with some empirical parameters.  These empirical parameters were determined by comparison between measurements in specially designed experiments and the results of mathematical models that describe the process.  In addition, the application of the multicomponent diffusion coefficients is described in two cases where liquid diffusion is important: convective evaporation of a multicomponent stationary liquid film and a falling film. To study liquid transport through the solid, isothermal drying experiments were performed to determine the transient composition profiles and total liquid content of sand samples wetted with ternary liquid mixtures with different initial compositions and temperatures.  A mathematical model including mass transfer by capillary movement of the liquid and interactive diffusion in both the gas and liquid phases was developed.  To simulate the capillary movement of liquid mixtures, parameters experimentally determined for single liquids were weighed according to liquid composition. A fairly good agreement between theoretical and experimental liquid composition profiles was obtained considering that axial dispersion was included in the model. To study the matrix of multicomponent diffusion coefficients in the liquid phase, the redistribution of liquid composition in a partially filled tube exposed to a longitudinal temperature gradient was analysed.  Experimental work was carried out using two main ternary mixtures with different initial compositions and temperature gradients.  Experimental data were compared with the results of a theoretical model that describes the steady-state liquid composition distribution in a partially filled non-isothermal tube to find the empirical exponent that modifies the matrix of thermodynamic factors.  Correlations for the exponents as a function of temperature were determined for each particular multicomponent mixture. The effective thermal conductivity of a porous solid containing multicomponent liquid mixtures was studied by measuring the liquid composition, liquid content and temperature distributions in a cylindrical sample dried by convection from the open upper side and heated by contact with a hot source at the bottom side.  Simulations performed at a quasi steady state were compared with experiments to estimate the adjusting geometric parameter of Krischer’s model for effective thermal conductivity, which includes the contribution of the evaporation-diffusion-condensation mechanism. The results revealed that a resistance corresponding to a parallel arrangement between the phases seems to dominate in this case. In the study of the convective drying of a multicomponent stationary liquid film, the equations describing interactive mass transfer were decoupled by a similarity transformation and solved simultaneously with a conduction equation by the method of variable separation.  Variations of physical properties along the process trajectory were taken into account by a stepwise application of the solution in time intervals with averaged coefficients from previous time steps.  Despite simplifications, the analytical solution gives a good insight into the selectivity of the drying process and is computationally fast.  On the other hand, numerical simulations of the convective evaporation of the multicomponent falling liquid film into an inert gas with a co-current flow arrangement of the phases almost always revealed a transition from liquid-phase-controlled conditions to a process in which neither the gas nor the liquid completely controls the evaporation. The results obtained in this work would be useful in implementing models to improve the design, process exploration and optimisation of dryers by incorporating the solid-side effects to describe the drying of liquid mixtures along the whole process. / QC 20110124

Afin d’améliorer le recyclage des thermoplastiques, de nouveaux mélanges sont étudiés pour élargir les débouchés offerts à ces matériaux. Ils visent à combiner efficacement les contributions de deux dispersions de polyéthylène (PE) et de polyamide (PA) pour renforcer les propriétés d’une matrice polypropylène (PP). Des stratégies de compatibilisation spécifiques à chaque phase minoritaire sont mises en place. Elles permettent d’élaborer en une seule étape d’extrusion réactive un mélange de deux dispersions nodulaires submicroniques et indépendantes. Grâce aux interphases de copolymères polyoléfines entourant le PE, ces particules facilitent l’écoulement plastique des macromolécules de PP avoisinantes à la place de la fissuration de la matrice. Entre le PP et le PA, deux compatibilisations différentes sont appliquées. Celle utilisant le polypropylène greffé d’anhydride maléique (PPgMA) forme une interface rigide et cohésive. Le module et la tenue en température supérieure du polyamide se répercutent alors sur les propriétés du mélange sans pour autant provoquer de fragilisation du matériau à température ambiante grâce à l’effet toujours efficace des particules de PE permettant de dissiper les contraintes concentrées autour du PA. Une compatibilisation alternative à base de poly(styrène-bloc-(éthylène-co-butylène)-bloc-styrène) greffé d’anhydride maléique (SEBSgMA) forme une interphase souple autour des particules de PA. Au lieu d’augmenter le module des mélanges, cette dispersion se comporte alors elle aussi comme un modifiant choc souple et augmente la déformabilité du mélange. Il est possible de tirer profit de la morphologie hétérogène du matériau pour localiser préférentiellement des particules de talc dans la phase PA des mélanges ternaires et ainsi minimiser le contact entre la charge et la matrice. Ainsi, les cavités formées par décohésion de l’interface charge/polymère restent confinées au sein d’une phase dispersée ce qui minimise leur impact sur la déformabilité du mélange. Le module d’Young de la phase PA est par contre augmenté ce qui se fait sentir sur le composite dans son ensemble. Une telle démarche permet de combiner rigidité et ténacité dans un mélange hétérogène de polymères. / In order to increase thermoplastic polymer recycling, new blends are studied to open-up new prospects for such materials. The objective is to efficiently combined the effects of two minor phases of polyethylene (PE) and polyamide (PA) to tune the properties of a polypropylene matrix (PP). Specific compatibilisation strategies adapted to each minor phase are established. They allow the self-arrangement in only one step of reactive-extrusion of a controlled morphology with two nodular and independent particle populations finely dispersed in the PP based blend. Thanks to the polyolefin copolymer interphases around PE, these particles promote PP shear yielding instead of matrix crazing. Two different compatibilisation routes are applied at PP/PA interface. The one using maleic anhydride grafted polypropylene (PPgMA) forms strong bonds between the two homopolymers and a stiff interface. In this case, the higher PA Young’s modulus strengthens the entire blend without inducing brittleness at room temperature thanks to the presence of the PE particles acting as stress dissipater around PA nodules. The alternative compatibilisation based on maleic anhydride grafted styrene-ethylene-buthylene-styrene bloc copolymer (SEBSgMA) creates a soft interphase around PA particles. Instead of heighten the blend modulus, this compatibilizer makes the PA particles appear very flexible and act as an impact modifier, and therefore increases the deformation capability of the blend. It is possible to take advantage of the heterogeneous morphology of the ternary polymer blend to design particular composites. Inorganic particles such as talc can be preferentially localized in the PA particles of the blend, minimizing contacts between the filler and the PP matrix. Thus, the cavities due to polymer/filler interface debonding stay confined within a dispersed phase which prevent their growth and the apparition of a catastrophic fracture. On the other hand, talc increases the Young’s modulus of PA particles and consequently the modulus of the entire composite. The design of such a heterogeneous material allows the increase of both strength and toughness simultaneously.

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