Biomass steam gasification in fluidized bed of inert or catalytic particles: Comparison between experimental results and thermodynamic equilibrium predictions

In order to improve the understanding of biomass gasification in a bed fluidized by steam, the thermochemical equilibrium of the reactive system was studied. The equilibrium results were compared to LGC experimental results, obtained by the gasification of oak and fir in a laboratory-scale fluidized bed of different catalysts: sand, alumina, and alumina impregnated with nickel. The research was completed by a study of the influence on the equilibrium of additional parameters such as the quantity of steam, the pressure or the kind of biomass. Those results of simulation may be used for evaluating the limits of actual reactors.The following conclusion may be drawn from all the results: The thermodynamic equilibrium state calculated is far away from the experimental results obtained on sand particles. The steam to biomass ratio, between 0.4 and 1 kgsteam/kgdry biomass, has a strong influence on the gas mixture composition. The temperature increase and the use of catalyst allow producing a gas mixture with a high content of hydrogen and carbon monoxide. The H2:CO ratio may reach values greater than 3. The use of catalyst allows the system to get closer from the equilibrium, especially for the nickel based catalyst

Vapogazéification de la biomasse en Lit Fluidisé Circulant : Élaboration des outils théoriques et expérimentaux

Ces travaux concernent l'étude d'un procédé de vapogazéification de biomasse en lit fluidisé circulant. En résultent un ensemble d'outils théoriques (modèles de simulation et de dimensionnement) et expérimentaux (pilote de vapogazéification en lit fluidisé circulant) dans le but de permettre la construction d'un procédé à dimension industrielle. Le dimensionnement, la conception et la construction d'un pilote de vapogazéification de 20 kg/h de biomasse en lit fluidisé circulant ont été réalisés. L'hydrodynamique de ce pilote a été étudiée de manière à isoler les paramètres clés permettant d'en assurer le contrôle. Les résultats obtenus lors de l'opération de pilote ont en outre permis de mieux comprendre les mécanismes d'attrition de particules polydisperses (olivine et char) en lit fluidisé circulant. Pour compléter cette étude, les phénomènes de mélange et de ségrégation des particules ont été étudiés par voie expérimentale et numérique (CFD-3D MFIX). Enfin, un certain nombre de modèles numériques (0D, 1D bulle-émulsion, bilan de population) ont été proposés pour répondre aux besoins techniques d'aide à la conception des lits fluidisés circulants appliqués à la vapogazéification de biomasse. ABSTRACT : The vapogasification of biomass in a Circulating Fluidized Bed has been studied in order to enable the design and the erection of an industrial process. Theoretical and experimental tools have been designed to allow an engineering approach. In order to understand the hydrodynamic behaviour of the reactor, a pilot plant has been designed and erected to feed 20 kg/h of biomass. An exhaustive study of process parameters has been carried out, to determine predominant parameters for the process global control. Operating the built system has also permit to understand attrition phenomenon of polydisperse particles (olivine and char) in the Circulating Fluidized Bed. In order to complete those results, a study of mixing and segregation of those polydisperse particles has been carried out in fluidized bed with both experimental and numerical (CFD-3D MFIX) approaches. A significant contribution has also been done to numerical models assisting biomass vapogasification in Circulating Fluidized Beds design: 0D, 1D, bubble-emulsion, population balance)

Biomass vapogasification in Circulating Fluidized Bed: Development of theoretical and experimental tools

The vapogasification of biomass in a Circulating Fluidized Bed has been studied in order to enable the design and the erection of an industrial process. Theoretical and experimental tools have been designed to allow an engineering approach. In order to understand the hydrodynamic behaviour of the reactor, a pilot plant has been designed and erected to feed 20 kg/h of biomass. An exhaustive study of process parameters has been carried out, to determine predominant parameters for the process global control. Operating the built system has also permit to understand attrition phenomenon of polydisperse particles (olivine and char) in the Circulating Fluidized Bed. In order to complete those results, a study of mixing and segregation of those polydisperse particles has been carried out in fluidized bed with both experimental and numerical (CFD-3D MFIX) approaches. A significant contribution has also been done to numerical models assisting biomass vapogasification in Circulating Fluidized Beds design: 0D, 1D, bubble-emulsion, population balance)

Evaluation of a permeability-porosity relationship in a low permeability creeping material using a single transient test

A method is presented for the evaluation of the permeability-porosity relationship in a low-permeability porous material using the results of a single transient test. This method accounts for both elastic and non-elastic deformations of the sample during the test and is applied to a hardened class G oil well cement paste. An initial hydrostatic undrained loading is applied to the sample. The generated excess pore pressure is then released at one end of the sample while monitoring the pore pressure at the other end and the radial strain in the middle of the sample during the dissipation of the pore pressure. These measurements are back analysed to evaluate the permeability and its evolution with porosity change. The effect of creep of the sample during the test on the measured pore pressure and volume change is taken into account in the analysis. This approach permits to calibrate a power law permeability-porosity relationship for the tested hardened cement paste. The porosity sensitivity exponent of the power-law is evaluated equal to 11 and is shown to be mostly independent of the stress level and of the creep strains

Poromechanical behaviour of hardened cement paste under isotropic loading

The poromechanical behaviour of hardened cement paste under isotropic loading is studied on the basis of an experimental testing program of drained, undrained and unjacketed compression tests. The macroscopic behaviour of the material is described in the framework of the mechanics of porous media. The poroelastic parameters of the material are determined and the effect of stress and pore pressure on them is evaluated. Appropriate effective stress laws which control the evolution of total volume, pore volume, solid volume, porosity and drained bulk modulus are discussed. A phenomenon of degradation of elastic properties is observed in the test results. The microscopic observations showed that this degradation is caused by the microcracking of the material under isotropic loading. The good compatibility and the consistency of the obtained poromechanical parameters demonstrate that the behaviour of the hardened cement paste can be indeed described within the framework of the theory of porous media.Comment: Cement and Concrete Research (2008) In pres

Biomass vapogasification in Circulating Fluidized Bed : Development of theoretical and experimental tools

Ces travaux concernent l'étude d'un procédé de vapogazéification de biomasse en lit fluidisé circulant. En résultent un ensemble d'outils théoriques (modèles de simulation et de dimensionnement) et expérimentaux (pilote de vapogazéification en lit fluidisé circulant) dans le but de permettre la construction d'un procédé à dimension industrielle. Le dimensionnement, la conception et la construction d'un pilote de vapogazéification de 20 kg/h de biomasse en lit fluidisé circulant ont été réalisés. L'hydrodynamique de ce pilote a été étudiée de manière à isoler les paramètres clés permettant d'en assurer le contrôle. Les résultats obtenus lors de l'opération de pilote ont en outre permis de mieux comprendre les mécanismes d'attrition de particules polydisperses (olivine et char) en lit fluidisé circulant. Pour compléter cette étude, les phénomènes de mélange et de ségrégation des particules ont été étudiés par voie expérimentale et numérique (CFD-3D MFIX). Enfin, un certain nombre de modèles numériques (0D, 1D bulle-émulsion, bilan de population) ont été proposés pour répondre aux besoins techniques d'aide à la conception des lits fluidisés circulants appliqués à la vapogazéification de biomasse.The vapogasification of biomass in a Circulating Fluidized Bed has been studied in order to enable the design and the erection of an industrial process. Theoretical and experimental tools have been designed to allow an engineering approach. In order to understand the hydrodynamic behaviour of the reactor, a pilot plant has been designed and erected to feed 20 kg/h of biomass. An exhaustive study of process parameters has been carried out, to determine predominant parameters for the process global control. Operating the built system has also permit to understand attrition phenomenon of polydisperse particles (olivine and char) in the Circulating Fluidized Bed. In order to complete those results, a study of mixing and segregation of those polydisperse particles has been carried out in fluidized bed with both experimental and numerical (CFD-3D MFIX) approaches. A significant contribution has also been done to numerical models assisting biomass vapogasification in Circulating Fluidized Beds design: 0D, 1D, bubble-emulsion, population balance)

Biomass vapogasification in Circulating Fluidized Bed (Development of theoretical and experimental tools)

Ces travaux concernent l'étude d'un procédé de vapogazéification de biomasse en lit fluidisé circulant. En résultent un ensemble d'outils théoriques (modèles de simulation et de dimensionnement) et expérimentaux (pilote de vapogazéification en lit fluidisé circulant) dans le but de permettre la construction d'un procédé à dimension industrielle. Le dimensionnement, la conception et la construction d'un pilote de vapogazéification de 20 kg/h de biomasse en lit fluidisé circulant ont été réalisés. L'hydrodynamique de ce pilote a été étudiée de manière à isoler les paramètres clés permettant d'en assurer le contrôle. Les résultats obtenus lors de l'opération de pilote ont en outre permis de mieux comprendre les mécanismes d'attrition de particules polydisperses (olivine et char) en lit fluidisé circulant. Pour compléter cette étude, les phénomènes de mélange et de ségrégation des particules ont été étudiés par voie expérimentale et numérique (CFD-3D MFIX). Enfin, un certain nombre de modèles numériques (0D, 1D bulle-émulsion, bilan de population) ont été proposés pour répondre aux besoins techniques d'aide à la conception des lits fluidisés circulants appliqués à la vapogazéification de biomasse.The vapogasification of biomass in a Circulating Fluidized Bed has been studied in order to enable the design and the erection of an industrial process. Theoretical and experimental tools have been designed to allow an engineering approach. In order to understand the hydrodynamic behaviour of the reactor, a pilot plant has been designed and erected to feed 20 kg/h of biomass. An exhaustive study of process parameters has been carried out, to determine predominant parameters for the process global control. Operating the built system has also permit to understand attrition phenomenon of polydisperse particles (olivine and char) in the Circulating Fluidized Bed. In order to complete those results, a study of mixing and segregation of those polydisperse particles has been carried out in fluidized bed with both experimental and numerical (CFD-3D MFIX) approaches. A significant contribution has also been done to numerical models assisting biomass vapogasification in Circulating Fluidized Beds design: 0D, 1D, bubble-emulsion, population balance).TOULOUSE-INP (315552154) / SudocSudocFranceF

Mélange et ségrégation en lit fluidisé dense de particules de media fluidisé (olivine) et de granules de biomasse

Ce travail, réalisé dans le cadre du projet GAYA et soutenu par l’ADEME, est consacré à l’étude du mélange et ségrégation en lit fluidisé dense. La fluidisation gaz-solide est de plus en plus appliquée pour la mise en œuvre de procédés physiques ou réactionnels faisant intervenir des matériaux divisés de nature, de forme et/ou de taille hétérogènes. Les phénomènes de mélange et de ségrégation engendrés doivent être connus afin de parfaitement contrôler les procédés mis en jeu au sein de ces réacteurs, notamment dans le cas de la pyrolyse et de la gazéification de la biomasse. Ce papier présente des résultats expérimentaux concernant l’étude hydrodynamique de mélanges binaires d’olivine et de biomasse. Des mesures de concentration de biomasse le long du lit sont réalisées à partir d’une méthode dite de « lit figé et sectionné » et montrent que le niveau de ségrégation est intimement lié à la vitesse de fluidisation. Ces mesures expérimentales sont comparées à des résultats de simulations numériques 3D réalisées à partir d’une approche de type eulérienne n-fluides implantée dans un code CFD multiphasique, réactif, volumes finis, parallèle et non structuré. Les comparaisons réalisées entre les mesures expérimentales de l’indice de mélange et les résultats des simulations numériques sont en relativement bon accord pour les vitesses de fluidisation élevées. Toutefois, les modèles mathématiques utilisés pour la simulation numérique ne permettent pas de représenter la ségrégation observée expérimentalement pour de faibles vitesses de fluidisation

Marine Polyether Phycotoxin Palytoxin Induces Apoptotic Cell Death via Mcl-1 and Bcl-2 Downregulation

Palytoxin is considered one of the most potent biotoxins. As palytoxin-induced cancer cell death mechanisms remain to be elucidated, we investigated this effect on various leukemia and solid tumor cell lines at low picomolar concentrations. As palytoxin did not affect the viability of peripheral blood mononuclear cells (PBMC) from healthy donors and did not create systemic toxicity in zebrafish, we confirmed excellent differential toxicity. Cell death was characterized by a multi-parametric approach involving the detection of nuclear condensation and caspase activation assays. zVAD-sensitive apoptotic cell death was concomitant with a dose-dependent downregulation of antiapoptotic Bcl-2 family proteins Mcl-1 and Bcl-xL. Proteasome inhibitor MG-132 prevented the proteolysis of Mcl-1, whereas the three major proteasomal enzymatic activities were upregulated by palytoxin. Palytoxin-induced dephosphorylation of Bcl-2 further exacerbated the proapoptotic effect of Mcl-1 and Bcl-xL degradation in a range of leukemia cell lines. As okadaic acid rescued cell death triggered by palytoxin, protein phosphatase (PP)2A was involved in Bcl-2 dephosphorylation and induction of apoptosis by palytoxin. At a translational level, palytoxin abrogated the colony formation capacity of leukemia cell types. Moreover, palytoxin abrogated tumor formation in a zebrafish xenograft assay at concentrations between 10 and 30 pM. Altogether, we provide evidence of the role of palytoxin as a very potent and promising anti-leukemic agent, acting at low picomolar concentrations in cellulo and in vivo