704 resultados para Etch adhesives


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Do presente trabalho resultou a submissão de um artigo, com o título UV Curing Adhesives for Conservation of Glass- Chemical and Mechanical Stability, para comunicação oral em conferência internacional intitulada Recent Advances in Glass and Ceramics Conservation, a ocorrer em Wroclaw, Polónia, de 25 a 29 de Maio de 2016, no âmbito do ICOM-CC Glass and Ceramics Working Group Interim Meeting.

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En lien avec l’avancée rapide de la réduction de la taille des motifs en microfabrication, des processus physiques négligeables à plus grande échelle deviennent dominants lorsque cette taille s’approche de l’échelle nanométrique. L’identification et une meilleure compréhension de ces différents processus sont essentielles pour améliorer le contrôle des procédés et poursuivre la «nanométrisation» des composantes électroniques. Un simulateur cellulaire à l’échelle du motif en deux dimensions s’appuyant sur les méthodes Monte-Carlo a été développé pour étudier l’évolution du profil lors de procédés de microfabrication. Le domaine de gravure est discrétisé en cellules carrées représentant la géométrie initiale du système masque-substrat. On insère les particules neutres et ioniques à l’interface du domaine de simulation en prenant compte des fonctions de distribution en énergie et en angle respectives de chacune des espèces. Le transport des particules est effectué jusqu’à la surface en tenant compte des probabilités de réflexion des ions énergétiques sur les parois ou de la réémission des particules neutres. Le modèle d’interaction particule-surface tient compte des différents mécanismes de gravure sèche telle que la pulvérisation, la gravure chimique réactive et la gravure réactive ionique. Le transport des produits de gravure est pris en compte ainsi que le dépôt menant à la croissance d’une couche mince. La validité du simulateur est vérifiée par comparaison entre les profils simulés et les observations expérimentales issues de la gravure par pulvérisation du platine par une source de plasma d’argon.

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ABSTRACT: Nylon tire cord (1680/2) was dipped in different adhesives based on resorcinol formaldehyde resin and latex (RFL) and was bonded to natural rubber-based compounds. The resin-rubber ratio in the RFL adhesive was optimized. The variation of pull-through load was studied by varying the drying and curing temperature of the dipped nylon tire cord. RFL adhesive based on vinylpyridine latex was found to have better rubber-to-nylon tire cord bonding, compared with the one based on natural rubber latex. Addition of a formaldehyde donor into the RFL adhesive/rubber compound improves adhesion.

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The aim of the investigation is to develop new high performance adhesive systems based on neoprene-phenolic blends. Initially the effect of addition of all possible ingredients like fillers, adhesion promoters, curing agents and their optimum compositions to neoprene solution is investigated. The phenolic resin used is a copolymer of phenol-cardanolformaldehyde prepared in the laboratory. The optimum ratio between phenol and cardanol that gives the maximum bond strength in metal-metal, rubber-rubber and rubber-metal specimens has been identified. Further the ratio between total phenols and formaldehyde is also optimised. The above adhesive system is further modified by the addition of epoxidized phenolic novolacs. For this purpose, phenolic novolac resins are prepared in different stoichiometric ratios and are subsequently epoxidized. The effectiveness of the adhesive for bonding different metal and rubber substrates is another part of the study. To study the ageing behaviour, different bonded specimens are exposed to high temperature, hot water and salt water and adhesive properties have been evaluated. The synthesized resins have been characterized by FTIR , HNMR spectroscopy. The molecular weights of the resins have been obtained by GPC. Thermogravimetric analysis and differential scanning calorimetry are used to study the thermal properties. The fractured surface analysis is studied by scanning electron microscopy. The study has brought to light the influence of phenol/ formaldehyde stoichiometric ratio, addition of cardanol (a renewable resource), adhesion promoters and suitability of the adhesive for different substrates and the age resistance of adhesive joints among other things.

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This research project aims at developing new applications for CNSL in the polymer field. Cashew nut shell liquid (CNSL) is a cheap agro-byproduct and renewable resource which consists mainly of substituted phenols. By using CNSL in place of phenol, phenol derived from petrochemicals can be conserved and a cheap agro-byproduct utilized.In this study CNSL based resin is prepared by condensing a mixture of phenol and CNSL with hexamethylenetetramine and the effect of P: F ratio and CNSL: P ratio on the properties of synthesized resin is studied. The adhesive properties of CNSL based resin in combination with neoprene rubber are investigated. The effect of varying the stoichiometric ratios between total phenol and formaldehyde and CNSL and phenol of the resin, resin content, choice and extent of fillers and adhesion promoters in the adhesive formulation are studied. The effect of resin on the ageing properties of various elastomers is also studied by following changes in tensile strength, elongation at break, modulus, tear strength, swelling index and acetone soluble matter. Crude CNSL and resins with different P: F ratios and CNSL: P ratios are incorporated into elastomers. Lastly, utility of CNSL based resin as binder for making particleboard is investigated.The results show that CNSL based resin is an effective ingredient in adhesives for bonding aluminium to aluminium. The resin used for adhesive fonnulation gives the best performance at 45 to 55 phr resin and a total phenol: formaldehyde of l:2.9. The resin when added at a rate of l5 phr improves ageing characteristics of elastomers with respect to mechanical properties. The reaction mixture of CNSL and hexa and the resin resulting from the condensation of CN SL, phenol and hexa can be used as effective binders for moulding particleboard.

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The thesis presents the results of the investigations on the crystallisation ‘behaviour, detect structure end electrical properties of certain organic crystals---phthslic snhydride end potsssiun scid phthalate Hollow crystals of phthalic snhydride were grown from vapour. the norpholog of these hollow crystals were studied in detail and s. mechanism for their growth has been proposed. A closed crystal—vapour system was used to study the basal plane growth of the whiskers and the sequential growth, observed, confirmed the mechanism suggested for hollow crystals. The dendritic crystals of phthslic enhydride were grown, both iron the melt and solution. The observed morphologies of these dendrites ere described. Bpherulites of phthalic anhydride have been grown by the artificial initiation of nucleation, from melt and solution. The variation of the substructure oi’ these spherulites with the growth tenperature wee investigated. The spherulitic filll having ribbon substructure were etched to reveal dislocations. A mechanism for the formation of the observed etch pattern has been suggested. the slip occurring in these ribbons were studied and the results are presented

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Graphene has captured the attention of scientific community due to recently emerging high performance applications. Hence, studying its reinforcing effects on epoxy resin is a significant step. In this study, microwave exfoliated reduced graphene oxide (MERGO) was prepared from natural graphite for subsequent fabrication of epoxy nanocomposites using triethylenetetramine (TETA) as a curing agent via insitu polymerization. Thermogravimetric analysis (TGA), X-ray diffraction (XRD), Raman spectroscopy, Fourier transform infrared spectroscopy (FTIR), C13 NMR spectroscopy, X-ray photoelectron spectroscopy (XPS) and ultravioletevisible (UVevis) spectroscopy were employed to confirm the simultaneous reduction and exfoliation of graphene oxide. The reinforcing effect of MERGO on epoxy resin was explored by investigating its static mechanical properties and dynamic mechanical analysis (DMA) at MERGO loadings of 0 to 0.5 phr. The micro-structure of epoxy/MERGO nanocomposites was investigated using scanning electron microscope (SEM), transmission electron microscope (TEM) and XRD techniques. The present work reports an enhancement of 32%, 103% and 85% in tensile, impact and flexural strength respectively of epoxy by the addition of even 0.25 phr MERGO. At this loading elastic and flexural moduli also increased by 10% and 65%, respectively. Single-edge-notch three-point-Bending (SEN-TPB) fracture toughness (KIC) measurements were carried out where a 63% increase was observed by the introduction of 0.25 phr MERGO. The interfacial interactions brought about by graphene also benefited the dynamic mechanical properties to a large extent in the form of a significant enhancement in storage modulus and slightly improved glass transition temperature. Considerable improvements were also detected in dielectric properties. The epoxy nanocomposite also attained an ac conductivity of 10 5 S/m and a remarkable increase in dielectric constant. The simple and cost effective way of graphene synthesis for the fabrication of epoxy/MERGO nanocomposites may be extended to the preparation of other MERGO based polymer nanocomposites. This remarkable class of materials has thrown open enormous opportunities for developing conductive adhesives and in microelectronics

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Polymers with conjugated π-electron backbone display unusual electronic properties such as low energy optical transition, low ionization potentials, and high electron affinities. The properties that make these materials attractive include a wide range of electrical conductivity, mechanical flexibility and thermal stability. Some of the potential applications of these conjugated polymers are in sensors, solar cells, field effect transistors, field emission and electrochromic displays, supercapacitors and energy storage. With recent advances in the stability of conjugated polymer materials, and improved control of properties, a growing number of applications are currently being explored. Some of the important applications of conducting polymers include: they are used in electrostatic materials, conducting adhesives, shielding against electromagnetic interference (EMI), artificial nerves, aircraft structures, diodes, and transistors.

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The progress in microsystem technology or nano technology places extended requirements to the fabrication processes. The trend is moving towards structuring within the nanometer scale on the one hand, and towards fabrication of structures with high aspect ratio (ratio of vertical vs. lateral dimensions) and large depths in the 100 µm scale on the other hand. Current procedures for the microstructuring of silicon are wet chemical etching and dry or plasma etching. A modern plasma etching technique for the structuring of silicon is the so-called "gas chopping" etching technique (also called "time-multiplexed etching"). In this etching technique, passivation cycles, which prevent lateral underetching of sidewalls, and etching cycles, which etch preferably in the vertical direction because of the sidewall passivation, are constantly alternated during the complete etching process. To do this, a CHF3/CH4 plasma, which generates CF monomeres is employed during the passivation cycle, and a SF6/Ar, which generates fluorine radicals and ions plasma is employed during the etching cycle. Depending on the requirements on the etched profile, the durations of the individual passivation and etching cycles are in the range of a few seconds up to several minutes. The profiles achieved with this etching process crucially depend on the flow of reactants, i.e. CF monomeres during the passivation cycle, and ions and fluorine radicals during the etching cycle, to the bottom of the profile, especially for profiles with high aspect ratio. With regard to the predictability of the etching processes, knowledge of the fundamental effects taking place during a gas chopping etching process, and their impact onto the resulting profile is required. For this purpose in the context of this work, a model for the description of the profile evolution of such etching processes is proposed, which considers the reactions (etching or deposition) at the sample surface on a phenomenological basis. Furthermore, the reactant transport inside the etching trench is modelled, based on angular distribution functions and on absorption probabilities at the sidewalls and bottom of the trench. A comparison of the simulated profiles with corresponding experimental profiles reveals that the proposed model reproduces the experimental profiles, if the angular distribution functions and absorption probabilities employed in the model is in agreement with data found in the literature. Therefor the model developed in the context of this work is an adequate description of the effects taking place during a gas chopping plasma etching process.

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High-speed semiconductor lasers are an integral part in the implemen- tation of high-bit-rate optical communications systems. They are com- pact, rugged, reliable, long-lived, and relatively inexpensive sources of coherent light. Due to the very low attenuation window that exists in the silica based optical fiber at 1.55 μm and the zero dispersion point at 1.3 μm, they have become the mainstay of optical fiber com- munication systems. For the fabrication of lasers with gratings such as, distributed bragg reflector or distributed feedback lasers, etching is the most critical step. Etching defines the lateral dimmensions of the structure which determines the performance of optoelectronic devices. In this thesis studies and experiments were carried out about the exist- ing etching processes for InP and a novel dry etching process was de- veloped. The newly developed process was based on Cl2/CH4/H2/Ar chemistry and resulted in very smooth surfaces and vertical side walls. With this process the grating definition was significantly improved as compared to other technological developments in the respective field. A surface defined grating definition approach is used in this thesis work which does not require any re-growth steps and makes the whole fabrication process simpler and cost effective. Moreover, this grating fabrication process is fully compatible with nano-imprint lithography and can be used for high throughput low-cost manufacturing. With usual etching techniques reported before it is not possible to etch very deep because of aspect ratio dependent etching phenomenon where with increasing etch depth the etch rate slows down resulting in non-vertical side walls and footing effects. Although with our de- veloped process quite vertical side walls were achieved but footing was still a problem. To overcome the challenges related to grating defini- tion and deep etching, a completely new three step gas chopping dry etching process was developed. This was the very first time that a time multiplexed etching process for an InP based material system was demonstrated. The developed gas chopping process showed extra ordinary results including high mask selectivity of 15, moderate etch- ing rate, very vertical side walls and a record high aspect ratio of 41. Both the developed etching processes are completely compatible with nano imprint lithography and can be used for low-cost high-throughput fabrication. A large number of broad area laser, ridge waveguide laser, distributed feedback laser, distributed bragg reflector laser and coupled cavity in- jection grating lasers were fabricated using the developed one step etch- ing process. Very extensive characterization was done to optimize all the important design and fabrication parameters. The devices devel- oped have shown excellent performance with a very high side mode suppression ratio of more than 52 dB, an output power of 17 mW per facet, high efficiency of 0.15 W/A, stable operation over temperature and injected currents and a threshold current as low as 30 mA for almost 1 mm long device. A record high modulation bandwidth of 15 GHz with electron-photon resonance and open eye diagrams for 10 Gbps data transmission were also shown.

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In this work investigation of the QDs formation and the fabrication of QD based semiconductor lasers for telecom applications are presented. InAs QDs grown on AlGaInAs lattice matched to InP substrates are used to fabricate lasers operating at 1.55 µm, which is the central wavelength for far distance data transmission. This wavelength is used due to its minimum attenuation in standard glass fibers. The incorporation of QDs in this material system is more complicated in comparison to InAs QDs in the GaAs system. Due to smaller lattice mismatch the formation of circular QDs, elongated QDs and quantum wires is possible. The influence of the different growth conditions, such as the growth temperature, beam equivalent pressure, amount of deposited material on the formation of the QDs is investigated. It was already demonstrated that the formation process of QDs can be changed by the arsenic species. The formation of more round shaped QDs was observed during the growth of QDs with As2, while for As4 dash-like QDs. In this work only As2 was used for the QD growth. Different growth parameters were investigated to optimize the optical properties, like photoluminescence linewidth, and to implement those QD ensembles into laser structures as active medium. By the implementation of those QDs into laser structures a full width at half maximum (FWHM) of 30 meV was achieved. Another part of the research includes the investigation of the influence of the layer design of lasers on its lasing properties. QD lasers were demonstrated with a modal gain of more than 10 cm-1 per QD layer. Another achievement is the large signal modulation with a maximum data rate of 15 Gbit/s. The implementation of optimized QDs in the laser structure allows to increase the modal gain up to 12 cm-1 per QD layer. A reduction of the waveguide layer thickness leads to a shorter transport time of the carriers into the active region and as a result a data rate up to 22 Gbit/s was achieved, which is so far the highest digital modulation rate obtained with any 1.55 µm QD laser. The implementation of etch stop layers into the laser structure provide the possibility to fabricate feedback gratings with well defined geometries for the realization of DFB lasers. These DFB lasers were fabricated by using a combination of dry and wet etching. Single mode operation at 1.55 µm with a high side mode suppression ratio of 50 dB was achieved.

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El presente trabajo tiene como objetivo mostrar la relación que existe entre la cadena de suministro, global manufacturing y su relación con el desempeño organizacional en el sector manufacturero. El proyecto va a estar divido en tres grandes partes, en primer lugar estará el marco conceptual donde se especificarán los conceptos más significativos que abarcan la investigación, seguido del marco teórico donde se expondrán las teorías y estudios encontrados, analizados y estudiados con el fin de desembocar en la tercer parte que serán las conclusiones y recomendaciones que se darán a partir de los análisis y teorías que compactan el tema de la relación existente entre la cadena de suministro, global manufacturing y el desempeño organizacional.

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La sang de porc és un subproducte comestible que es genera als escorxadors industrials durant el procés d'obtenció de la canal. Aquest subproducte es caracteritza per presentar una elevada càrrega contaminant i, degut a l'elevat volum que es genera, és necessari trobar estratègies que permetin la seva revaloració i aprofitament, a la vegada que disminuïm la contaminació ambiental i les despeses que es deriven del seu processament abans de l'abocament. La fracció cel·lular (FC) constitueix el 40 % de la sang de porc i conté principalment l'hemoglobina (Hb), que representa al voltant del 90 % del contingut en proteïna d'aquesta fracció (un 35 % aproximadament). L'elevat percentatge en proteïna i en ferro, i les seves bones propietats funcionals fan que l'aprofitament d'aquest subproducte com a primera matèria o ingredient de la indústria alimentària sigui una alternativa molt útil a l'hora de reduir les despeses de la indústria càrnia, sempre que es resolguin els problemes de l'enfosquiment i dels sabors estranys que pot conferir la FC quan s'addiciona a productes alimentaris. Una altra possible utilització de la FC és aprofitar les propietats colorants de l'Hb o del grup hemo, com a colorant d'origen natural en diversos productes alimentaris. Els objectius del present treball eren, en primer lloc, determinar les millors condicions d'aplicació del procés de conservació de la FC mitjançant la deshidratació per atomització i caracteritzar físico-químicament i microbiològica el concentrat d'Hb en pols. En segon lloc, avaluar l'eficàcia de diferents additius antioxidants i/o segrestants del ferro per prevenir l'enfosquiment que pateix la FC durant la deshidratació. En tercer lloc, aplicar tractaments d'altes pressions hidrostàtiques com a procés d'higienització i avaluar els efectes d'aquest tractament sobre la microbiota contaminant, el color i les propietats funcionals de la FC. Finalment, desenvolupar un procés d'obtenció d'hidrolitzats proteics descolorats a partir de l'Hb amb la finalitat d'utilitzar-los com a ingredients nutricionals i/o funcionals. La millor temperatura de deshidratació per atomització de la FC hemolitzada era 140ºC. La FC en pols presentava un contingut en humitat del 5,3 % i un percentatge de solubilitat proteica del 96 %. La deshidratació per atomització induïa canvis en l'estructura nativa de l'Hb i, per tant, un cert grau de desnaturalització que pot conduir a una disminució de les seves propietats funcionals. L'extracte sec de la FC en pols estava composat per un 94,6 % de proteïna, un 3 % de sals minerals i un 0,7 % de greix. Els valors CIE L*a*b* del color de la FC en pols eren força constants i reflectien el color vermell marró fosc d'aquesta, a causa de l'oxidació del ferro hèmic que es produeix durant la deshidratació. La càrrega contaminant de la FC fresca de la sang de porc era força elevada i el tractament d'hemòlisi amb ultrasons i la centrifugació posterior no produïen una reducció significativa de la microbiota contaminant, obtenint un producte amb uns recomptes microbiològics de l'ordre de 106 ufc·mL-1. La deshidratació per atomització produïa una disminució d'una unitat logarítmica dels recomptes totals de la FC hemolitzada. Tanmateix, el producte en pols encara reflectia l'elevada contaminació de la primera matèria, fet que condiciona negativament la seva utilització com a ingredient alimentari, a no ser que es millorin les condicions de recollida de la sang a l'escorxador o que aquesta o la FC es sotmeti a algun tractament d'higienització prèviament a la deshidratació. Les isotermes de sorció a 20ºC de la FC en pols tenien forma sigmoïdal i una histèresi estreta i llarga. L'equació GAB és un bon model matemàtic per ajustar les dades de sorció obtingudes experimentalment i determinar la isoterma d'adsorció de la FC deshidratada per atomització. El percentatge d'humitat de la FC deshidratada a 140ºC es corresponia a un valor d'aw a 20 ºC d'aproximadament el 0,16. Tenint en compte que estava per sota dels valors d'aw corresponents a la capa monomolecular, es pot garantir la conservació a temperatura ambient del producte, sempre que s'envasi en recipients tancats que no permetin l'entrada d'humitat de l'exterior. De l'estudi de la possible estabilització del color de la FC deshidratada per atomització mitjançant l'addició d'antioxidants i/o segrestants de ferro, es va observar que només l'àcid ascòrbic, la glucosa, l'àcid nicotínic i la nicotinamida, tenien efectes positius sobre el color del producte en pols. L'ascòrbic i la glucosa no milloraven la conservació del color de l'Hb però disminuïen l'enfosquiment que es produeix durant la deshidratació, amb la qual cosa es pot obtenir un producte en pols de color marró més clar. L'addició de dextrina o L-cisteïna no disminuïa l'enfosquiment ni evitava el canvi de color de l'Hb. L'àcid nicotínic i la nicotinamida protegien el color de l'Hb durant el procés de deshidratació i l'emmagatzematge de la FC en pols. Les millors condicions d'aplicació del tractament amb altes pressions hidrostàtiques (HHP) sobre la FC eren 400 MPa, a 20ºC, durant 15 minuts, perquè produïen una millora significativa de la qualitat microbiològica, no afectaven negativament al color, no comprometien gaire la solubilitat proteica l'Hb i, malgrat que produïen un augment de la viscositat, la FC romania fluida després del tractament. Aquest tractament permetia una reducció de la microbiota contaminant de la FC d'entre 2 i 3 unitats logarítmiques. L'aplicació de l'alta pressió i la posterior deshidratació per atomització permetien obtenir un producte en pols amb recomptes totals de l'ordre de 2,8 unitats logarítmiques. El color de la FC pressuritzada en pols era igual que el de la FC control deshidratada, perquè ambdues mostres presentaven la mateixa susceptibilitat a l'oxidació del grup hemo produïda per la deshidratació. L'alta pressió incrementava la susceptibilitat de l'Hb als efectes desnaturalitzants de la deshidratació, fonamentalment a pH 7 (PIE), ja que es va observar una disminució de la solubilitat proteica a pH neutre després dels 2 processos tecnològics. La FC en pols presentava una màxima capacitat escumant al PIE de l'Hb. L'aplicació del tractament HHP produïa una disminució de la capacitat escumant de la FC en pols, però no tenia efectes negatius sobre l'estabilitat de l'escuma formada. Tampoc es van observar efectes negatius del tractament HHP sobre l'activitat emulsionant de l'Hb. La màxima activitat emulsionant de l'Hb s'aconseguia amb una concentració de FC en pols de l'1,5 % a pH 7 i de l'1 % a pH 4,5. Les pastes obtingudes per escalfament de la FC presentaven característiques molt diferenciades depenent del pH. A pH neutre es formaven unes pastes dures i consistents, mentre que a pH àcid les pastes eren poc consistents, molt adhesives i més elàstiques que les anteriors. Aquestes tenien una capacitat de retenció d'aigua molt superior que les de pH 7, en les quals l'aigua quedava retinguda per capil·laritat. La textura i capacitat de retenció d'aigua de les pastes tampoc eren afectades pel tractament HHP. El tractament HHP incrementava l'activitat de la Tripsina sobre l'Hb quan el substrat i l'enzim es tractaven conjuntament i afavoria el procés d'obtenció d'hidrolitzats descolorats a partir de la FC, la qual cosa permetia assolir el mateix grau de descoloració amb una dosi d'enzim inferior. El tractament d'hidròlisi de la FC amb la utilització combinada de Tripsina seguida d'un tractament amb Pepsina permetia l'obtenció d'un hidrolitzat proteic d'Hb descolorat i hidrolitzava completament la globina, donant lloc a 2 pèptids de 10,8 i 7,4 KDa. Val a dir que també produïa un 60 80 % de nitrogen soluble en TCA, constituït fonamentalment per pèptids petits i aminoàcids lliures. Els hidrolitzats trípsics i pèpsics d'Hb, obtinguts a partir de FC no pressuritzada i deshidratats per atomització a 180ºC, eren de color blanc i tenien un contingut en humitat del 4,7 %, un 84,2 % de proteïna i 9,7 % de sals minerals. El procés d'hidròlisi permetia una reducció considerable de la contaminació de la FC, obtenint un producte en pols amb uns recomptes totals de l'ordre de 102-103 ufc·g-1. Pel que fa a la funcionalitat dels hidrolitzats d'Hb deshidratats per atomització, aquests presentaven una elevada solubilitat proteica a pH 5 i 7 i romanien solubles després d'un escalfament a 80ºC durant 30 min. Tanmateix, aquesta hidròlisi afectava molt negativament la capacitat de mantenir escumes estables i l'activitat emulsionant.

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Surface coatings are very common on mineral grains in soils but most laboratory dissolution experiments are carried out on pristine, uncoated mineral grains. An experiment designed to unambiguously isolate the effect of surface coatings on mineral dissolution from any influence of solution saturation state is reported. Two aliquots of 53 to 63 mum anorthite feldspar powder were used. One was dissolved in pH 2.6 HCl, the other in pH 2.6 FeCl3 solution, both for similar to6000 h in flow-through reactors. An amorphous Fe-rich, Al-, Ca- and Si-free orange precipitate coated the anorthite dissolved in the FeCl3 solution. BET surface area of the anorthite increased from 0.16 to 1.65 m(2) g(-1) in the HCl experiment and to 3.89 m(2) g(-1) in the FeCl3 experiment. The increase in surface area in the HCl experiment was due to the formation of etch pits on the anorthite grain surface whilst the additional increase in the FeCl3 experiment was due to the micro- and meso-porous nature of the orange precipitate. This precipitate did not inhibit or slow the dissolution of the anorthite. Steady state dissolution rates for the anorthite dissolved in the HCl and FeCl3 were similar to2.5 and 3.2 X 10(-10) mol(feldspar) m(-2) s(-1) respectively. These rates are not significantly different after the cumulative uncertainty of 17% in their value due to uncertainty in the inputs parameters used in their calculation is taken into account. Results from this experiment support previous theoretical and inference-based conclusions that porous coatings should not inhibit mineral dissolution. Copyright (C) 2003 Elsevier Ltd.

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Laboratory determined mineral weathering rates need to be normalised to allow their extrapolation to natural systems. The principle normalisation terms used in the literature are mass, and geometric- and BET specific surface area (SSA). The purpose of this study was to determine how dissolution rates normalised to these terms vary with grain size. Different size fractions of anorthite and biotite ranging from 180-150 to 20-10 mu m were dissolved in pH 3, HCl at 25 degrees C in flow through reactors under far from equilibrium conditions. Steady state dissolution rates after 5376 h (anorthite) and 4992 h (biotite) were calculated from Si concentrations and were normalised to initial- and final- mass and geometric-, geometric edge- (biotite), and BET SSA. For anorthite, rates normalised to initial- and final-BET SSA ranged from 0.33 to 2.77 X 10(-10) mol(feldspar) m(-2) s(-1), rates normalised to initial- and final-geometric SSA ranged from 5.74 to 8.88 X 10(-10) mol(feldspar) m(-2) s(-1) and rates normalised to initial- and final-mass ranged from 0.11 to 1.65 mol(feldspar) g(-1) s(-1). For biotite, rates normalised to initial- and final-BET SSA ranged from 1.02 to 2.03 X 10(-12) mol(biotite) m(-2) s(-1), rates normalised to initial- and final-geometric SSA ranged from 3.26 to 16.21 X 10(-12) mol(biotite) m(-2) s(-1), rates normalised to initial- and final-geometric edge SSA ranged from 59.46 to 111.32 x 10(-12) mol(biotite) m(-2) s(-1) and rates normalised to initial- and final-mass ranged from 0.81 to 6.93 X 10(-12) mol(biotite) g(-1) s(-1). For all normalising terms rates varied significantly (p <= 0.05) with grain size. The normalising terms which gave least variation in dissolution rate between grain sizes for anorthite were initial BET SSA and initial- and final-geometric SSA. This is consistent with: (1) dissolution being dominated by the slower dissolving but area dominant non-etched surfaces of the grains and, (2) the walls of etch pits and other dissolution features being relatively unreactive. These steady state normalised dissolution rates are likely to be constant with time. Normalisation to final BET SSA did not give constant ratios across grain size due to a non-uniform distribution of dissolution features. After dissolution coarser grains had a greater density of dissolution features with BET-measurable but unreactive wall surface area than the finer grains. The normalising term which gave the least variation in dissolution rates between grain sizes for biotite was initial BET SSA. Initial- and final-geometric edge SSA and final BET SSA gave the next least varied rates. The basal surfaces dissolved sufficiently rapidly to influence bulk dissolution rate and prevent geometric edge SSA normalised dissolution rates showing the least variation. Simple modelling indicated that biotite grain edges dissolved 71-132 times faster than basal surfaces. In this experiment, initial BET SSA best integrated the different areas and reactivities of the edge and basal surfaces of biotite. Steady state dissolution rates are likely to vary with time as dissolution alters the ratio of edge to basal surface area. Therefore they would be more properly termed pseudo-steady state rates, only appearing constant because the time period over which they were measured (1512 h) was less than the time period over wich they would change significantly. (c) 2006 Elsevier Inc. All rights reserved.