20 resultados para BUBBLE PRECURSORS

em Aston University Research Archive


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This paper reports on the results of research into the connections between transaction attributes and buyer-supplier relationships (BSRs) in advanced manufacturing technology (AMT) acquisition and implementation. The investigation began by examining the impact of the different patterns of BSR on the performance of the AMT acquisition. In understanding the phenomena, the study drew upon and integrated the literature of transaction cost economics theory, BSRs, and AMT, and used this as the basis for a theoretical framework and hypotheses development. This framework was then empirically tested using data that were gathered through a questionnaire survey with 147 companies and analyzed using a structural equation modeling technique. The results of the analysis indicated that the higher the level of technological specificity and uncertainty, the more firms are likely to engage in a stronger relationship with technology suppliers. However, the complexity of the technology being implemented was associated with BSR only indirectly through its association with the level of uncertainty (which has a direct impact upon BSR). The analysis also provided strong support for the premise that developing strong BSR could lead to an improved performance in acquiring and implementing AMT. The implications of the study are offered for both the academic and practitioner audience.

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Investigations into the modelling techniques that depict the transport of discrete phases (gas bubbles or solid particles) and model biochemical reactions in a bubble column reactor are discussed here. The mixture model was used to calculate gas-liquid, solid-liquid and gasliquid-solid interactions. Multiphase flow is a difficult phenomenon to capture, particularly in bubble columns where the major driving force is caused by the injection of gas bubbles. The gas bubbles cause a large density difference to occur that results in transient multi-dimensional fluid motion. Standard design procedures do not account for the transient motion, due to the simplifying assumptions of steady plug flow. Computational fluid dynamics (CFD) can assist in expanding the understanding of complex flows in bubble columns by characterising the flow phenomena for many geometrical configurations. Therefore, CFD has a role in the education of chemical and biochemical engineers, providing the examples of flow phenomena that many engineers may not experience, even through experimentation. The performance of the mixture model was investigated for three domains (plane, rectangular and cylindrical) and three flow models (laminar, k-e turbulence and the Reynolds stresses). mThis investigation raised many questions about how gas-liquid interactions are captured numerically. To answer some of these questions the analogy between thermal convection in a cavity and gas-liquid flow in bubble columns was invoked. This involved modelling the buoyant motion of air in a narrow cavity for a number of turbulence schemes. The difference in density was caused by a temperature gradient that acted across the width of the cavity. Multiple vortices were obtained when the Reynolds stresses were utilised with the addition of a basic flow profile after each time step. To implement the three-phase models an alternative mixture model was developed and compared against a commercially available mixture model for three turbulence schemes. The scheme where just the Reynolds stresses model was employed, predicted the transient motion of the fluids quite well for both mixture models. Solid-liquid and then alternative formulations of gas-liquid-solid model were compared against one another. The alternative form of the mixture model was found to perform particularly well for both gas and solid phase transport when calculating two and three-phase flow. The improvement in the solutions obtained was a result of the inclusion of the Reynolds stresses model and differences in the mixture models employed. The differences between the alternative mixture models were found in the volume fraction equation (flux and deviatoric stress tensor terms) and the viscosity formulation for the mixture phase.

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The reactions of group 16 heterocycles with organometallic reagents are described. Thiophenes have been used as models for organic sulfur in coal and their reactivity towards triiron dodecacarbonyl has been investigated. Reaction of unsubstituted thiophene with Fe3(CO)12 results in desulfurisation of the heterocycle, with the organic fragment being recovered in the form of the ferrole, C4H4.Fe2(CO)6. In addition a novel organometallic compound of iron is isolated, the formula of which is shown to be C4H4.Fe3(CO)8. Bezothiophene reacts with Fe3(CO)12 to yield benzothiaferrole, C8H6S.Fe2(CO)6, in which the sulfur is retained in the heterocycle. Dibenzothiophene, a more accurate model for organic sulfur in coal, displays no reactivity towards the iron carbonyl, suggesting that the more condensed systems will desulfurise less readily. Microwave methodology has been successful in accelerating the reactions of thiophenes with Fe3(CO)12. However, reaction of benzothiophene does not proceed to the desulfurisation stage while dibenzothiophene is unreactive even under microwave conditions. Tellurophenes (Te analogues of thiophenes) are shown to mimic the behaviour of thiophenes towards certain organometallic reagents with the advantage that their greater reactivity enables recovery of products in higher yields. Hence, reaction of tellurophene with Fe3(CO)12 again affords the ferrole but with an almost ten-fold increase in yield over thiophene. More significantly, dibenzotellurophene is also detellurated by the iron carbonyl affording the previously inaccessible dibenzoferrole, C12H8.Fe2(CO)6, thereby demonstrating the mechanistic feasibility of dechalcogenation of the more condensed aromatic molecules. The potential of tellurium heterocycles to act as precursors for novel organometallics is also recognised owing to the relatively facile elimination of the heteroatom from these systems. Thus, 2-telluraindane reacts with Fe3(CO)12 to yield a novel organometallic compound of formula C16H16.Fe(CO)3, arising from the unsymmetric dimerisation of two organic fragments.

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Various 2,2,6,6-tetramethyl piperidines and their N-alkyl derivatives of stable nitroxyl radical precursors containing acrylic(s) and methacrylic(s) groups were reactively processed in the presence of a peroxide as bound-antioxidant masterbatches for polyolefin stabilisation. It was found that grafting of the antioxidant monomers onto the polymer backbone was inevitably in competition with homopolymerisation of the monomers as well as melt degradation of the polymer and other side reactions. As previously reported, binding efficiency of bisacrylic nitroxyl precursor was maximum due to formation of unextractable homopolymer of the antioxidant. On the other hand, the binding efficiency of monoacrylic derivatives was low and the homopolymers were found extractable, which suggests that the bound monoacrylic derivatives are entirely grafted onto the polyolefin backbone. Application of bis and tri-functional coagents gave improved binding efficiency of the monoacrylic monomers. This may be due to copolymerisation of the antioxidants with the coagents and grafting of the copolymers onto the polymer backbone. Comparison of photostabilising activity of the fully extracted bound antioxidants to those of the corresponding unbound analogous showed lower results for the former. However, thermal stabilising activity of the bound antioxidants was higher than that of the unbound analogous due to better substantivity. Analysis using physical techniques and GPC for molecular weight distribution of masterbatches containing the bound monoacrylic antioxidants showed formation of high molecular weight products. Model reaction of a secondary amine derivative in liquid hydrocarbon and analysis of the product using FTIR and NMR spectroscopy indicated a possibility of side reaction, i.e. involvement of the amine active group (>N-H) of the antioxidant in the binding process to form the high molecular weight product. Implementation of various N-alkylated derivatives did not inhibit the side reaction. The photostabilising activity of the bound-antioxidants can be improved when applied in conjunction with small amounts of a benzophenone uv-stabiliser. The synergistic stabilising activity, however, was diminished when the uv-stabiliser was removed from the system during the service time. Nitroxyl precursors containing methacrylic group(s) gave lower binding efficiency than the corresponding acrylic derivatives. Reversible deploymerisation of the grafted methacrylic antioxidants may be responsible for this. Bis and tris-acrylic coagents improved the binding efficiency, and the presence of methacrylic group improved stabilising activity of the antioxidants. N-methyl derivatives were found to exhibit better stabilising activity than their parent secondary amine derivatives.

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The synthetic hectorite, laponite has been used within the paper industry to produce mildly conducting paper for use in electrographic printing. The aim of this research was to modify laponite in order to improve the electrical conductivity. In a continuation of a previous investigation involving organotin intercalation of laponite, the organotin precursor (p-CH3,OC6H4)4Sn was synthesised and characterised using Mass Spectroscopy, Infrared Spectroscopy and elemental analysis. Results of intercalation with this compound and a range of organobismuth and organoantimony compounds suggested that a halide content within the precursor was necessary for improvement in conductivity to be observed. Organometallic intercalation of a range of organotellurium compounds with laponite provided evidence that a hydrolysis reaction on the clay surface followed by the release of hydrochloric acid was an important first step if a reaction was to occur with the clay. Atomic Absorption Spectroscopy studies have shown that the acid protons underwent exchange with the interlayer sodium ions in the clay to varying degrees. Gas-liquid Chromatography and Infrared Spectroscopy revealed that the carbon-tellurium bond remained intact. Powder X-ray diffraction revealed that there had been no increase in the basal spacing. The a.c. conductivity of the modified clays in the form of pressed discs was studied over a frequency range of 12Hz - 100kHz using two electrode systems, silver paste and stainless steel. The a.c. conductivity consists of two components, ionic and reactive. The conductivity of laponite was increased by intercalation with organometallic compounds. The most impressive increase was gained using the organotellurium precursor (p-CH3OC6H4)2TeCl2. Conductivity investigations using the stainless steel electrode where measurements are made under pressure showed that in the case of laponite, where poor particle-particle contact exists at ambient pressure, there is a two order of magnitude increase in the measured a.c. conductivity. This significant increase was not seen in modified laponites where the particle-particle contact had already been improved upon. Investigations of the clay surface using Scanning Electron Microscopy suggested that the improvement in particle-particle contact is the largest factor in the determination of the conductivity. The other important factor is the nature and the concentration of the interlayer cations. A range of clays were synthesised in order to increase the concentration of sodium interlayer cations. A sol-gel method was employed to carry out these syntheses. A conductivity evaluation showed that increasing the concentration of the sodium cations within the clay led to an increase in the conductivity.

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High strength, high modulus carbon fibres are becoming increasingly important as high performance engineering materials. This thesis describes how they may be prepared by heat treatment from filaments spun from polyacrylonitrile and its copolymers. The chemistry of the first stages of heat treatment is very important in controlling the mechanical properties of the carbonised product. A cyclisation reaction has been found to be responsible for the relatively high thermal stability of pyrolysed polyacrylonitrile, but without oxidation the fibres degrade and fuse. An initial oxidation stage is, therefore, essential to the preparation of fibre of high orientation. The cyclised product of pyrolysis is probably a poly 1,4 dihydropiridine and oxidation converts this to aromatic structures, and cyclised structures containing carbonyl and other oxygenated groups. Oxidation is found to assist the carbon fibre preparation process, by producing a product which condenses at an earlier stage of heat treatment, before fusion can occur. Carbon fibre strength and modulus are dependent upon producing a highly oriented crystal structure. While oxidation of the polymer stabilises the fibre so as to prevent disorientation, further large increases in orientation, with a commensurate improvement in strength and modulus, can be obtained by stretching at temperatures above 1,700 °C. This process is analogous to the way fibre orientation is increased by the stretching of the precursor. A lamellar graphite structure can be created in high temperature fibre, by carefully controlling the degree of oxidation. This type of graphite can produce very high values of Young's modulus. More often, however, graphite fibre has a fibrillar fine structure, which is explicable in terms of continuous graphite ribbons. A ribbon model is the most satisfactory representation of the structure of carbon fibre, as it explains the mechanism of the development of long range order and the variation of Young's modulus with crystalline preferred orientation.

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The simulation of two-phase flow for an experimental airlift reactor (32-l volume) using commercially available software from Fluent Incorporated is presented here (http://www.fluent.co.uk). Data from the simulation is compared with the experimental data obtained by the tracking of a magnetic particle and analysis of the pressure drop to determine the gas hold-up. Comparisons between vertical velocity and gas hold-up were made for a series of experiments where the superficial gas velocity in the riser was adjusted between 0.01 and 0.075 m s-1. © 2003 Elsevier B.V. All rights reserved.