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Letteratura scientifica selezionata sul tema "Hollow fibre"

Autore: Grafiati

Pubblicato: 4 giugno 2021

Ultima modifica: 19 febbraio 2022

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Articoli di riviste sul tema "Hollow fibre"

1

Mu, Hai Bo, Gui Zeng Hao, Xiao Wei Li e Bo Meng. "Preparation and Properties of Asymmetric Porous Aluminium-Oxide Ceramic Hollow Fibre Membranes". Key Engineering Materials 537 (gennaio 2013): 87–91. http://dx.doi.org/10.4028/www.scientific.net/kem.537.87.

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Asymmetric porous aluminium-oxide ceramic hollow fibre membranes have been prepared by the phase inversion / sintering technique. The effect of non-solvent such as ethanol, isopropanol and ethylene glycol monomethylether(2-methoxyethanol) on the geometry and performance of hollow fibres was investigated. Morphologies of Al2O3 ceramic hollow fibre membranes were characterized using a scanning electron microscope (SEM). The effective porosity and the mechanical strength were determined by Archimedes method, and three point method, respectively. The prepared Al2O3 hollow fibre membranes show the asymmetric structure with a finger-like layer and a sponge-like layer. The effective porosity of the prepared hollow fibre membranes exceeds 47%, and the bending strength of the hollow membranes exceeds 63 MPa. The Al2O3 hollow fibre membranes with moderate permeation characteristics for gas and pure water are prepared by the introduction of nonsolvent in membrane casting solution. The separation factors of H2 to N2 or CO2 of the hollow fibers with nonsolvent are over 2.0.

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2

Horiuchi, Noriaki. "Hollow-core fibre". Nature Photonics 7, n. 8 (30 luglio 2013): 584–85. http://dx.doi.org/10.1038/nphoton.2013.203.

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3

Hucker, Martyn, Ian Bond, Andrew Foreman e Jennifer Hudd. "Optimisation of Hollow Glass Fibres and their Composites". Advanced Composites Letters 8, n. 4 (luglio 1999): 096369359900800. http://dx.doi.org/10.1177/096369359900800406.

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Hollow glass fibre reinforced plastics have a structural performance niche in a class of their own. They offer increased flexural rigidity compared to solid glass fibre reinforced plastics, they offset the need for thin sandwich construction which is both difficult and expensive, and they provide an opportunity to develop laminates with improved or tailored characteristics. An experimental hollow glass fibre manufacturing facility is in operation at the University of Bristol. The facility is capable of drawing precision hollow glass fibres of various diameters with varying degrees of hollowness under precise parameter control. Hollow borosilicate glass fibres have been manufactured from tubular preforms with a variety of internal and external diameters, which correspond to a range of hollowness values. In all cases, the resulting hollowness was reduced from that present in the preform state, regardless of drawing rate or furnace temperature. In fact, temperature has been demonstrated to be of paramount importance in controlling fibre hollowness due to the interaction between glass viscosity and surface tension effects. These results suggest that for a given temperature and draw rate there is a single condition where fibre hollowness is maximised and external diameter minimised.

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4

Lim, Keng, Hui An, Peng Wang, Guiqin Liu e Simon Yu. "Theoretical and Computational Analysis on Double-End Submerged Hollow Fibre Membrane Modules". Energies 11, n. 5 (24 aprile 2018): 1042. http://dx.doi.org/10.3390/en11051042.

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This paper studies the potential increase in permeate output flow rate that submerged hollow fibres can achieve when operating in double-end suction. The flow dynamics of submerged hollow fibre membranes with different combinations of fibre inner diameter, membrane thickness, and membrane permeability were numerically simulated. Fibre features (fibre inner diameter, membrane thickness, and membrane permeability) are then characterised for their effects on the increment in permeate flow rate due to change in configuration. Concurrently, an analytical model of a fibre in double-end suction is modelled. Analysis on the double-end fibre model has indicated that the fibre characteristic ratio, λ, has a direct influence on the relative increase in output flow rate when both ends are open. Parametric investigations on the three fibre features have shown that their effects on relative output increase agree with the co-relations indicated by λ. For fibres with λ less than 4, a proportional relationship between a fibre’s λ value and the percentage increment in permeate flow rate is observed when adopting double-end suction. The fibre characteristic ratio, λ, in addition to characterising flux uniformity, can further be used to consider the effectiveness of applying double-end suction in Submerged Hollow Fibre Membrane Module (SHFMM) systems at the design stage.

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5

Wicaksana, F., A. G. Fan e V. Chen. "The relationship between critical flux and fibre movement induced by bubbling in a submerged hollow fibre system". Water Science and Technology 51, n. 6-7 (1 marzo 2005): 115–22. http://dx.doi.org/10.2166/wst.2005.0629.

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Bubbling has been used to enhance various processes. In this paper we deal with the effect of bubbling on submerged hollow fibre membranes, where bubbling is applied to prevent severe membrane fouling. Previous work with submerged hollow fibres has observed that significant fibre movement can be induced by bubbling and that there is a qualitative relationship between fibre movement and filtration performance. Therefore, the aim of the present research has been to analyse the link between bubbling, fibre movement and critical flux, identified as the flux at which the transmembrane pressure (TMP) starts to rise. Tests were performed on vertical isolated fibres with a model feed of yeast suspension. The fibres were subject to steady bubbling from below. The parameters of interest were the fibre characteristics, such as tightness, diameter and length, as well as feed concentration. The results confirmed that the critical fluxes are affected by the fibre characteristics and feed concentration. Higher critical flux values can be achieved by using loose fibres, smaller diameters and longer fibres. The enhancement is partially linked to fibre movement and this is confirmed by improved performance when fibres are subject to mechanical movement in the absence of bubbling.

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6

Chen, X. D., G. M. Ai e J. J. J. Chen. "Modelling Hollow-Fibre Ultrafiltration". Developments in Chemical Engineering and Mineral Processing 13, n. 1-2 (15 maggio 2008): 109–19. http://dx.doi.org/10.1002/apj.5500130111.

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7

Kling, Sándor, e Tibor Czigány. "Analysis of Applicability of the Hollow Carbon Fibres for Self-Repairing Composites". Materials Science Forum 729 (novembre 2012): 246–51. http://dx.doi.org/10.4028/www.scientific.net/msf.729.246.

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The geometry and mechanical properties of solid and hollow carbon fibres were investigated by light-and scanning electron microscopy, and by single fibre tensile tests. The hollowness factor of fibres was determined by their external and internal diameter. The tensile strength was determined by single fibre tensile break tests. It was shown that the bigger the diameter of the fibres the lower the mechanical properties is. It was found that the hollow carbon fibres are suitable for preparation of a self-repairing composite with the advantage over other solutions because of their geometrical and mechanical properties.

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8

Han, De Zhi, Xiao Yao Tan, Zi Feng Yan e Shao Min Liu. "Enhanced Oxygen Permeation of Pt-Modified La_0.6Sr_0.4Co_0.2Fe_0.8O_3-α Hollow Fibre Membranes". Advanced Materials Research 550-553 (luglio 2012): 630–33. http://dx.doi.org/10.4028/www.scientific.net/amr.550-553.630.

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Perovskite La0.6Sr0.4Co0.2Fe0.8O3-α(LSCF) hollow fibre membranes were fabricated by a combined phase inversion and sintering technique. The prepared membrane possessed a novel structure consisting of only one thin dense layer and one porous layer. A porous layer of platinum was coated on the outer surface of the hollow fibres to improve the surface exchange reactions. Oxygen permeation fluxes through both the original and modified hollow fibre membranes were measured under air/He gradients at different temperature. The results indicated that the oxygen permeation fluxes can be improved from the initial values of 0.17-1.58 ml cm-2min-1in the original hollow fibre membrane to 0.29-3.99 ml cm-2min-1in the Pt-modified membrane in the temperature range of 750-950 °C. An oxygen spillover mechanism has been put forward to explain the effect of Pt on the improvement of oxygen permeation fluxes.

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9

Abd Rahman, Norashidah, Siti Amirah Azra Khairuddin, Norwati Jamaluddin e Zainorizuan Mohd Jaini. "Strength of Reinforced Fibrous Foamed Concrete-Filled Hollow Section". Materials Science Forum 936 (ottobre 2018): 219–23. http://dx.doi.org/10.4028/www.scientific.net/msf.936.219.

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At present, research on concrete-filled sections extends to using lightweight concrete to reduce the total weight of such structures. However, research on concrete-filled hollow sections (CFHS) using foamed concrete remains ongoing. Therefore, this study was conducted to determine the strength of reinforced fibrous foamed CFHSs. Two types of fibre, namely, steel and polypropylene fibres, were used. A short-column specimen was prepared and tested under compression load. Result shows that adding steel fibre to foamed concrete indicates a higher strength than adding polypropylene fibre. The strength of the CFHS is increased by adding reinforced bar and fibre in foamed concrete.

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10

Abd Aziz, Mohd Haiqal, Mohd Hafiz Dzarfan Othman, Ahmad Fauzi Ismail, Mukhlis Abdul Rahman, Juhana Jaafar, Siti Khadijah Hubadillah e Tai Zhong Cheng. "Fabrication of low-cost ceramic hollow fiber membranes from aluminium dross waste for water purification". Malaysian Journal of Fundamental and Applied Sciences 15, n. 4 (25 agosto 2019): 483–88. http://dx.doi.org/10.11113/mjfas.v15n4.1210.

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In this study, alumina-spinel composite hollow fibre membranes were fabricated from abundantly available aluminium dross waste, which can be commonly obtained from aluminium-producing factory. The hollow fibre membranes were successfully fabricated by using a combine phase inversion method and sintering technique. The effects of sintering temperatures on morphology, mechanical strength, and permeability of the hollow fibre membranes were systematically investigated. X-ray fluorescence (XRF) was used to analyze the composition of the aluminium dross waste, while x-ray diffraction analysis (XRD) were further studied to characterize the major crystalline phase of the sintered hollow fibre membranes. An increase in sintering temperatures resulted in densification of hollow fibre membrane, consequently induced the flux reduction. The presence of spinel in microstructural of hollow fibre assisted in decreasing the sintering temperature. As comparison to pure alumina membrane counterparts, this alternative ceramic hollow fibre membrane exhibited a comparable mechanical strength of 78.3-155.1 MPa with lower sintering temperatures ranging from 1350 ˚C to 1400 ˚C at ceramic loading of 40%.

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Tesi sul tema "Hollow fibre"

1

Koonaphapdeelert, Sirichai. "Ceramic hollow fibre membrane contactors". Thesis, Imperial College London, 2009. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.501286.

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2

Wicaksana, Filicia School of Chemical Engineering &amp Industrial Chemistry UNSW. "Submerged hollow fibre membranes in bubbling systems". Awarded by:University of New South Wales. School of Chemical Engineering and Industrial Chemistry, 2006. http://handle.unsw.edu.au/1959.4/25998.

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This study focuses on the optimisation of submerged hollow fibre membrane performance by analysing the role of air sparging on the reduction of membrane fouling. In submerged hollow fibre membranes, rising bubbles have been shown to induce shear, liquid movement and fibre displacement. The interaction between fibre movement induced by bubbling and the microfiltration performance was assessed for various parameters (fibre tightness, fibre length, fibre diameter, air flowrate, nozzle size, and feed concentration). A model feed of yeast suspension and a series of isolated fibres were used. The fibre movement was assessed by monitoring the displacement using video recording. Bubble population parameters were also measured. The results suggest that bubbleinduced fibre movement plays an important role in controlling membrane fouling. Investigations of the critical flux at various operating conditions also supported these conclusions. Since energy consumption for aeration is a major contributor to the cost in submerged membranes, the potential to minimise the aeration cost has been tested by implementing intermittent aeration and different nozzle sizes. It was found that an optimum condition associated with a low fouling rate could be reached by combining various aeration intermittencies and nozzle sizes. An attempt to suppress fouling without aeration was made by incorporating vibrations into a submerged hollow fibre membrane system. The effects of vibration frequency, type of yeast (washed and unwashed) on the filtration performance were observed. The impact of coagulant addition on filtration enhancement was also analysed. The performance of microfiltration was evaluated based on its critical flux value. The findings in this preliminary study indicated potential fouling control by applying vibrations to submerged membranes. A semi-empirical model was developed to predict the filtration behaviour by taking into account the bubble-induced shear and fibre movement. The predicted critical flux values suggested that membrane fouling appears to be more prominent at low air flowrate, with tight fibres, and higher feed concentrations. The model fits the experimental data with discrepancies from approximately 0.3% to 20%. The predicted filtration profiles at different operating modes demonstrate the importance of bubble-induced shear and fibre movement in the improvement of filtration performance.

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3

Deshmukh, Sandeep Prabhakar. "Composite hollow fibre membranes for gas separation". Thesis, University of Leeds, 1993. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.423301.

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4

Shearer, Holly. "Hollow fibre bioreactors for bone tissue engineering". Thesis, University of Bath, 2007. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.441441.

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5

Zhou, Jian. "Polyacrylonitrile hollow fibre membranes for gas separation". Thesis, University of Leeds, 1996. http://etheses.whiterose.ac.uk/424/.

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Polyacrylonitrile (PAN) hollow fibres have been spun by a dry-jet wet spinning technique, using a commercial PAN polymer (Courtelle) redissolved in dimethylformamide (DMF). After failure to produce satisfactory porous hollow fibres from PAN/DMF solutions, a series of studies on the porous substructure of PAN cast films prepared with a variety of additives in the casting solution and at varying temperatures of the coagulation bath were carried out. A porous and flexible PAN cast film was produced when it was precipitated in water at 55 °C with CuSO4 present in the casting solution. Hollow fibres produced from a spinning solution composed of 25wt% PAN, 70wt% DMF and 5wt% CuSO4 were more porous and flexible than those produced from 25wt% PAN and 75wt% DMF spinning solution, and appeared to be more suitable for gas separation studies. The permeability of the PAN hollow fibre membranes to single gases was studied. The experimental results showed that the calculated pore radius on the surface of the fibre was in the range of 4- 32 nm. After coating with silicone rubber, the membranes showed very poor gas permeability and selectivity. Since PAN has a low intrinsic gas permeability, the low permeability observed is ascribed to a thick skin layer. The low selectivity of the membranes is related to their high surface porosity (> 10-4), or to the large pores present which are imperfectly blocked. With such fibres, little or no gas will pass through the membranes by solution-diffusion in the PAN. In order to reduce the surface porosity on the skin layer of the hollow fibres, a dualbath coagulation spinning system was used. The gas permeability of H2 in these membranes is lower than that obtained by the single bath coagulation system, while the gas permeability of the other gases, such as CO2 and CH4, were too low to measure. These results indicate that a high selectivity can be obtained by the dual bath coagulation spinning system although the selectivity is accompanied by too low a permeability, which is itself caused by too thick a skin layer. Surface modifications of PAN hollow fibre were carried out in order to modify the surface porosity of the fibres. After the treatments, the hollow fibre membranes did not give significant improvement in gas permeability and selectivity. But, when PAN hollow fibres were treated with cuprammonium hydroxide solution at room temperature, the fibres became coloured and no longer soluble in the usual solvents. The insolubility of the fibres is presumed to be due to a newly-formed crosslinked structure. The crosslinking of the fibres is reversed when the fibres are treated with EDTA solution. It has been observed that the presence of the copper in the fibres increases the tensile strength and decreases the elongation of the hollow fibres. The interaction of the PAN fibre with the cuprammonium hydroxide gave no improvement in gas separation performance but might be the basis for general acrylic fibre modification.

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6

Xu, Mengrong. "Advances in hollow core fibres and application to mid-infrared fibre gas lasers". Thesis, University of Bath, 2018. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.760959.

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Anti-resonant hollow core fibre is a new kind of optical fibre waveguide in which light is trapped in a hollow core surrounded by the capillary formed microstructured cladding. This fibre exhibits high damage threshold, low dispersion and ultra-low nonlinearity with relatively low loss of a few tens of dB/km. Its intrinsic feature of multimode delivery limits the applications with high requirements of single mode transmission. In my thesis, I demonstrate how the design of hollow core fibre can be improved with single mode guidance. S2 imaging measurement was used to analyse the mode content of the solid core fibres. In my research, I established S2 measurement to measure the mode contents in hollow core fibres for the first time. Two hollow core fibres with 8 capillaries and 7 capillaries in their claddings were fabricated in same fashion and showed differences in low attenuations. By comparing the mode contents in both of the fibres via S2 imaging measurement, 7-capillary HCF was demonstrated to give better performance on single mode guidance. Among the applications of the HCF, the property of delivering high power in HCF makes the gas filled HCF laser possible. In my research, a continuous-wave mid-infrared acetylene filled hollow core laser was built with a slope efficiency of 33% and an output power of over 1 watt at the wavelength region of 3.1~3.2 μm. The pump source is an Erbium-doped fibre amplified tunable laser diode which works at C-band wavelength. The fibre without the gain medium has two transmission bands with low attenuation of 0.037 dB/m and 0.063 dB/m at pumping and lasing wavelengths respectively. This laser system works in either cavity-based configuration or single pass ASE configuration. The latter configuration shows a better performance in high output power and high slope efficiency. The optimized laser system was studied experimentally with the proper fibre length and gas pressure. This laser system could be extended to be filled with other molecules to longer wavelengths and has potential for high power output.

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7

Zsirai, Tamas. "Fouling and clogging in hollow fibre membrane bioreactor". Thesis, Cranfield University, 2013. http://dspace.lib.cranfield.ac.uk/handle/1826/8411.

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The sustainability of a large pilot-scale hollow fibre immersed membrane bioreactor (HF iMBR) has been investigated with specific reference to membrane surface fouling and membrane channel clogging. Studies were conducted at normal sludge solids concentration of around 8 g/L and were also extended to concentrations more associated with thickening processes (around 32 g/L). A review of mechanically- moved membranes was conducted with a view to exploring a low energy means of sustaining operation through suppressing clogging. Methods were devised to quantify the amount of clogged solids within the membrane fibre bundle, either through their separation and gravimetric analysis or in-situ gravimetic estimation of the clogged solids without their removal from the membrane HF bundle. Outcomes generally revealed clogging to be as important a contributor to suppression of permeability as fouling, the key differentiator being that chemical cleaning had no sustained impact on permeability recovery when clogging took place. It was further substantiated that the operating permeability of membranes, once they had been clogged, could not be returned to that of the preclogged state despite declogging (i.e. mechanical removal of the solids) followed by the repeated application of chemically-enhanced backwashing. This was attributed to membrane pore plugging. Cont/d.

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8

Yeow, May Ling. "Fabrication of poly(vinylidene fluoride) hollow fibre membranes". Thesis, University of Bath, 2004. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.426179.

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9

Gbenedio, Ejirooghene Patrick. "Multifunctional inorganic hollow fibre membranes for chemical reactions". Thesis, Imperial College London, 2010. http://hdl.handle.net/10044/1/6415.

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Over the last few decades, the availability of inorganic membranes which can withstand high temperatures and harsh chemical environments has resulted in a wide range of opportunities for the application of membranes in chemical reactions. In particular, the combination of membrane separation and catalytic reaction in a single operating unit is an attractive way to increase conversions, to achieve better yields and to make more efficient use of natural resources in many reactions. In this work, a highly compact multifunctional Pd and Pd-Ag/alumina hollow fibre membrane reactor (HFMR) have been developed and applied to catalytic chemical reactions. The developed HFMR consists of a thin and defect free Pd-based membrane coated onto the outer surface of an alumina hollow fibre substrate with a unique asymmetric pore structure, i.e. a sponge-like outer layer and a finger-like inner layer where catalyst is deposited. In one study, a Pd-Ag layer was coated onto the outer surface of the substrate followed by deposition of sub-micron sized Pt(0.5wt.%)/γ-alumina catalysts into the finger-like voids of the substrates. This design achieved propane conversion as high as 42 % at the initial stage of the reaction at 723 K and space-time yields (STY) of the HFMR were approximately 60 times higher than that of a fixed bed reactor (FBR). In order to further increase catalytic surface area in the reaction zone, a sol-gel method was used to deposit Pt(1 wt.%)/SBA-15 catalysts into the finger-like voids of a substrate to develop a Pd/alumina HFMR. Benefiting from this novel design, the functionalized alumina hollow fibre substrates with surface area/volume values of up to 1918.4 m2/m3 possess a specific surface area of about 31.8 m2/g for catalysts. It was observed that in comparison with a conventional FBR, greater propene selectivity and propene yield was achieved by using the HFMR for propane dehydrogenation. The generic advantages of the design of these compact HFMR systems can be applied to further applications such as the water-gas shift reaction, which was also carried out in this study.

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Gouveia, Gil Ana Maria. "Catalytic hollow fibre membrane reactors for H2 production". Thesis, Imperial College London, 2015. http://hdl.handle.net/10044/1/39795.

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Pre-combustion decarbonisation is one of the three main routes widely discussed for CO2 capture from fossil fuels. This thesis focuses on the development of a catalytic hollow fibre membrane reactor for the combined steam methane reforming (SMR) and water-gas shift (WGS) reaction, using a Ni-based catalyst, and at a temperature window suitable for harvesting pure H2, a clean energy carrier, from the reaction by a Pd membrane. Apart from developing the catalyst and the Pd-based composite membrane, which are normally considered as the two essential components of a membrane reactor involving hydrogen separation, this study introduces the concept of incorporating the catalyst into a micro-structured ceramic hollow fibre substrate to promote mass transfer efficiency. Meanwhile, the impact of each fabrication step, i.e. catalyst composition and preparation, ceramic hollow fibre fabrication, catalyst incorporation and electroless plating of Pd membranes, on the assembly and final performance of the catalytic hollow fibre membrane reactor was systematically evaluated. In contrast to previous studies involving micro-structured ceramic hollow fibres for catalytic reactions, the one developed in this study possesses a plurality of unique micro-channels, with significant openings on the inner surface of the ceramic hollow fibre. In addition to reduced mass transfer resistance for both catalytic reaction and hydrogen permeation, a microstructure of this type significantly facilitates catalyst incorporation and, as a results, enable the application of this hollow fibres for a wider spectrum of catalytic reactions.

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Libri sul tema "Hollow fibre"

1

Love, Adrian. Hollow Core Optical Fibre Based Gas Discharge Laser Systems. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-93970-4.

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2

Walters, Blake. The importance of diffusion relaxation components in the NMR of tissue: An experimental investigation using hollow fibre bundles. Ottawa: National Library of Canada = Bibliothèque nationale du Canada, 1993.

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3

Fire Hollow. Ward Hill, MA: Raven's Wing, 2010.

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4

Odderstol, Eric S. Hydraulic modeling and economic optimization of hollow fiber membranes. Springfield, Va: Available from the National Technical Information Service, 1991.

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5

Zander, Amy K. Hollow fiber stripping analysis (HFSA) for taste and odor quantification. Denver, CO: AWWA Research Foundation and American Water Works Association, 1996.

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6

Mines, United States Bureau of. Calamity Hollow Mine Fire Project (in Five Parts) 5. Excavation and Evaluation of the Fire Zone. S.l: s.n, 1986.

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Gollan, Arye. Research into an asynetric membrane hollow fiber device for oxygen enriched air production. Washington, D.C: United States, Department of Energy, 1985.

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8

Arahman, Nasrul. Development and modification of polyethersulfone hollow fiber membrane for water purification of ground water in tsunami affected area: International research collaboration and scientific publication : report 3rd year. Banda Aceh: University of Syiah Kuala, 2012.

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Arahman, Nasrul. Development and modification of polyethersulfone hollow fiber membrane for water purification of ground water in tsunami affected area of Banda Aceh: Report competitive grant for international research collaboration and publication. Banda Aceh: University of Syiah Kuala, 2010.

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10

Board, United States National Transportation Safety. Marine accident report: Ramming of the Eads Bridge by barges in tow on the M/V Anne Holly with subsequent ramming and near breakaway of the President Casino on the Admiral, St. Louis Harbor, Missouri, April 4, 1998. Washington, D.C: The Board, 2000.

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Capitoli di libri sul tema "Hollow fibre"

1

Nagy, Endre. "Hollow Fibre Enzymatic Reactor, Modeling of". In Encyclopedia of Membranes, 1–2. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-40872-4_1243-1.

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2

Schönherr, O. T. "Cell Culture in Hollow Fibre Bioreactors". In Advanced Research on Animal Cell Technology, 107–17. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-0875-8_8.

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3

Kingsbury, Benjamin F. K., Zhentao Wu e K. Li. "Inorganic Hollow Fibre Membranes for Chemical Reaction". In Membranes for Membrane Reactors, 117–53. Chichester, UK: John Wiley & Sons, Ltd, 2011. http://dx.doi.org/10.1002/9780470977569.ch3.

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4

Piatkiewicz, W., J. Wojcicki, D. Falkenhagen, H. Klinkmann, H. Goch e M. Hay. "Hollow Fibre Based Modules For Blood Purification". In The Influence of New Technology on Medical Practice, 67–74. London: Macmillan Education UK, 1988. http://dx.doi.org/10.1007/978-1-349-09609-1_12.

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5

Jones, A. F., J. A. King-Hele e P. T. Cardew. "A Mathematical Model of a Hollow-Fibre Filter". In Progress in Industrial Mathematics at ECMI 96, 50–57. Wiesbaden: Vieweg+Teubner Verlag, 1997. http://dx.doi.org/10.1007/978-3-322-96688-9_6.

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6

Cadwell, John J. S., e William G. Whitford. "Three-dimensional cell-based assays in hollow fibre bioreactors". In Technology Platforms for 3D Cell Culture, 327–50. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781118851647.ch14.

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7

Al-Saadi, A., T. Aravinthan e W. Lokuge. "Numerical Investigation on Hollow Pultruded Fibre Reinforced Polymer Tube Columns". In Lecture Notes in Civil Engineering, 455–65. Singapore: Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-7603-0_45.

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Gerber, Heidi, e Kenneth McCullough. "Serum-Free Monoclonal Antibody Production in a Hollow Fibre Bioreactor". In Animal Cell Technology: Developments Towards the 21st Century, 181–86. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0437-1_29.

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9

Shnyder, Steven D. "Use of the Hollow Fibre Assay for Studies on Tumor Neovasculature". In Methods in Molecular Biology, 331–42. Totowa, NJ: Humana Press, 2008. http://dx.doi.org/10.1007/978-1-59745-241-0_21.

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10

Davis, J. M., C. M. Lavender, K. J. Bowes, J. A. J. Hanak, B. S. Combridge e S. L. Kingsland. "Human Therapeutic Monoclonal Anti-D Antibody Produced in Long-Term Hollow-Fibre Culture". In Animal Cell Technology: Developments Towards the 21st Century, 149–53. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0437-1_24.

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Atti di convegni sul tema "Hollow fibre"

1

Bartuli, Erik, e Tereza Kroulikova. "Testing of Polymeric Hollow Fibre Heat Exchanger with Crossed Hollow Fibres". In The 5th World Congress on Mechanical, Chemical, and Material Engineering. Avestia Publishing, 2019. http://dx.doi.org/10.11159/htff19.143.

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2

Perrella, C., J. Anstie, P. Light, F. Benabid, A. G. White e A. N. Luiten. "Hollow-core fibre frequency standard". In 2014 IEEE International Frequency Control Symposium (FCS). IEEE, 2014. http://dx.doi.org/10.1109/fcs.2014.6859855.

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3

West, J. A., E. M. Kosik Williams e K. W. Koch. "Hollow-core rib waveguide sensor". In 19th International Conference on Optical Fibre Sensors, a cura di David D. Sampson. SPIE, 2008. http://dx.doi.org/10.1117/12.786116.

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4

Vincetti, L., e A. Polemi. "Hollow core fibre for THz applications". In 2009 IEEE Antennas and Propagation Society International Symposium (APSURSI). IEEE, 2009. http://dx.doi.org/10.1109/aps.2009.5171653.

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5

Yerolatsitis, S., R. Shurvinton, Peng Song, R. J. A. Francis-Jones e K. R. Rusimova. "Birefringent anti-resonant hollow-core fibre". In 45th European Conference on Optical Communication (ECOC 2019). Institution of Engineering and Technology, 2019. http://dx.doi.org/10.1049/cp.2019.0850.

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6

Nellikka, Apurv Chaitanya, Jabir M. V., J. Banerji e G. K. Samanta. "Nonlinear Generation of Hollow Gaussian Beam". In International Conference on Fibre Optics and Photonics. Washington, D.C.: OSA, 2016. http://dx.doi.org/10.1364/photonics.2016.tu4a.25.

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7

Stefani, Alessio, Richard Lwin, Alexander Argyros e Simon Fleming. "Hollow-Core Antiresonant Fibers with a Twist". In Australian Conference on Optical Fibre Technology. Washington, D.C.: OSA, 2016. http://dx.doi.org/10.1364/acoft.2016.aw4c.4.

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8

Jiang, X., T. G. Euser, A. Abdolvand, F. Babic, N. Joly e P. St J. Russell. "SF6 glass hollow-core photonic crystal fibre". In 12th European Quantum Electronics Conference CLEO EUROPE/EQEC. IEEE, 2011. http://dx.doi.org/10.1109/cleoe.2011.5942792.

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9

LEMOS, C. O. T., F. B. da SILVA, M. H. M. REIS, A. M. G. GIL e K. LI. "CHARACTERISATION OF ASYMMETRIC ALUMINA HOLLOW FIBRE MEMBRANES". In XX Congresso Brasileiro de Engenharia Química. São Paulo: Editora Edgard Blücher, 2015. http://dx.doi.org/10.5151/chemeng-cobeq2014-0669-24512-156188.

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10

Argyros, Alexander, e Jarryd Pla. "Hollow-core kagome lattice polymer optical fibres". In 2006 Australian Conference on Optical Fibre technology (ACOFT). IEEE, 2007. http://dx.doi.org/10.1109/acoft.2007.4516299.

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Rapporti di organizzazioni sul tema "Hollow fibre"

1

Ma, Yi Hua, W. Moser, A. Shelekhin e Shyhing Pien. Hollow fiber catalytic membranes. Office of Scientific and Technical Information (OSTI), settembre 1993. http://dx.doi.org/10.2172/10184061.

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2

Kandil, Sherif M. Nano-Engineered Porous Hollow Fiber Membrane-Based AC System. Office of Scientific and Technical Information (OSTI), settembre 2014. http://dx.doi.org/10.2172/1155013.

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3

EVANS, LINDSEY, e JAMES E. MILLER. Sweeping Gas Membrane Desalination Using Commercial Hydrophobic Hollow Fiber Membranes. Office of Scientific and Technical Information (OSTI), gennaio 2002. http://dx.doi.org/10.2172/793312.

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4

Rosinski, Andrew, Garrett Swindlehurst, Hai Du, Ryan P. Lively, Yoshiaki Kawajiri, Matthew Realff, William J. Koros et al. Improving Energy Efficiency of Air Separation via Hollow Fiber Sorbents. Office of Scientific and Technical Information (OSTI), marzo 2019. http://dx.doi.org/10.2172/1503603.

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5

Corwin, Kristan L., Brian R. Washburn, Wolfgang Rudolph, Vasudevan Nampoothiri e Fetah Benabid. Gas-Filled Hollow Core Fiber Lasers Based on Population Inversion. Fort Belvoir, VA: Defense Technical Information Center, dicembre 2013. http://dx.doi.org/10.21236/ada593591.

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6

Nenoff, Tina M., Sarah E. Moore, Sera Mirchandani, Vasiliki Karanikola, Robert G. Arnold e Eduardo Saez. Multi-objective Optimization of Solar-driven Hollow-fiber Membrane Distillation Systems. Office of Scientific and Technical Information (OSTI), settembre 2017. http://dx.doi.org/10.2172/1395756.

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7

Washburn, Brian R., e Kristan L. Corwin. Molecular Gas-Filled Hollow Optical Fiber Lasers in the Near Infrared. Fort Belvoir, VA: Defense Technical Information Center, gennaio 2012. http://dx.doi.org/10.21236/ada563791.

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8

Deng, S., T. Liu, S. Sourirajan, T. Matsuura e B. Farnand. A study of volatile hydrocarbon emission control by polyetherimide hollow fiber membranes. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1994. http://dx.doi.org/10.4095/304620.

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9

Ma, Y. H., W. R. Moser, S. Pien e A. B. Shelekhin. Development of hollow fiber catalytic membrane reactors for high temperature gas cleanup. Office of Scientific and Technical Information (OSTI), ottobre 1994. http://dx.doi.org/10.2172/10185653.

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10

Ma, Yi H., M. R. Moser e S. M. Pien. Development of hollow-fiber catalytic-membrane reactors for high-temperature gas cleanup. Office of Scientific and Technical Information (OSTI), dicembre 1992. http://dx.doi.org/10.2172/10110112.

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