Understanding water and ion transport behaviour and permeability through poly(amide) thin film composite membrane

Molecular dynamics (MD) together with the adaptive biasing force (ABF) and metadynamics free energy calculation methods was used to investigate the permeation properties of salt water through poly(amide) thin film composite reverse osmosis membranes. The thin films were generated by annealing an amorphous cell of poly(amide) chains through an MD method. The MD results showed they have typical structural properties of the active layer of thin film composite membranes and comparable water diffusivity (2.13×10^-5cm²/s for the film with a density of 1.06g/cm³) and permeability (9.27×10^-15cm³cm/cm²sPa) to experimental data. The simulations of water permeation through the films under different transmembrane pressures revealed the behaviours of water molecules in the thin films and the dynamic regimes of water permeation, including Brownian diffusion, flush and jump diffusion regimes. The intermolecular interactions of water and ions with poly(amide) chains showed a strong dependence on the local structure of films. The attraction between water and ploy(amide) molecules can be up to 8.5kcal/mol in dense polymer regions and 5kcal/mol in the pores of about 3nm. The ABF and metadynamics simulations produced the profiles of free energy potential of water and ions along the depth of the thin films, which provided important information for quantitatively determining the barrier energy required for water permeation and rejection of ions. The thin film with a density of 1.06g/cm³ and a thickness of 6nm offers a rejection to Na⁺ but a slight absorption of Cl^- (0.25kcal/mol) at 0.3-0.4nm distance to its surface. Water molecules must overcome 63kcal/mol energy to move to the centre of the film. The dependences of the barrier energy and the water-polymer interaction energy on the local free volume size in the thin film were analysed. The simulations of water permeation under high transmembrane pressures showed a nonlinear response of the concentration and distribution of water molecules in the film to the imposed pressure. Compaction of the film segments close to the porous substrate and water congestion in dense regions significantly influenced the water permeation when the membrane was operated under pressures of more than 3.0MPa.

Ultraviolet-B and water stress effects on growth, gas exchange and oxidative stress in sunflower plants

The effects and interaction of drought and UV-B radiation were studied in sunflower plants (Helianthus annuus L. var. Catissol-01), growing in a greenhouse under natural photoperiod conditions. The plants received approximately 1.7 W m(-2) (controls) or 8.6 W m(-2) (+UV-B) of UV-B radiation for 7 h per day. The UV-B and water stress treatments started 18 days after sowing. After a period of 12 days of stress, half of the water-stressed plants (including both UV-B irradiated or non-irradiated) were rehydrated. Both drought and UV-B radiation treatments resulted in lower shoot dry matter per plant, but there was no significant interaction between the two treatments. Water stress and UV-B radiation reduced photosynthesis, stomatal conductance and transpiration. However, the amplitude of the effects of both stressors was dependent on the interactions. This resulted in alleviation of the negative effect of drought on photosynthesis and transpiration by UV-B radiation as the water stress intensified. Intercelluar CO(2) concentration was initially reduced in all treatments compared to control plants but it increased with time. Photosynthetic pigments were not affected by UV-B radiation. Water stress reduced photosynthetic pigments only under high UV-B radiation. The decrease was more accentuated for chlorophyll a than for chlorophyll b. As a measure for the maximum efficiency of photosystem II in darkness F (v)/F (m) was used, which was not affected by drought stress but initially reduced by UV-B radiation. Independent of water supply, UV-B radiation increased the activity of pirogalol peroxidase and did not increase the level of malondialdehyde. on the other hand, water stress did not alter the activity of pirogalol peroxidase and caused membrane damage as assessed by lipid peroxidation. The application of UV-B radiation together with drought seemed to have a protective effect by lowering the intensity of lipid peroxidation caused by water stress. The content of proline was not affected by UV-B radiation but was increased by water stress under both low and high UV-B radiation. After 24 h of rehydration, most of the parameters analyzed recovered to the same level as the unstressed plants.

An electrochemical gas sensor based on paper supported room temperature ionic liquids

A sensitive and fast-responding membrane-free amperometric gas sensor is described, consisting of a small filter paper foil soaked with a room temperature ionic liquid (RTIL), upon which three electrodes are screen printed with carbon ink, using a suitable mask. It takes advantage of the high electrical conductivity and negligible vapour pressure of RTILs as well as their easy immobilization into a porous and inexpensive supporting material such as paper. Moreover, thanks to a careful control of the preparation procedure, a very close contact between the RTIL and electrode material can be achieved so as to allow gaseous analytes to undergo charge transfer just as soon as they reach the three-phase sites where the electrode material, paper supported RTIL and gas phase meet. Thus, the adverse effect on recorded currents of slow steps such as analyte diffusion and dissolution in a solvent is avoided. To evaluate the performance of this device, it was used as a wall-jet amperometric detector for flow injection analysis of 1-butanethiol vapours, adopted as the model gaseous analyte, present in headspace samples in equilibrium with aqueous solutions at controlled concentrations. With this purpose, the RTIL soaked paper electrochemical detector (RTIL-PED) was assembled by using 1-butyl-3-methylimidazolium bis(trifluoromethanesulfonyl) imide as the wicking RTIL and printing the working electrode with carbon ink doped with cobalt(II) phthalocyanine, to profit from its ability to electrocatalyze thiol oxidation. The results obtained were quite satisfactory (detection limit: 0.5 mu M; dynamic range: 2-200 mu M, both referring to solution concentrations; correlation coefficient: 0.998; repeatability: +/- 7% RSD; long-term stability: 9%), thus suggesting the possible use of this device for manifold applications.

Movement of NH3 through the human urea transporter B: a new gas channel

Aquaporins and Rh proteins can function as gas (CO2 and NH3) channels. The present study explores the urea, H2O, CO2, and NH3 permeability of the human urea transporter B (UT-B) (SLC14A1), expressed in Xenopus oocytes. We monitored urea uptake using [14C]urea and measured osmotic water permeability (Pf) using video microscopy. To obtain a semiquantitative measure of gas permeability, we used microelectrodes to record the maximum transient change in surface pH (∆pHS) caused by exposing oocytes to 5% CO2/33 mM HCO3- (pHS increase) or 0.5 mM NH3/NH4+ (pHS decrease). UT-B expression increased oocyte permeability to urea by >20-fold, and Pf by 8-fold vs. H2O-injected control oocytes. UT-B expression had no effect on the CO2-induced ∆pHS but doubled the NH3-induced ∆pHS. Phloretin reduced UT-B-dependent urea uptake (Jurea * ) by 45%, Pf * by 50%, and (- ∆pHS * )NH3 by 70%. p-Chloromercuribenzene sulfonate reduced Jurea * by 25%, Pf * by 30%, and (∆pHS * )NH3 by 100%. Molecular dynamics (MD) simulations of membrane-embedded models of UT-B identified the monomeric UT-B pores as the main conduction pathway for both H2O and NH3 and characterized the energetics associated with permeation of these species through the channel. Mutating each of two conserved threonines lining the monomeric urea pores reduced H2O and NH3 permeability. Our data confirm that UT-B has significant H2O permeability and for the first time demonstrate significant NH3 permeability. Thus the UTs become the third family of gas channels. Inhibitor and mutagenesis studies and results of MD simulations suggest that NH3 and H2O pass through the three monomeric urea channels in UT-B.

Fenomeni di trasporto ed elettrostatici in membrane da Nanofiltrazione

Fenomeni di trasporto ed elettrostatici in membrane da Nanofiltrazione La capacità di predire le prestazioni delle membrane da nanofiltrazione è molto importante per il progetto e la gestione di processi di separazione a membrana. Tali prestazioni sono strettamente legate ai fenomeni di trasporto che regolano il moto dei soluti all’interno della matrice della membrana. Risulta, quindi, di rilevante importanza la conoscenza e lo studio di questi fenomeni; l’obiettivo finale è quello di mettere a punto modelli di trasporto appropriati che meglio descrivano il flusso dei soluti all’interno della membrana. A fianco dei modelli di trasporto ricopre, quindi, una importanza non secondaria la caratterizzazione dei parametri aggiustabili propri della membrana sulla quale si opera. La procedura di caratterizzazione di membrane deve chiarire le modalità di svolgimento delle prove sperimentali e le finalità che esse dovrebbero conseguire. Tuttavia, nonostante i miglioramenti concernenti la modellazione del trasporto di ioni in membrana ottenuti dalla ricerca negli ultimi anni, si è ancora lontani dall’avere a disposizione un modello univoco in grado di descrivere i fenomeni coinvolti in maniera chiara. Oltretutto, la palese incapacità del modello di non riuscire a prevedere gli andamenti sperimentali di reiezione nella gran parte dei casi relativi a miscele multicomponenti e le difficoltà legate alla convergenza numerica degli algoritmi risolutivi hanno fortemente limitato gli sviluppi del processo anche e soprattutto in termini applicativi. Non da ultimo, si avverte la necessità di poter prevedere ed interpretare l’andamento della carica di membrana al variare delle condizioni operative attraverso lo sviluppo di un modello matematico in grado di descrivere correttamente il meccanismo di formazione della carica. Nel caso di soluzioni elettrolitiche, infatti, è stato riconosciuto che la formazione della carica superficiale è tra i fattori che maggiormente caratterizzano le proprietà di separazione delle membrane. Essa gioca un ruolo importante nei processi di trasporto ed influenza la sua selettività nella separazione di molecole caricate; infatti la carica di membrana interagisce elettrostaticamente con gli ioni ed influenza l’efficienza di separazione degli stessi attraverso la partizione degli elettroliti dalla soluzione esterna all’interno dei pori del materiale. In sostanza, la carica delle membrane da NF è indotta dalle caratteristiche acide delle soluzioni elettrolitiche poste in contatto con la membrana stessa, nonché dal tipo e dalla concentrazione delle specie ioniche. Nello svolgimento di questo lavoro sono stati analizzati i principali fenomeni di trasporto ed elettrostatici coinvolti nel processo di nanofiltrazione, in particolare si è focalizzata l’attenzione sugli aspetti relativi alla loro modellazione matematica. La prima parte della tesi è dedicata con la presentazione del problema generale del trasporto di soluti all’interno di membrane da nanofiltrazione con riferimento alle equazioni alla base del modello DSP&DE, che rappresenta una razionalizzazione dei modelli esistenti sviluppati a partire dal modello DSPM, nel quale sono stati integrarti i fenomeni di esclusione dielettrica, per quanto riguarda la separazione di elettroliti nella filtrazione di soluzioni acquose in processi di Nanofiltrazione. Il modello DSP&DE, una volta definita la tipologia di elettroliti presenti nella soluzione alimentata e la loro concentrazione, viene completamente definito da tre parametri aggiustabili, strettamente riconducibili alle proprietà della singola membrana: il raggio medio dei pori all’interno della matrice, lo spessore effettivo e la densità di carica di membrana; in più può essere considerato un ulteriore parametro aggiustabile del modello il valore che la costante dielettrica del solvente assume quando confinato in pori di ridotte dimensioni. L’impostazione generale del modello DSP&DE, prevede la presentazione dei fenomeni di trasporto all’interno della membrana, descritti attraverso l’equazione di Nerst-Planck, e lo studio della ripartizione a ridosso dell’interfaccia membrana/soluzione esterna, che tiene in conto di diversi contributi: l’impedimento sterico, la non idealità della soluzione, l’effetto Donnan e l’esclusione dielettrica. Il capitolo si chiude con la presentazione di una procedura consigliata per la determinazione dei parametri aggiustabili del modello di trasporto. Il lavoro prosegue con una serie di applicazioni del modello a dati sperimentali ottenuti dalla caratterizzazione di membrane organiche CSM NE70 nel caso di soluzioni contenenti elettroliti. In particolare il modello viene applicato quale strumento atto ad ottenere informazioni utili per lo studio dei fenomeni coinvolti nel meccanismo di formazione della carica; dall’elaborazione dei dati sperimentali di reiezione in funzione del flusso è possibile ottenere dei valori di carica di membrana, assunta quale parametro aggiustabile del modello. che permettono di analizzare con affidabilità gli andamenti qualitativi ottenuti per la carica volumetrica di membrana al variare della concentrazione di sale nella corrente in alimentazione, del tipo di elettrolita studiato e del pH della soluzione. La seconda parte della tesi relativa allo studio ed alla modellazione del meccanismo di formazione della carica. Il punto di partenza di questo studio è rappresentato dai valori di carica ottenuti dall’elaborazione dei dati sperimentali di reiezione con il modello di trasporto, e tali valori verranno considerati quali valori “sperimentali” di riferimento con i quali confrontare i risultati ottenuti. Nella sezione di riferimento è contenuta la presentazione del modello teorico “adsorption-amphoteric” sviluppato al fine di descrivere ed interpretare i diversi comportamenti sperimentali ottenuti per la carica di membrana al variare delle condizioni operative. Nel modello la membrana è schematizzata come un insieme di siti attivi di due specie: il gruppo di siti idrofobici e quello de siti idrofilici, in grado di supportare le cariche derivanti da differenti meccanismi chimici e fisici. I principali fenomeni presi in considerazione nel determinare la carica volumetrica di membrana sono: i) la dissociazione acido/base dei siti idrofilici; ii) il site-binding dei contro-ioni sui siti idrofilici dissociati; iii) l’adsorbimento competitivo degli ioni in soluzione sui gruppi funzionali idrofobici. La struttura del modello è del tutto generale ed è in grado di mettere in evidenza quali sono i fenomeni rilevanti che intervengono nel determinare la carica di membrana; per questo motivo il modello permette di indagare il contributo di ciascun meccanismo considerato, in funzione delle condizioni operative. L’applicazione ai valori di carica disponibili per membrane Desal 5-DK nel caso di soluzioni contenenti singoli elettroliti, in particolare NaCl e CaCl2 permette di mettere in evidenza due aspetti fondamentali del modello: in primis la sua capacità di descrivere andamenti molto diversi tra loro per la carica di membrana facendo riferimento agli stessi tre semplici meccanismi, dall’altra parte permette di studiare l’effetto di ciascun meccanismo sull’andamento della carica totale di membrana e il suo peso relativo. Infine vengono verificate le previsioni ottenute con il modello dal suddetto studio attraverso il confronto con dati sperimentali di carica ottenuti dall’elaborazione dei dati sperimentali di reiezione disponibili per il caso di membrane CSM NE70. Tale confronto ha messo in evidenza le buone capacità previsionali del modello soprattutto nel caso di elettroliti non simmetrici quali CaCl2 e Na2SO4. In particolare nel caso un cui lo ione divalente rappresenta il contro-ione rispetto alla carica propria di membrana, la carica di membrana è caratterizzata da un andamento unimodale (contraddistinto da un estremante) con la concentrazione di sale in alimentazione. Il lavoro viene concluso con l’estensione del modello ADS-AMF al caso di soluzioni multicomponenti: è presentata una regola di mescolamento che permette di ottenere la carica per le soluzioni elettrolitiche multicomponenti a partire dai valori disponibili per i singoli ioni componenti la miscela.

Caratterizzazione di membrane metalliche e ionomeriche per applicazioni energetiche

The work of this thesis has been focused on the characterization of metallic membranes for the hydrogen purification from steam reforming process and also of perfluorosulphonic acid ionomeric (PFSI) membranes suitable as electrolytes in fuel cell applications. The experimental study of metallic membranes was divided in three sections: synthesis of palladium and silver palladium coatings on porous ceramic support via electroless deposition (ELD), solubility and diffusivity analysis of hydrogen in palladium based alloys (temperature range between 200 and 400 °C up to 12 bar of pressure) and permeation experiments of pure hydrogen and mixtures containing, besides hydrogen, also nitrogen and methane at high temperatures (up to 600 °C) and pressures (up to 10 bar). Sequential deposition of palladium and silver on to porous alumina tubes by ELD technique was carried out using two different procedures: a stirred batch and a continuous flux method. Pure palladium as well as Pd-Ag membranes were produced: the Pd-Ag membranes’ composition is calculated to be close to 77% Pd and 23% Ag by weight which was the target value that correspond to the best performance of the palladium-based alloys. One of the membranes produced showed an infinite selectivity through hydrogen and relatively high permeability value and is suitable for the potential use as a hydrogen separator. The hydrogen sorption in silver palladium alloys was carried out in a gravimetric system on films produced by ELD technique. In the temperature range inspected, up to 400°C, there is still a lack in literature. The experimental data were analyzed with rigorous equations allowing to calculate the enthalpy and entropy values of the Sieverts’ constant; the results were in very good agreement with the extrapolation made with literature data obtained a lower temperature (up to 150 °C). The information obtained in this study would be directly usable in the modeling of hydrogen permeation in Pd-based systems. Pure and mixed gas permeation tests were performed on Pd-based hydrogen selective membranes at operative conditions close to steam-reforming ones. Two membranes (one produced in this work and another produced by NGK Insulators Japan) showed a virtually infinite selectivity and good permeability. Mixture data revealed the existence of non negligible resistances to hydrogen transport in the gas phase. Even if the decrease of the driving force due to polarization concentration phenomena occurs, in principle, in all membrane-based separation systems endowed with high perm-selectivity, an extensive experimental analysis lack, at the moment, in the palladium-based membrane process in literature. Moreover a new procedure has been introduced for the proper comparison of the mass transport resistance in the gas phase and in the membrane. Another object of study was the water vapor sorption and permeation in PFSI membranes with short and long side chains was also studied; moreover the permeation of gases (i.e. He, N2 and O2) in dry and humid conditions was considered. The water vapor sorption showed strong interactions between the hydrophilic groups and the water as revealed from the hysteresis in the sorption-desorption isotherms and thermo gravimetric analysis. The data obtained were used in the modeling of water vapor permeation, that was described as diffusion-reaction of water molecules, and in the humid gases permeation experiments. In the dry gas experiments the permeability and diffusivity was found to increase with temperature and with the equivalent weight (EW) of the membrane. A linear correlation was drawn between the dry gas permeability and the opposite of the equivalent weight of PFSI membranes, based on which the permeability of pure PTFE is retrieved in the limit of high EW. In the other hand O2 ,N2 and He permeability values was found to increase significantly, and in a similar fashion, with water activity. A model that considers the PFSI membrane as a composite matrix with a hydrophilic and a hydrophobic phase was considered allowing to estimate the variation of gas permeability with relative humidity on the basis of the permeability in the dry PFSI membrane and in pure liquid water.

Integrazione tecnologica di grafene cresciuto per deposizione chimica da fase vapore per applicazioni termiche e termoelettriche

L’obiettivo del lavoro di tesi è quello di studiare l’integrazione del grafene con i processi tecnologici propri della tecnologia del silicio, per la realizzazione di dispositivi innovativi per la misura delle proprietà termiche e termoelettriche del grafene che sono tra le meno studiate ad oggi. L’attività sperimentale svolta, ha riguardato l’intero processo di produzione, processing ed integrazione tecnologica del grafene. Da una parte è stato messo a punto un processo ottimizzato, partendo da una approfondita ricerca bibliografica, per il trasferimento delle membrane dai substrati di crescita, in rame, a quelli di destinazione, SiO2 e Si3N4, mantenendo la completa compatibilità con i processi della microelettronica del silicio in particolare per quanto riguarda l’eliminazione dei residui metallici dalla sintesi. Dall’altra è stata sviluppata una procedura di patterning micrometrico del grafene, affidabile e riproducibile, e, soprattutto, compatibile con la microelettronica del silicio. Le membrane, cresciute tramite deposizione da fase vapore (Chemical Vapor Deposition), sono state caratterizzate tramite la microscopia elettronica, a scansione e in trasmissione, la microscopia ottica, spettroscopia Raman e microscopia a forza atomica, tecniche che sono state utilizzate per caratterizzare i campioni durante l'intero processo di patterning. Il processo di etching del grafene in ossigeno, realizzato con il plasma cleaner, strumento che nasce per la pulizia di campioni per microscopia elettronica, è stato messo a punto il attraverso una estesa attività di test sia dei parametri di funzionamento dello strumento che del fotoresist da utilizzare. La procedura di patterning micrometrico vera e propria, ha comportato di affrontare diverse classi di problemi, dalla rimozione del fotoresist con soluzioni diverse (soluzione di sviluppo dedicata e/o acetone) alla rimozione dei residui presenti sulle membrane di grafene anche a valle del patterning stesso. La rimozione dei residui tramite acido cloridrico, insieme ad una procedura di annealing a 400°C in aria per la rimozione dei residui del fotoresist polimerico che erano presenti a valle dell’etching in ossigeno, ha permesso di ottenere un patterning del grafene ben definito su scala micrometrica e una ridottissima presenza di residui. Le procedure ottimizzate di trasferimento e di patterning sono il principale avanzamento rispetto allo stato dell’arte. Le metodiche messe a punto in questo lavoro, consentiranno di integrare il grafene direttamente nel processo di micro-fabbricazione di dispositivi per misure termiche e termoelettriche, per i quali quali sono in realizzazione le maschere di processo che rappresentando la naturale conclusione del lavoro di tesi.

Preparazione e caratterizzazione di coating grafenici su film polimerici per proprietà barriera ai gas

In questo elaborato è stata discussa la preparazione di coating grafenici su film polimerici per migliorare le proprietà barriera ai gas. Le tecniche impiegate per l’applicazione dei coating sono basate sulla teoria dell’accrescimento layer by layer e sul trasferimento a pressione di materiale filtrato. Queste tecniche sono state riprodotte in laboratorio su tre tipologie di grafene: ossido di grafene, grafene sospeso in acqua e polvere di grafene commerciale per osservare le condizioni operative e i risultati. Dagli esperimenti condotti si sono ottenuti campioni che sono stati testati su uno strumento per la misura della permeabilità ai gas. Nello stesso periodo è stato messo a punto un metodo analitico spettrofotometrico per la stima della concentrazione di grafene all’interno di soluzioni e sospensioni.

Epithelial transformations in the establishment of the blood-gas barrier in the developing chick embryo lung

The tall epithelium of the developing chick embryo lung is converted to a squamous one, which participates in formation of the thin blood-gas barrier. We show that this conversion occurred through processes resembling exocrine secretion. Initially, cells formed intraluminal protrusions (aposomes), and then transcellular double membranes were established. Gaps between the membranes opened, thus, severing the aposome from the cell. Alternatively, aposomes were squeezed out by adjacent cells or were spontaneously constricted and extruded. As a third mechanism, formation and fusion of severed vesicles or vacuoles below the aposome and their fusion with the apicolateral plasma membrane resulted in severing of the aposome. The atria started to form by progressive epithelial attenuation and subsequent invasion of the surrounding mesenchyme at regions delineated by subepithelial alpha-smooth muscle actin-positive cells. Further epithelial attenuation was achieved by vacuolation; rupture of such vacuoles with resultant numerous microfolds and microvilli, which were abscised to accomplish a smooth squamous epithelium just before hatching.

Comparing oxygen transfer performance between three membrane oxygenators: effect of temperature changes during cardiopulmonary bypass

Recently, a new oxygenator (Dideco 903 [D903], Dideco, Mirandola, Italy) has been introduced to the perfusion community, and we set about testing its oxygen transfer performance and then comparing it to two other models. This evaluation was based on the comparison between oxygen transfer slope, gas phase arterial oxygen gradients, degree of blood shunting, maximum oxygen transfer, and diffusing capacity calculated for each membrane. Sixty patients were randomized into three groups of oxygenators (Dideco 703 [D703], Dideco; D903; and Quadrox, Jostra Medizintechnik AG, Hirrlingen, Germany) including 40/20 M/F of 68.6 +/- 11.3 years old, with a body weight of 71.5 +/- 12.1 kg, a body surface area (BSA) of 1.84 +/- 0.3 m(2), and a theoretical blood flow rate (index 2.4 times BSA) of 4.4 +/- 0.7 L/min. The maximum oxygen transfer (VO(2)) values were 313 mL O(2)/min (D703), 579 mL O(2)/min (D903), and 400 mL O(2)/min (Quadrox), with the D903 being the most superior (P < 0.05). Oxygen (O(2)) gradients were 320 mm Hg (D703), 235 mm Hg (D903), and 247 mm Hg (Quadrox), meaning D903 and Quadrox are more efficient versus the D703 (P < 0.05). Shunt fraction (Qs/Qt) and diffusing capacity (DmO(2)) were comparable (P = ns). Diffusing capacity values indexed to BSA (DmO(2)/m(2)) were 0.15 mL O(2)/min/mm Hg/m(2) (D703), 0.2 mL O(2)/min/mm Hg/m(2) (D903), and 0.18 mL O(2)/min/mm Hg/m(2) (Quadrox) with D903 outperforming D703 (P < 0.0005). During hypothermia (32.0 +/- 0.3 degrees C), there was a lower absolute and relative VO(2 )for all three oxygenators (P = ns). The O(2) gradients, DmO(2) and DmO(2)/m(2), were significantly lower for all oxygenators (P < 0.01). Also, Qs/Qt significantly rose for all oxygenators (P < 0.01). The oxygen transfer curve is characteristic to each oxygenator type and represents a tool to quantify oxygenator performance. Using this parameter, we demonstrated significant differences among commercially available oxygenators. However, all three oxygenators are considered to meet the oxygen needs of the patients.

Local degradation of structural, mechanical, electrical and chemical properties of membrane electrode assembly in polymer electrolyte fuel cell

Polymer electrolyte fuel cell (PEMFC) is promising source of clean power in many applications ranging from portable electronics to automotive and land-based power generation. However, widespread commercialization of PEMFC is primarily challenged by degradation. The mechanisms of fuel cell degradation are not well understood. Even though the numbers of installed units around the world continue to increase and dominate the pre-markets, the present lifetime requirements for fuel cells cannot be guarantee, creating the need for a more comprehensive knowledge of material’s ageing mechanism. The objective of this project is to conduct experiments on membrane electrode assembly (MEA) components of PEMFC to study structural, mechanical, electrical and chemical changes during ageing and understanding failure/degradation mechanism. The first part of this project was devoted to surface roughness analysis on catalyst layer (CL) and gas diffusion layer (GDL) using surface mapping microscopy. This study was motivated by the need to have a quantitative understanding of the GDL and CL surface morphology at the submicron level to predict interfacial contact resistance. Nanoindentation studies using atomic force microscope (AFM) were introduced to investigate the effect of degradation on mechanical properties of CL. The elastic modulus was decreased by 45 % in end of life (EOL) CL as compare to beginning of life (BOL) CL. In another set of experiment, conductive AFM (cAFM) was used to probe the local electric current in CL. The conductivity drops by 62 % in EOL CL. The future task will include characterization of MEA degradation using Raman and Fourier transform infrared (FTIR) spectroscopy. Raman spectroscopy will help to detect degree of structural disorder in CL during degradation. FTIR will help to study the effect of CO in CL. XRD will be used to determine Pt particle size and its crystallinity. In-situ conductive AFM studies using electrochemical cell on CL to correlate its structure with oxygen reduction reaction (ORR) reactivity

Microfluidic hydrogen generator : featuring passive on-demand gas generation and self-circulated reactant for integration with micro fuel cell

A microfluidic hydrogen generator is presented in this work. Its fabrication, characterization, and integration with a micro proton exchange membrane (PEM) fuel cell are described. Hydrogen gas is generated by the hydrolysis of aqueous ammonia borane. Gas generation, as well as the circulation of ammonia borane from a rechargeable fuel reservoir, is performed without any power consumption. To achieve this, directional growth and selective venting of hydrogen gas is maintained in the microchannels, which results in the circulation of fresh reactant from the fuel reservoir. In addition to this self-circulation mechanism, the hydrogen generator has been demonstrated to self-regulate gas generation to meet demands of a connected micro fuel cell. All of this is done without parasitic power consumption from the fuel cell. Results show its feasibility in applications of high-impedance systems. Lastly, recommendations for improvements and suggestions for future work are described

Extracorporeal membrane oxygenation (ECMO): extended indications for artificial support of both heart and lungs

Extracorporeal membrane oxygenation (ECMO) was used to achieve temporary artificial support in cardiac and pulmonary function in 22 patients from 1987 to September 1990. Standard indications were postcardiotomy cardiogenic shock (n = 4), neonatal (n = 1) and adult respiratory distress syndrome (n = 4). ECMO was also used for extended indications, such as graft failure following heart (n = 11) or lung transplantation (n = 2). In six of these cases ECMO was instituted as a bridge device to subsequent retransplantation of either the heart (n = 4) or one lung (n = 2). One out of nine patients supported by ECMO for standard indications, and two out of 13 patients supported for extended indications are long-term survivors. This series illustrates the results with ECMO in emergency situations, in patients under immunosuppressive protocols, or in patients with advanced lung failure requiring almost complete artificial gas exchange. In such complex situations, ECMO does provide stabilization until additional therapeutic measures are in effect. ECMO cannot be recommended for postoperative cardiogenic shock but short-term ECMO support is an accepted method in most cases with graft failure or pulmonary failure or other origin.

Electrocatalytic hydrogenation of acetophenone using a Polymer Electrolyte Membrane Electrochemical Reactor

The use of a solid polymeric electrolyte, spe, is not commonly found in organic electrosynthesis despite its inherent advantages such as the possible elimination of the electrolyte entailing simpler purification processes, a smaller sized reactor and lower energetic costs. In order to test if it were possible to use a spe in industrial organic electrosynthesis, we studied the synthesis of 1-phenylethanol through the electrochemical hydrogenation of acetophenone using Pd/C 30 wt% with different loadings as cathode and a hydrogen gas diffusion anode. A Polymer Electrolyte Membrane Electrochemical Reactor, PEMER, with a fuel cell structure was chosen to carry out electrochemical reduction with a view to simplifying an industrial scale-up of the electrochemical process. We studied the influence of current density and cathode catalyst loading on this electroorganic synthesis. Selectivity for 1-phenylethanol was around 90% with only ethylbenzene and hydrogen detected as by-products.

Performance Assessment of a Polymer Electrolyte Membrane Electrochemical Reactor under Alkaline Conditions – A Case Study with the Electrooxidation of Alcohols

A novel polymer electrolyte membrane electrochemical reactor (PEMER) configuration has been employed for the direct electrooxidation of propargyl alcohol (PGA), a model primary alcohol, towards its carboxylic acid derivatives in alkaline medium. The PEMER configuration comprised of an anode and cathode based on nanoparticulate Ni and Pt electrocatalysts, respectively, supported on carbonaceous substrates. The electrooxidation of PGA was performed in 1.0 M NaOH, where a cathode based on a gas diffusion electrode was manufactured for the reduction of oxygen in alkaline conditions. The performance of a novel alkaline anion-exchange membrane based on Chitosan (CS) and Poly(vinyl) alcohol (PVA) in a 50:50 composition ratio doped with a 5 wt.% of poly (4-vinylpyridine) organic ionomer cross-linked, methyl chloride quaternary salt resin (4VP) was assessed as solid polymer electrolyte. The influence of 4VP anionic ionomer loading of 7, 12 and 20 wt.% incorporated into the electrocatalytic layers was examined by SEM and cyclic voltammetry (CV) upon the optimisation of the electroactive area, the mechanical stability and cohesion of the catalytic ink onto the carbonaceous substrate for both electrodes. The performance of the 4VP/CS:PVA membrane was compared with the commercial alkaline anion-exchange membrane FAA −a membrane generally used in direct alcohol alkaline fuel cells- in terms of polarisation plots in alkaline conditions. Furthermore, preparative electrolyses of the electrooxidation of PGA was performed under alkaline conditions of 1 M NaOH at constant current density of 20 mA cm−2 using a PEMER configuration to provide proof of the principle of the feasibility of the electrooxidation of other alcohols in alkaline media. PGA conversion to Z isomers of 3-(2-propynoxy)-2-propenoic acid (Z-PPA) was circa 0.77, with average current efficiency of 0.32. Alkaline stability of the membranes within the PEMER configuration was finally evaluated after the electrooxidation of PGA.