Mixed Matrix Membranes (MMMs) have received worldwide attention during the last decades. This is due to the fact that the resulting materials can combine the good processability and low cost of polymer membranes with the diverse functionality, high performance and thermal properties of the fillers. This work explores the fabrication and application of MMMs. We focused on the design and fabrication of nanofillers to impart target functionality to the membrane for water treatment, protective coating and gas separation. This thesis is divided into three sections according to the application including: I- Water Treatment: This part is divided into three chapters, two related to the membrane distillation (MD) and one related to the oil spill. Three different nanofillers have been used: Periodic mesoporous organosilica (PMO), graphene and carbon nanotube (CNT). Those nanofillers were homogeneously incorporated into polyetherimide (PEI) electrospun nanofiber membranes. The doped nanoparticle not only improved the mechanical properties and thermal stability of the pristine fiber but also enhanced the MD and oil spill performance due to the functionality of those nanofillers. II- Protective coating: This part includes two chapters describing the design and the fabrication of a smart antibacterial and anti-corrosion coating. In the first project, we fabricated colloidal lysozyme-templated gold nanoclusters gating antimicrobial-loaded silica nanoparticles (MSN-AuNCs@lys) as nano-fillers in poly(ethylene oxide)/poly(butylene terephthalate) polymer matrix. MSN-AuNCs@lys dispersed homogeneously within the polymer matrix with zero NPs leaching. The system was coated on a common radiographic dental imaging device that is prone to oral bacteria contamination. This coating can successfully sense and inhibit bacterial contamination via a controlled release mechanism that is only triggered by bacteria. In the second project, the coaxial electrospinning approach has been applied to fabricate smart core-shell nanofiber for controlled release of anti-corrosion material. Acetal-dextran was used as a pH controlled shell of the fibers and polyvinyl alcohol (PVA) as a hydrophilic core. Caffeine, as an anti-corrosion inhibitor was encapsulated in the fiber core to test its potential application as an anticorrosion coating. The almost negligible release was noticed at neutral pH. In acidic pH due to corrosion, the fibers quickly respond by releasing caffeine cargo. III- Gas separation: We describe the synthesis and application of novel ethylene-diamine-based PMO. The novel nanoparticles were homogeneously incorporated into polydimethylsiloxane to fabricate a MMMs thin layer on a porous polyacrylonitrile support. Our results prove that our PMOs can be used as nanofillers to enhance the CO2 selectivity of the PDMS polymer.

No description available.

This research aimed to develop new composite membranes using a polymer of intrinsic microporosity (PIM-1) and metal organic frameworks (MOFs) for use in gas separations. PIM-1 was successfully synthesised using the high temperature method (40 min, 160 oC) and the resulting polymer was cast into membranes. PIM-1 membranes were chemically modified by reacting hexamethylenediamine (HMDA) with the nitrile group of PIM-1 to form HMDA-modified PIM-1 membranes. Surfaces of PIM-1 membranes were also modified by basic hydrolysis to form amide-modified PIM-1 membranes. These polymer materials were characterized by different techniques (GPC, NMR, ATR-IR, TGA, Elemental analysis and nitrogen sorption analysis). In addition, eight MOF materials [MIL-101(Cr), ED-g-MIL-101(Cr), TEPA-g-MIL-101(Cr), MIL-101(Cr)-NH2, MIL-101(Al)-NH2, UiO-66(Zr), UiO-66-NH2 and UiO-66(COOH)2] were successfully synthesized. They were chosen due to having high surface areas and large porosity. These MOF compounds were characterized using PXRD, SEM, TGA, and low pressure N2.Successful PIM-1/MOF MMMs were fabricated utilising PIM-1 and the MOFs outlined above with various loadings. The highest MOF loading achieved was 28.6 wt. %, apart from MIL-101(Cr)-NH2, for which it was 23.1 wt. %, and MIL-101(Al)-NH2, for which it was 19.8 wt. %. The morphology of MMMs was characterized by scanning electron microscopy (SEM), proving the dispersion of MOF fillers. Novel PIM-1 supported MOF membranes were successfully prepared by depositing ZIF-8 and HKUST-1 layers on the surfaces of unmodified and modified PIM-1 membranes. These materials were characterized using PXRD, SEM, ATR-IR and SEM-EDX. Gas permeation properties of the MOF/PIM-1 MMMs and PIM-1 supported MOF membranes were determined using a time lag method. Most MMMs tested showed an increase in the permeability and stable selectivity as the MOF amount was increased. However, this was not true for MIL-101(Al)-NH2, where the permeability and selectivity decreased. In contrast, PIM-1 supported ZIF-8 and HKUST-1 membranes caused a sharp decrease in the permeability and increase in the selectivity.

Mixed matrix membranes (MMMs) have gained importance because they combine the desirable properties of the polymers and the organic/inorganic filler materials and they may have a very big potential. In this study polyethersulfone (PES) was used as polymeric material, and Zeolitic Imidazolate Framework-8 (ZIF-8) was used as porous filler material, and 2-hydroxy 5-methyl aniline(HMA), was used as a third component in membrane formulation. In this study, ZIF-8 crystals were synthesized with varying particle sizes, and a novel recycling methodology was developed to improve the efficiency of ZIF-8 production. ZIF-8 nano-crystals were synthesized by a 1-hour stirring method at room temperature and characterized by X-ray diffractometer, scanning electron microscopy (SEM), transmission electron microscopy (TEM), dynamic light scattering (DLS) and thermal gravimetric analysis (TGA). In order to investigate the effect of ZIF-8 loading on the membrane performance, different types of membranes were prepared with varying amounts of ZIF-8 between 10-60% (w/w). Moreover, ternary mixed matrix membranes were synthesized consisting of different amounts of ZIF-8 between 10-30% (w/w) and HMA 1-10% (w/w). Gas transport properties of the membranes were investigated by single gas permeation experiments of H2, CO2 and CH4 at 3 bar feed pressure. In order to investigate the effect of feed pressure on the gas transport properties of the membranes, single gas experiments were conducted on 3, 6, 8, 10 and 12 bar feed pressures. Moreover, binary gas permeation experiments of CO2/CH4 pair were conducted through selected membranes at 3 bar and 12 bar feed pressures. In addition to gas permeation experiments, the morphology and thermal characteristics of the membranes were characterized by SEM, TGA and differential scanning calorimetry (DSC) analysis. The incorporation of ZIF-8 crystals into continuous PES matrix resulted in high performance gas separation membranes. The permeabilities of all studied gases increased with ZIF-8 loading while the ideal selectivities showed a slight decrease compared to neat PES membrane. Highly reproducible and repeatable results were obtained up to 30 % w/w ZIF-8 loading, while membrane formulation reproducibility was decreased for higher ZIF-8 contents (&gt / 30 w/w %). Addition of HMA improved the gas separation performances of the binary membranes significantly by decreasing permeabilities and increasing ideal selectivities. PES/ZIF-8(%20)/HMA(%7) membrane has the best separation performance for all gases among the ternary membranes. When 7 w/w % HMA was added to PES/ZIF-8(%20) membrane, H2 permeability decreased from 26.3 to 13.7 barrer, while H2/CH4 ideal selectivity increased from 61.8 to 103.7. Increasing feed pressures appreciably increased the separation performances of all membranes. While the H2 permeability is pressure independent, the CO2 and CH4 permeabilities were reduced with increasing feed pressures and the highest selectivity improvement was observed in H2/CH4 pair for all membrane compositions. For instance, when the feed pressure was increased from 3 bar to 12 bar, the percentage improvements in ideal selectivities through PES/ZIF-8(%10)/HMA(%4) membrane were calculated as 26, 69, 113 % for the H2/CO2, CO2/CH4 and H2/CH4 gas pairs / respectively. This results show that working at higher feed pressures will be more advantageous for separation of the studied gas pairs. The ideal selectivities and the separation factors were equal to each other for all membrane compositions both for 3 and 12 bar operating pressures.

The goal of this project was to understand and model the performance of hybrid inorganic-organic membranes under realistic operating conditions for hydrocarbon gas/vapor separation, using butane isomers as the model vapors and a hybrid membrane of 6FDA-DAM-5A as an advanced separation system. To achieve the set goal, three objectives were laid out. The first objective was to determine the factors affecting separation performance in dense neat polymer. One main concern was plasticization. High temperature annealing has been reported as an effect means of suppressing plasticization. A study on the effect of annealing temperature was performed by analyzing data acquired via sorption and permeation measurements. Based on the findings from this study, a suitable annealing temperature was determined. Another factor studied was the effect of operating temperature. In deciding a suitable operating temperature, factors such as its possible effect on plasticization as well as reducing heating/cooling cost in industrial application were considered. Based on the knowledge that industrial applications of this membrane would involve mixture separation, the second objective was to understand and model the complexity of a mixed gas system. This was investigated via permeation measurements using three feed compositions. An interesting transport behavior was observed in the mixed gas system, which to the best of our knowledge, has not been observed in other mixed gas systems involving smaller penetrants. This mixed gas transport behavior presented a challenge in predictability using well-established transport models. Two hypotheses were made to explain the observed transport behavior, which led to the development of a new model termed the HHF model and the introduction of a fitting parameter termed the CAUFFV fit. Both the HHF model and CAUFFV fit showed better agreement with experimental data than the well-established mixed gas transport model. The final objective was to explore the use of mixed matrix membranes as a means of improving the separation performance of this system. A major challenge with the fabrication of good mixed matrix membranes was the adhesion of the zeolite particle with the polymer. This was addressed via sieve surface modification through a Grignard treatment process. Although a Grignard treatment procedure existed, there was a challenge of reproducibility of the treatment. This challenge was addressed by exploring the relationship between the sieves and the solvent used in the treatment, and taking advantage of this relationship in the Grignard treatment process. This study helped identify a suitable solvent, which allowed for successful and reproducible treatment of commercial LTA sieves; however, treatment of lab-made sieves continues to prove challenging. Based on improved understanding of the Grignard treatment reaction mechanism, modifications were made to the existing Grignard treatment procedure, resulting in the introduction of a "simplified" Grignard treatment procedure. The new procedure requires less control over the reaction process, thus making it more attractive for industrial application. Permeation measurements were made using mixed matrix membranes in both single and mixed gas systems. Selectivity enhancements were observed under both single and mixed gas systems using sieve loadings of 25 and 30wt%. The Maxwell model was used to make predictions of mixed matrix membrane performance. Although the experimental results were not in exact agreement with Maxwell predictions, the observed selectivity enhancement was very encouraging and shows potential for future application. Recommendations were made for future study of this system.

Polymeric membranes exhibit a trade-off between permeability and selectivity in gas separations which limits their viability as an economically feasible post-combustion carbon capture technology. One approach to improve the separation properties of polymeric membranes is the inclusion of particulate materials into the polymer matrix to create what are known as mixed matrix membranes (MMMs). By combining the polymer and particulate phases, beneficial properties of both can be seen in the resulting composite material. One of the most notable challenges in producing mixed matrix membranes is in the formation of performance-hindering defects at the polymer-filler interface. Non-selective voids or polymer chain rigidification are but two non-desirable effects which can be observed. The material selection and synthesis route are key to minimising these defects. Thin membranes are also highly desirable to achieve greater gas fluxes and improved economical separation processes. Hence smaller nano-sized particles are of particular interest to minimise the disruption to the polymer matrix. This is a challenge due to the tendency of some small particles to form agglomerations. This work involved introducing novel nanoscale filler particles into PEBAX MH1657, a commercially available block-copolymer consisting of poly(ethylene oxide) and nylon 6 chains. Poly(ether-b-amide) materials possess an inherently high selectivity for the CO2/N2 separation due to polar groups in the PEO chain but suffer from low permeabilities. Mixed matrix membranes were fabricated with PEBAX MH1657 primarily using two filler particles, nanoscale ZIF-8 and novel nanoscale MCM-41 hollow spheres. This work primarily investigated the effects of the filler loading on both the morphology and gas transport properties of the composite materials. The internal structure of the membranes was examined using scanning electron microscopy (SEM), and the gas transport properties determined using a bespoke time-lag gas permeation apparatus. ZIF-8 is a zeolitic imidazolate framework which possesses small pore windows that may favour CO2 transport over that of N2. ZIF-8-PEBAX membranes were successfully synthesised up to 7wt.%. It was found that for filler loadings below 5wt.%, the ZIF-8 was well dispersed within the polymer phase. At these loadings modest increases in the CO2 permeability coeffcient of 0-20% compared to neat PEBAX were observed. Above this 5wt.% loading large increases in both CO2, N2 and He permeability coeffcients coincided with the presence of large micron size clusters formed of hundreds of filler ZIF-8 particles. The increases in permeability were attributed to voids observed within the clusters. MCM-41 is a metal organic framework that has seen notable interest in the field of carbon capture, due to its tunable pore size and ease of functionalisation. Two types of novel MCM-41 hollow sphere (MCM-41-HS) of varying pore size were incorporated into PEBAX and successfully used to fabricate MMMs up to 10wt.%. SEM showed the MCM-41 generally interacted well with the polymer with no signs of voids and was generally well dispersed. However, some samples of intermediate loading in both cases showed highly asymmetric distribution of nanoparticles and high particle density regions near one external face of the membrane which also showed the highest CO2 permeability coeffcients. It is suspected that these high permeabilities are due to the close proximity of nanoparticles permitting these regions to act in a similar way to percolating networks. It was determined that there was no observable effect of the varying pore size which was expected given the transport in the pores should be governed by Knudsen diffusion.

Η παρούσα διδακτορική διατριβή αποτελείται από δύο ξεχωριστές ενότητες οι οποίες έχουν σαν στόχο τη μελέτη τροποποιημένων πολυμερικών μεμβρανών για χρήση σε κυψελίδες καυσίμου αγωγής πρωτονίων και σε εφαρμογές διαχωρισμού αερίων. Στην πρώτη ενότητα έγινε εκτίμηση του μοριακού προσανατολισμού μονοαξονικά εφελκυσμένων πολυμερικών μεμβρανών Nafion-115 με τη βοήθεια πολωμένων φασμάτων UV-Raman. Πειράματα δυναμικής μηχανικής ανάλυσης επαλήθευσαν τις προσδοκίες για βελτίωση των μηχανικών ιδιοτήτων του πολυμερικού ηλεκτρολύτη κατά μήκος της διεύθυνσης εφελκυσμού. Η θερμική ανάλυση των δειγμάτων με τις τεχνικές της διαφορικής θερμιδομετρίας σάρωσης και της θερμοσταθμικής ανάλυσης δεν έδειξε κάποια ιδιαίτερη διαφοροποίηση μεταξύ εφελκυσμένων και μη δοκιμίων Nafion-115, πέραν της βελτίωσης της ικανότητας των τανυσμένων μεμβρανών να συγκρατούν το όποιο νερό υπάρχει στο ιονομερές. Μικρή ήταν η αύξηση της ιοντικής αγωγιμότητας που παρατηρήθηκε στα τανυσμένα δείγματα κατά μήκος της διεύθυνσης εφελκυσμού. Η προσπάθεια τροποποίησης του Nafion® με διαξονικό εφελκυσμό είχε σαν αποτέλεσμα τη λήψη λεπτών πολυμερικών ηλεκτρολυτικών μεμβρανών με αποτελεσματικότερες ιδιότητες στην τάση διέλευσης της μεθανόλης, σε σχέση με τις μη τροποποιημένες μεμβράνες. Επιπρόσθετα, με τον ελεγχόμενο διαξονικό και σταθερού πλάτους μονοαξονικό εφελκυσμό κατέστη δυνατό να επιτευχθεί η εξισορρόπηση των ποσοστών διαστολής κατά το μήκος και πλάτος της επιφάνειας του Nafion, μετά τον εμποτισμό του με νερό. Όσον αφορά στην τροποποίηση του Nafion με εναπόθεση στοιβάδας αγώγιμου πολυμερούς πολυανιλίνης (PAni) ή πολυπυρρόλης (PPy) με ενσωματωμένα αντισταθμιστικά ιόντα SO42- ή Nafion-, η φασματοσκοπική μελέτη, μέσω ATR-FTIR, σε συνδυασμό με τις μικροφωτογραφίες SEM που ελήφθησαν, οδήγησαν στα εξής συμπεράσματα: Για τις σύνθετες μεμβράνες Nafion/PAni που παρασκευάστηκαν με την τεχνική της διάχυσης, από τη μία ελήφθησαν δείγματα με ικανοποιητική συνάφεια μεταξύ του κυρίως όγκου της πολυμερικής μεμβράνης Nafion και της PAni, από την άλλη όμως, υπάρχει και κάποιο ποσοστό μονομερούς ανιλίνης (Ani) που εγκλωβίζεται στο εσωτερικό του Nafion, και μάλιστα σε σημαντικό βαθμό, που εξαρτάται από το χρόνο σύνθεσης. Αντίθετα, οι αντίστοιχες μελέτες στις μεμβράνες Nafion/PPy δε φανερώνουν την ύπαρξη διείσδυσης της PPy ή του μονομερούς στην κύρια μάζα του Nafion, ή τουλάχιστον όχι σε τέτοιο βαθμό που να μπορεί να ανιχνευθεί μέσω της τεχνικής που χρησιμοποιήθηκε. Ιδιαίτερο είναι το ενδιαφέρον που προκύπτει από τις φασματοσκοπικές μετρήσεις στην πλευρά του σύνθετου πολυμερούς όπου εναποτίθετο το πολυμερισμένο αγώγιμο υλικό, καθώς με το χρόνο σύνθεσης παρατηρούνται μετατοπίσεις κορυφών του Nafion προς χαμηλότερες συχνότητες, υποδεικνύοντας ενδεχόμενη αλληλεπίδραση με το αγώγιμο πολυμερές. Στη δεύτερη ενότητα μελετήθηκαν οι σύνθετες (ή “mixed matrix”) πολυμερικές μεμβράνες πολυσουλφόνης (PSF) με ενσωματωμένες φυλλώδεις αργυλοφωσφορικές νανονιφάδες τύπου AlPO. Αρχικά πραγματοποιήθηκε η σύνθεση των νανονιφάδων AlPO. Με στόχο τη βελτίωση της συμβατότητάς τους με την πολυμερική μήτρα έγινε παρεμβόλιση με κατάλληλη επιφανειοδραστική ουσία και χαρακτηρισμός με XRD που έδειξε τη διεύρυνση της απόστασης μεταξύ των διαδοχικών στρωμάτων του κρυστάλλου από 9Å σε 33Å περίπου. Στη συνέχεια παρασκευάσθηκαν οι σύνθετες μεμβράνες με διαφορετικές συγκεντρώσεις της ανόργανης φάσης, με τη μέθοδο του film casting. Με βάση τις εικόνες SEM οι νανονιφάδες φαίνεται να έχουν ικανοποιητική διασπορά στη μάζα της πολυσουλφόνης, ενώ τα φάσματα XRD δείχνουν πως η ενσωμάτωση των παρεμβολισμένων νανονιφάδων στην πολυμερική μήτρα δεν επέφερε κάποια σημαντική αλλαγή στη δομή τους. Οι νανονιφάδες, ακόμα και σε μικρές συγκεντρώσεις, βελτιώνουν σε σημαντικό βαθμό τη διαχωριστική ικανότητα των αμιγώς πολυμερικών μεμβρανών για τα ζεύγη αερίων H2/N2 και Η2/CH4 όχι όμως και για το ζεύγος Η2/CO2. Αντίθετα, η αύξηση του ποσοστού των νανονιφάδων AlPO οδηγεί σε μείωση της διαπερατότητας του H2. Oι σύνθετες μεμβράνες PSF/AlPO δείχνουν μια μικρή βελτίωση του μέτρου ελαστικότητας αποθηκευόμενης ενέργειας σε σχέση με τις πολυμερικές μεμβράνες PSF, εμφανίζουν επίσης ελαφρώς μειωμένη θερμοκρασία υαλώδους μετάβασης και, κατά τη θέρμανσή τους, ακολουθούν τρία στάδια απώλειας μάζας λόγω αποσύνθεσης της επιφανειοδραστικής ουσίας σε συνδυασμό με απώλεια φυσικά και χημικά ροφημένου νερού. / The present thesis consists of two separate parts which focus on the study of modified polymer membranes for use in fuel cells applications and gas separation processes. In the first part, the molecular orientation of uniaxially drawn Nafion-115 membranes was estimated utilizing polarized UV-Raman spectra. Dynamic mechanical analysis revealed the enhanced strength of the drawn samples along the draw axis. Thermal analysis, carried out via differential scanning calorimetry, and thermogravimetric analysis did not show any difference between drawn and undrawn specimens, except from a slight enhanced capability of the drawn membranes to water content retain. Proton conductivity is slightly enhanced along the stretching direction, as well. The attempts for biaxial stretching of Nafion® had as a result the production of very thin polymer electrolyte membranes with lower permeability to methanol than the commercial one. In addition, with biaxial and constant width uniaxial stretching, the swelling of Nafion along and across its surface can be controlled. The process of modifying Nafion by embedding conducting polymer layers of polypyrrole or polyaniline with SO42- or Nafion- incorporated into the film as counter-ions is studied via ATR-FTIR spectroscopy in combination with SEM microphotographs. Nafion/PAni composite membranes synthesized by the diffusion method showed very good adherence between Nafion and PAni layers but it seems that there is some Ani monomer still remaining inside the bulk structure of Nafion, depending on the time of synthesis. In contrast, the corresponding studies on Nafion/PPy membranes show that there is no penetration of PPy or Py inside Nafion, at least not to the extent that it could be traced using ATR-FTIR spectroscopy. The spectroscopic measurements from the conducting polymer side show red-shifts of absorption bands of Nafion revealing possible specific interactions with the conducting polymer. In the second part, composite (or mixed matrix) polymeric membranes with dispersed aluminophosphate nanoflakes were studied. At the beginning AlPO nanoflakes were synthesized. To enhance the compatibility with the polymer matrix conventional AlPO nanoflakes were intercalated using suitable surfactant. XRD characterization showed a further individual layers` separation since the distance between them is increased from 9Å to 33Å. Subsequently, mixed matrix membranes with different nanoflakes loading were synthesized, using film casting method. Based on SEM images nanoflakes seem to be well dispersed in the mass of polysulfone, while XRD graphs implied that the incorporation of intercalated nanoflakes into the polymer matrix did not affect their structural characteristics. Nanoflakes incorporation, even at very low concentrations, improves the H2/N2 and H2/CH4 selectivity and deteriorates the H2/CO2 selectivity compared with the pure polymer. On the other hand, the higher the percentage of the AlPO flakes, the more pronounced the decrease in hydrogen permeability. PSF/AlPO membranes exhibit improved storage modulus, appear to have slightly lower glass transition temperature compared with PSF membranes and during their heating, follow a three steps mass loss due to the surfactant decomposition and the loss of physically and chemically absorbed water.

[ES] La presente tesis doctoral se centra en el desarrollo de nuevas membranas de separación de gases, así como su empleo in-situ en reactores catalíticos de membrana para la intensificación de procesos. Para este propósito, se han sintetizado varios materiales, como polímeros para la fabricación de membranas, catalizadores tanto para la metanación del CO2 como para la reacción de síntesis de Fischer-Tropsch, y diversas partículas inorgánicas nanométricas para su uso en membranas de matriz mixta. En lo referente a la fabricación de las membranas, la tesis aborda principalmente dos tipos: orgánicas e inorgánicas. Con respecto a las membranas orgánicas, se han considerado diferentes materiales poliméricos, tanto para la capa selectiva de la membrana, así como soporte de la misma. Se ha trabajado con poliimidas, puesto que son materiales con temperaturas de transición vítrea muy alta, para su posterior uso en reacciones industriales que tienen lugar entre 250-300 ºC. Para conseguir membranas muy permeables, manteniendo una buena selectividad, es necesario obtener capas selectivas de menos de una micra. Usando como material de soporte otro tipo de polímero, no es necesario estudiar la compatibilidad entre ellos, siendo menos compleja la obtención de capas finas. En cambio, si el soporte es de tipo inorgánico, un exhaustivo estudio de la relación entre la concentración y la viscosidad de la solución polimérica es altamente necesario. Diversas partículas inorgánicas nanométricas se estudiaron para favorecer la permeación de agua a través de los materiales poliméricos. En segundo lugar, en cuanto a membranas inorgánicas, se realizó la funcionalización de una membrana de paladio para favorecer la permeación de hidrógeno y evitar así la contaminación por monóxido de carbono. El motivo por el cual se dopó con otro metal la capa selectiva de la membrana metálica fue para poder emplearla en un reactor de Fischer-Tropsch. Con relación al diseño y fabricación de los reactores, durante esta tesis, se desarrolló el prototipo de un microreactor para la metanación de CO2, donde una membrana polimérica de capa fina selectiva al agua se integró para evitar la desactivación del catalizador, y a su vez desplazar el equilibrio y aumentar la conversión de CO2. Por otro lado, se rediseñó un reactor de Fischer-Tropsch para poder introducir una membrana metálica selectiva a hidrogeno y poder inyectarlo de manera controlada. De esta manera, y siguiendo estudios previos, el objetivo fue mejorar la selectividad a los productos deseados mediante el hidrocraqueo y la hidroisomerización de olefinas y parafinas con la ayuda de la alta presión parcial de hidrógeno. / [CAT] La present tesi doctoral es centra en el desenvolupament de noves membranes de separació de gasos, així com el seu ús in-situ en reactors catalítics de membrana per a la intensificació de processos. Per a aquest propòsit, s'han sintetitzat diversos materials, com a polímers per a la fabricació de membranes, catalitzadors tant per a la metanació del CO2 com per a la reacció de síntesi de Fischer-Tropsch, i diverses partícules inorgàniques nanomètriques per al seu ús en membranes de matriu mixta. Referent a la fabricació de les membranes, la tesi aborda principalment dos tipus: orgàniques i inorgàniques. Respecte a les membranes orgàniques, diferents materials polimèrics s'ha considerat com a candidats prometedors, tant per a la capa selectiva de la membrana, així com com a suport d'aquesta. S'ha treballat amb poliimides, ja que són materials amb temperatures de transició vítria molt alta, per al seu posterior ús en reaccions industrials que tenen lloc entre 250-300 °C. Per a aconseguir membranes molt permeables, mantenint una bona selectivitat, és necessari obtindre capes selectives de menys d'una micra. Emprant com a material de suport altre tipus de polímer, no és necessari estudiar la compatibilitat entre ells, sent menys complexa l'obtenció de capes fines. En canvi, si el suport és de tipus inorgànic, un exhaustiu estudi de la relació entre la concentració i la viscositat de la solució polimèrica és altament necessari. Diverses partícules inorgàniques nanomètriques es van estudiar per a afavorir la permeació d'aigua a través dels materials polimèrics. En segon lloc, quant a membranes inorgàniques, es va realitzar la funcionalització d'una membrana de pal¿ladi per a afavorir la permeació d'hidrogen i evitar la contaminació per monòxid de carboni. El motiu pel qual es va dopar amb un altre metall la capa selectiva de la membrana metàl¿lica va ser per a poder emprar-la en un reactor de Fischer-Tropsch. En relació amb el disseny i fabricació dels reactors, durant aquesta tesi, es va desenvolupar el prototip d'un microreactor per a la metanació de CO2, on una membrana polimèrica de capa fina selectiva a l'aigua es va integrar per a així evitar la desactivació del catalitzador i al seu torn desplaçar l'equilibri i augmentar la conversió de CO2. D'altra banda, un reactor de Fischer-Tropsch va ser redissenyat per a poder introduir una membrana metàl¿lica selectiva a l'hidrogen i poder injectar-lo de manera controlada. D'aquesta manera, i seguint estudis previs, el objectiu va ser millorar la selectivitat als productes desitjats mitjançant el hidrocraqueix i la hidroisomerització d'olefines i parafines amb l'ajuda de l'alta pressió parcial d'hidrogen. / [EN] The present thesis is focused on the development of new gas-separation membranes, as well as their in-situ integration on catalytic membrane reactors for process intensification. For this purpose, several materials have been synthesized such as polymers for membrane manufacture, catalysts for CO2 methanation and Fischer-Tropsch synthesis reaction, and inorganic materials in form of nanometer-sized particles for their use in mixed matrix membranes. Regarding membranes manufacture, this thesis deals mainly with two types: organic and inorganic. With regards to the organic membranes, different polymeric materials have been considered as promising candidates, both for the selective layer of the membrane, as well as a support thereof. Polyimides have been selected since they are materials with very high glass transition temperatures, in order to be used in industrial reactions which take place at temperatures around 250-300 ºC. To obtain highly permeable membranes, while maintaining a good selectivity, it is necessary to develop selective layers of less than one micron. Using another type of polymer as support material, it is not necessary to study the compatibility between membrane and support. On the other hand, if the support is inorganic, an exhaustive study of the relation between the concentration and the viscosity of the polymer solution is highly necessary. In addition, various inorganic particles were studied to favor the permeation of water through polymeric materials. Secondly, as regards to inorganic membranes, the functionalization of a palladium membrane to favor the permeation of hydrogen and avoid carbon monoxide contamination was carried out. The membrane selective layer was doped with another metal in order to be used in a Fischer-Tropsch reactor. Regarding the design and manufacture of the reactors used during this thesis, a prototype of a microreactor for CO2 methanation was carried out, where a thin-film polymer membrane selective to water was integrated to avoid the deactivation of the catalyst and to displace the equilibrium and increase the CO2 conversion. On the other hand, a Fischer-Tropsch reactor was redesigned to introduce a hydrogen-selective metal membrane and to be able to inject it in a controlled manner. In this way, and following previous studies, the aim is to enhance the selectivity to the target products by hydrocracking and hydroisomerization the olefins and paraffins assisted by the presence of an elevated partial pressure of hydrogen. / I would like to acknowledge the Spanish Government, for funding my research with the Severo Ochoa scholarship. / Escorihuela Roca, S. (2019). Novel gas-separation membranes for intensified catalytic reactors [Tesis doctoral no publicada]. Universitat Politècnica de València. https://doi.org/10.4995/Thesis/10251/121139 / TESIS