931 resultados para membrane separation factor


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We have studied the synergetic effect of confinement (carbon nanopore size) and surface chemistry (the number of carbonyl groups) on CO2 capture from its mixtures with CH4 at typical operating conditions for industrial adsorptive separation (298 K and compressed CO2CH4 mixtures). Although both confinement and surface oxidation have an impact on the efficiency of CO2/CH4 adsorptive separation at thermodynamics equilibrium, we show that surface functionalization is the most important factor in designing an efficient adsorbent for CO2 capture. Systematic Monte Carlo simulations revealed that adsorption of CH4 either pure or mixed with CO2 on oxidized nanoporous carbons is only slightly increased by the presence of functional groups (surface dipoles). In contrast, adsorption of CO2 is very sensitive to the number of carbonyl groups, which can be examined by a strong electric quadrupolar moment of CO2. Interestingly, the adsorbed amount of CH4 is strongly affected by the presence of the co-adsorbed CO2. In contrast, the CO2 uptake does not depend on the molar ratio of CH4 in the bulk mixture. The optimal carbonaceous porous adsorbent used for CO2 capture near ambient conditions should consist of narrow carbon nanopores with oxidized pore walls. Furthermore, the equilibrium separation factor was the greatest for CO2/CH4 mixtures with a low CO2 concentration. The maximum equilibrium separation factor of CO2 over CH4 of ∼18–20 is theoretically predicted for strongly oxidized nanoporous carbons. Our findings call for a review of the standard uncharged model of carbonaceous materials used for the modeling of the adsorption separation processes of gas mixtures containing CO2 (and other molecules with strong electric quadrupolar moment or dipole moment).

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Bis-triazinylphenanthroline ligands (BTPhens), which contain additional alkyl (n-butyl and sec-butyl) groups attached to the triazine rings, have been synthesized, and the effects of this alkyl substitution on their extraction properties with Ln(III) and An(III) cations in simulated nuclear waste solutions have been studied. The speciation of n-butyl-substituted ligand (C4- BTPhen) with some trivalent lanthanide nitrates was elucidated by 1 H-NMR spectroscopic titrations. These experiments have shown that the dominant species in solution were the 1:2 complexes [Ln(III)(BTPhen)2], even at higher Ln(III) concentrations, and the relative stability of 2:1 to 1:1 BTPhen-Ln(III) complexes varied with different lanthanides. As expected, sec-butylsubstituted ligand (sec-C4 BTPhen) showed higher solubility than C4-BTPhen in certain diluents. A greater separation factor (SFAm/Eu = ca. 210) was observed for sec-C4-BTPhen compared to C4-BTPhen (SFAm/Eu = ca. 125) in 1-octanol at 4 M HNO3 solutions. The greater separation factor may be due to the higher solubility of the 2:1 complex for sec-C4-BTPhen at the interface than the 1:1 complex of C4-BTPhen.

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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

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Este estudo avalia a eficiência, viabilidade e espontaneidade de processos de adsorção do íon nitrato em caulinita sem tratamento e modificada com uréia, empregando como material de partida o rejeito de processamento de caulim do rio Jari. Os materiais foram caracterizados por difração de raios X, fluorescência de raios X e espectroscopia IV (DRX, FRX e FTIR). As medidas de pH de equilíbrio foram efetuadas por potenciometria e as concentrações de equilíbrio (Ce) de nitrato medidas por cromatografia iônica. Quantidades adsorvidas no equilíbrio (qe), constantes de distribuição (Kd=qe/Ce), fator de separação (RL) e variação de energia livre de Gibbs (ΔGº), foram calculados com base nos dados experimentais de adsorção. Os resultados de DRX e FTIR confirmaram a formação do complexo caulinita-uréia a partir do tratamento efetuado no rejeito de caulim. Os seguintes dados foram obtidos nos processos de adsorção de nitrato, no rejeito de caulim natural e tratado com uréia: qMax= 18,17 e 14,1 mmol kg-1; Kd=0,7-2,2 e 0,45-1,5 L Kg-1; RL= 0,35-0,85 e 0,25-0,80; ΔGº= -9,3 a -5,8 e -9,1 a -5,4 kJ mol-1, respectivamente. Os valores de Kd, ΔGº e RL são típicos de processos de adsorção física (fisissorção), viáveis e espontâneos e os de qMax indicam que a retenção de nitrato em rejeito de caulim natural é mais eficiente do que em rejeito modificado com uréia.

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The research of new advanced processes for syngas production is a part of a European project for the production of a new Gas to Liquid Process (NextGTL). The crucial points in the production of GTL process are the energy required for the air separation used in autothermal reforming or the heat required for steam reforming and the efficiency in carbon utilization. Therefore a new multistep oxy-reforming process scheme was developed at lower temperature with intermediate H2 membrane separation to improve the crucial parameter. The process is characterized by a S/C of 0.7 and O2/C of 0.21 having a smoothed temperature profile in which kinetic regime is easily obtained. Active catalysts for low temperature oxy-reforming process have been studied working at low pressure to discriminate among the catalyst and at high pressure to prove it on industrial condition. It allows the selection of the Rh as active phase among single and bimetallic VIII group metal. The study of the matrix composition and thermal treatment has been carried out on Rh-Mg/Al hydrotalcite selected as reference catalyst. The research to optimize the catalyst lead to enhanced performances through the identification of a limitation of the Rh reduction from the oxides matrix as key point to increase the Rh performances. The Rh loading have been studied to allow the catalyst scale up for pilot process in Chieti in a shape of Rh-HT on honeycomb ceramic material. The developed catalyst has enhanced methane conversion in a inch diameter monolith reactor if compared with the semi-industrial catalyst chosen in the project as the best reference.

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In dieser Arbeit wird eine Einteilung der degenerativen strukturellen Veränderungen der Synovialmembran vorgestellt. Anhand der Kriterien Fibrosierung des Stromas, Rückgang des Gefäßnetzes, Auftreten von Hyalinose und chondroider Metaplasie mit und ohne Nachweis von CPPD Kristallen wurden Präparate der Synovialmembran von 59 Patienten mit Nachweis degenerativer strukturellen Veränderungen in 4 Stadien eingeteilt. rnHyalinose (Stadium 3) konnte in den untersuchten Schnitten nur relativ selten beobachtet werden, so dass am ehesten von einem Vorstadium zur chondroiden Metaplasie auszugehen ist. rnDie Verteilung der Erkrankungsdauer und des Alters in den verschiedenen Stadien lassen darauf schließen, dass höhere Stadien mit höherem Alter und längerer Erkrankungsdauer korrelieren. rnAus der vorhandenen Literatur ergeben sich Hinweise, welche Faktoren zu der Entstehung der strukturellen Veränderungen beitragen können: rnAus dem Netzwerk der Zytokine scheinen TGF-beta und die BMP’s an der Zunahme der Fibrose und an der Entstehung chondroider Metaplasie beteiligt zu sein. Makrophagen scheinen dabei eine wichtige Rolle zu spielen. Dies weist darauf hin, dass entzündliche und strukturelle Veränderungen miteinander vernetzt sind. rnBei der Entstehung der chondroiden Metaplasie kommen zusätzlich mechanische Einflüsse in Form von zyklischen Kompressionen als Einflussfaktor in Frage. rnDie Regulierung der Angiogenese ist noch zu wenig verstanden, um den Gefäßrückgang bei fortgeschrittenen strukturellen Veränderungen zu erklären. Erklärungsansätze sind zum einen zunehmende mechanische Schädigung bei zunehmender Inkongruenz der Gelenkflächen. Zum anderen könnte eine beginnende chondroide Metaplasie mit Expression von Chondromodulin I eine entscheidende Rolle spielen. rnInsgesamt muss man davon ausgehen, dass die zunehmenden strukturellen Veränderungen die Ernährung des Knorpels erschweren. Dabei ist an erster Stelle der Rückgang des Gefäßnetzes zu nennen. Dies erschwert nicht nur die Versorgung mit Nährstoffen, sondern auch den Abtransport von Stoffwechselprodukten. Ab einem gewissen Punkt ist aber auch davon auszugehen, dass die Funktion der Deckzellschicht beeinträchtigt wird. Wenn die Konzentration der Hyaluronsäure in der Synovia dadurch sinkt, kann dies durch eine vermehrte Permeabilität der Synovialmembran zum verstärkten Ausstrom von Wasser aus der Gelenkhöhle führen. Durch ein Ödem des umliegenden Gewebes kann dadurch der Blutfluss im Bereich des Gelenks zusätzlich vermindert werden. rnAuch die zunehmende Fibrosierung der Synovialmembran kann einen Einfluss auf die Permeabilität der Synovialmembran haben. Ob und in welchen Stadien der Veränderungen das einen relevanten Einfluss für die Ernährung der Chondrozyten hat, ist noch unklar.rn

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The present study is focused on the development of new VIII group metal on CeO2 – ZrO2 (CZO) catalyst to be used in reforming reaction for syngas production. The catalyst are tested in the oxyreforming process, extensively studied by Barbera [44] in a new multistep process configuration, with intermediate H2 membrane separation, that can be carried out at lower temperature (750°C) with respect the reforming processes (900 – 1000°C). In spite of the milder temperatures, the oxy-reforming conditions (S/C = 0.7; O2/C = 0.21) remain critical regarding the deactivation problems mainly deriving from thermal sintering and carbon formation phenomena. The combination of the high thermal stability characterizing the ZrO2, with the CeO2 redox properties, allows the formation of stable mixed oxide system with high oxygen mobility. This feature can be exploited in order to contrast the carbon deposition on the active metal surface through the oxidation of the carbon by means of the mobile oxygen atoms available at the surface of the CZO support. Ce0.5Zr0.5O2 is the phase claimed to have the highest oxygen mobility but its formation is difficult through classical synthesis (co-precipitation), hence a water-in-oil microemulsion method is, widely studied and characterized. Two methods (IWI and bulk) for the insertion of the active metal (Rh, Ru, Ni) are followed and their effects, mainly related to the metal stability and dispersion on the support, are discussed, correlating the characterization with the catalytic activity. Different parameters (calcination and reduction temperatures) are tuned to obtain the best catalytic system both in terms of activity and stability. Interesting results are obtained with impregnated and bulk catalysts, the latter representing a new class of catalysts. The best catalysts are also tested in a low temperature (350 – 500°C) steam reforming process and preliminary tests with H2 membrane separation have been also carried out.

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L’accoppiamento di diverse operazioni unitarie può in certi casi portare ad una cosiddetta “intensificazione di processo”, cioè ad un aumento sostanziale delle rese, dell’efficienza e della sostenibilità. Nel presente lavoro sono state pertanto analizzate le potenzialità di accoppiamento della fotocatalisi, il più studiato tra i “processi di ossidazione avanzata”, sia con alcuni processi a membrana per la sintesi verde di aromi sia con l’ozonizzazione per la depurazione di acque. È stato dimostrato che in entrambi i casi l’ottenimento di una significativa intensificazione di processo dipende in gran parte dai parametri operativi, in particolare dal rapporto, delta, tra la velocità caratteristica di fotocatalisi e quella del processo accoppiato. Nel caso della sintesi di aromi, in cui la fotocatalisi viene accoppiata con la pervaporazione o con la dialisi ricircolando al reattore il retentato dalla cella con la membrana. Il parametro delta dipende dalla velocità di reazione, dalle proprietà di trasporto delle membrane e naturalmente dal volume del rettore e dall’area della membrana. La reazione fotocatalitica produce l’aroma, ad esempio vanillina da acido ferulico, per ossidazione parziale e grazie al recupero del prodotto se ne evita l’ulteriore ossidazione aumentandone pertanto la resa. L’operare in apparati separati offre diversi vantaggi come la possibilità di variare senza vincoli il rapporto tra area della membrana e volume del reattore, ma impone di considerare anche il grado effettivo di accoppiamento dei processi. In questo caso, come evidenziato dal modello matematico, un sufficientemente elevato rapporto di ricircolo consente comunque di integrare efficacemente i processi. Nell’ozonizzazione fotocatalitica si hanno due importanti vantaggi: l’aumento della velocità di degradazione grazie alla sinergia tra i processi e la capacità di controllare la formazione di prodotti pericolosi. La sinergia viene massimizzata ad un valore ottimale di delta, mentre la formazione dei prodotti indesiderati viene controllata operando secondo le procedure che sono state individuate.

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Development of interfaces for sample introduction from high pressures is important for real-time online hyphenation of chromatographic and other separation devices with mass spectrometry (MS) or accelerator mass spectrometry (AMS). Momentum separators can reduce unwanted low-density gases and introduce the analyte into the vacuum. In this work, the axial jet separator, a new momentum interface, is characterized by theory and empirical optimization. The mathematical model describes the different axial penetration of the components of a jetgas mixture and explains the empirical results for injections of CO2 in helium into MS and AMS instruments. We show that the performance of the new interface is sensitive to the nozzle size, showing good qualitative agreement with the mathematical model. Smaller nozzle sizes are more preferable due to their higher inflow capacity. The CO2 transmission efficiency of the interface into a MS instrument is ~14% (CO2/helium separation factor of 2.7). The interface receives and delivers flows of ~17.5 mL/min and ~0.9 mL/min, respectively. For the interfaced AMS instrument, the ionization and overall efficiencies are 0.7-3% and 0.1-0.4%, respectively, for CO2 amounts of 4-0.6 µg C, which is only slightly lower compared to conventional systems using intermediate trapping. The ionization efficiency depends on to the carbon mass flow in the injected pulse and is suppressed at high CO2 flows. Relative to a conventional jet separator, the transmission efficiency of the axial jet separator is lower, but its performance is less sensitive to misalignments.

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The small heat shock proteins (sHSPs) are ubiquitous stress proteins proposed to act as molecular chaperones to prevent irreversible protein denaturation. We characterized the chaperone activity of Synechocystis HSP17 and found that it has not only protein-protective activity, but also a previously unrecognized ability to stabilize lipid membranes. Like other sHSPs, recombinant Synechocystis HSP17 formed stable complexes with denatured malate dehydrogenase and served as a reservoir for the unfolded substrate, transferring it to the DnaK/DnaJ/GrpE and GroEL/ES chaperone network for subsequent refolding. Large unilamellar vesicles made of synthetic and cyanobacterial lipids were found to modulate this refolding process. Investigation of HSP17-lipid interactions revealed a preference for the liquid crystalline phase and resulted in an elevated physical order in model lipid membranes. Direct evidence for the participation of HSP17 in the control of thylakoid membrane physical state in vivo was gained by examining an hsp17− deletion mutant compared with the isogenic wild-type hsp17+ revertant Synechocystis cells. We suggest that, together with GroEL, HSP17 behaves as an amphitropic protein and plays a dual role. Depending on its membrane or cytosolic location, it may function as a “membrane stabilizing factor” as well as a member of a multichaperone protein-folding network. Membrane association of sHSPs could antagonize the heat-induced hyperfluidization of specific membrane domains and thereby serve to preserve structural and functional integrity of biomembranes.

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Micro-organismos fotossintetizantes, incluído aqui o gênero Arthrospira, vêm sendo amplamente produzidos em larga escala em vários países, detendo um mercado que gera mais de 1 bilhão de dólares ao ano. A produção industrial utiliza grande volume de água com alta concentração salina para produzir milhares de toneladas de biomassa microalgal. É crescente a utilização de tratamento de águas por processo de separação por membranas, demonstrando ser uma técnica que gera água de ótima qualidade, de instalação compacta e de fácil automação. No presente trabalho, foi avaliada esta tecnologia para o reaproveitamento do meio de cultura em novos cultivos de micro-organismos fotossintetizantes, visando contribuir para a sustentabilidade deste processo produtivo. O efluente do cultivo de Arthrospira platensis oriundo de processo descontínuo em minitanques foi submetido a tratamento por membranas de filtração tangencial, incluindo microfiltração (MF) (porosidades de 0,65 µm e de 0,22 µm) e ultrafiltração (UF) (peso molecular de corte de 5.000 Da), em pressões transmembrana (TMP) de 22,5 a 90 kPa. Os processos de MF levaram a reduções médias de 53,9±1,3 % e 93,1±1,1 % de matéria orgânica natural (NOM) e pigmentos nos meios residuais, respectivamente. Com o uso de processos de UF, cujos meios foram previamente tratados por MF (0,22 µm e 22,5 kPa), as reduções médias de NOM e pigmentos foram de 57,2±0,5 % e 94,0±0,8 %, respectivamente. Os processos de MF com TMP de 22,5 kPa levaram a concentrações celulares máximas (Xm) equivalentes às obtidas com meio novo. O uso de membrana de 0,65 µm e TMP de 22,5 kPa levou a uma perda média de 2,9 %, 22,7 % e 16,4% dos nutrientes carbonato, fosfato e nitrato, respectivamente, mas a correção desses valores aos mesmos do meio padrão levou à obtenção dos mais altos valores de Xm (3586,6±80 mg L-1), produtividade em células (505,0±11,6 mg L-1 d-1) e fator de conversão de nitrogênio em células (29,6±0,7 mg mg-1). O teor protéico da biomassa foi estatisticamente igual ao da biomassa obtida de cultivo com meio padrão novo. Os dados deste trabalho evidenciam que processos de filtração por membrana são promissores para o reuso de meio de micro-organismos fotossintetizantes.

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E-cadherin is a cell-cell adhesion protein that is trafficked and delivered to the basolateral cell surface. Membrane-bound carriers for the post-Golgi exocytosis of E-cadherin have not been characterized. Green fluorescent protein (GFP)-tagged E-cadherin (Ecad-GFP) is transported from the trans-Golgi network (TGN) to the recycling endosome on its way to the cell surface in tubulovesicular carriers that resemble TGN tubules labeled by members of the golgin family of tethering proteins. Here, we examine the association of golgins with tubular carriers containing E-cadherin as cargo. Fluorescent GRIP domains from golgin proteins replicate the membrane binding of the full-length proteins and were coexpressed with Ecad-GFP. The GRIP domains of p230/golgin-245 and golgin-97 had overlapping but nonidentical distributions on the TGN; both domains were on TGN-derived tubules but only the golgin-97 GRIP domain coincided with Ecad-GFP tubules in live cells. When the Arl1-binding endogenous golgins, p230/golgin-245 and golgin-97 were displaced from Golgi membranes by overexpression of the p230 GRIP domain, trafficking of Ecad-GFP was inhibited. siRNA knockdown of golgin-97 also inhibited trafficking of Ecad-GFP. Thus, the GRIP domains of p230/golgin-245 and golgin-97 bind discriminately to distinct membrane subdomains of the TGN. Golgin-97 is identified as a selective and essential component of the tubulovesicular carriers transporting E-cadherin out of the TGN.

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The gene encoding the matricellular protein secreted protein, acidic and rich in cysteine (SPARC) was identified in a screen for genes expressed sex-specifically during mouse gonad development, as being strongly upregulated in the male gonad from very early in testis development. We present here a detailed analysis of SPARC gene and protein expression during testis development, from 11.5 to 15.5 days post coitum (dpc). Section in situ hybridization analysis revealed that SPARC mRNA is expressed by the Sertoli cells in the testis cords and the fetal Leydig cells, found within the interstitial space between the testis cords. Immunodetection with anti-SPARC antibody showed that the protein was located inside the testis cords, within the cytoplasm of Sertoli and germ cells. In the interstitium, SPARC was present intracellularly within the Leydig cells. The internalization of SPARC in Sertoli, Leydig, and germ cells suggests that it plays an intracellular regulatory role in these cell types during fetal testis development.

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The total thermoplastics pipe market in west Europe is estimated at 900,000 metric tonnes for 1977 and is projected to grow to some 1.3 million tonnes of predominantly PVC and polyolefins pipe by 1985. By that time, polyethylene for gas distribution pipe and fittings will represent some 30% of the total polyethylene pipe market. The performance characteristics of a high density polyethylene are significantly influenced by both molecular weight and type of comonomer; the major influences being in the long-term hoop stress resistance and the environmental stress cracking resistance. Minor amounts of hexene-1 are more effective than comonomers lower in the homologous series, although there is some sacrifice of density related properties. A synergistic improvement is obtained by combining molecular weight increase with copolymerisation. The Long-term design strength of polyethylene copolymers can be determined from hoop stress measurement at elevated temperatures and by means of a separation factor of approximate value 22, extrapolation can be made to room temperature performance for a water environment. A polyethylene of black composition has a sufficiently improved performance over yellow pigmented pipe to cast doubts on the validity of internationally specifying yellow coded pipe for gas distribution service. The chemical environment (condensate formation) that can exist in natural gas distribution networks has a deleterious effect on the pipe performance the reduction amounting to at least two decades in log time. Desorption of such condensate is very slow and the influence of the more aggressive aromatic components is to lead to premature stress cracking. For natural gas distribution purposes, the design stress rating should be 39 Kg/cm2 for polyethylenes in the molecular weight range of 150 - 200,000 and 55 Kg/cm2 for higher molecular weight materials.

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We analyse the size and density of thermally induced regions of close contact in cell : cell contact interfaces within a harmonic potential approximation, estimating these regions to be below one-tenth of a micron across. Our calculations indicate that as the distance between the close contact threshold depth and the mean membrane-membrane separation increases, the density of close contact patches decreases exponentially while there is only a minimal variation in their mean size. The technique developed can be used to calculate the probability of first crossing in reflection symmetry violating systems. © Europhysics Letters Association.