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		<title>Membranes</title>
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	<title><![CDATA[Membranes, Vol. 3, Pages 69-86: Pd-Ag Membrane Coupled to a Two-Zone Fluidized Bed Reactor (TZFBR) for Propane Dehydrogenation on a  Pt-Sn/MgAl2O4 Catalyst]]></title>
	<link>http://www.mdpi.com/2077-0375/3/2/69</link>
	<description>Several reactor configurations have been tested for catalytic propane dehydrogenation employing Pt-Sn/MgAl2O4 as a catalyst. Pd-Ag alloy membranes coupled to the multifunctional Two-Zone Fluidized Bed Reactor (TZFBR) provide an improvement in propane conversion by hydrogen removal from the reaction bed through the inorganic membrane in addition to in situ catalyst regeneration. Twofold process intensification is thereby achieved when compared to the use of traditional fluidized bed reactors (FBR), where coke formation and thermodynamic equilibrium represent important process limitations. Experiments were carried out at 500–575 °C and with catalyst mass to molar flow of fed propane ratios between 15.1 and 35.2 g min mmol−1, employing three different reactor configurations: FBR, TZFBR and TZFBR + Membrane (TZFBR + MB). The results in the FBR showed catalyst deactivation, which was faster at high temperatures. In contrast, by employing the TZFBR with the optimum regenerative agent flow (diluted oxygen), the process activity was sustained throughout the time on stream. The TZFBR + MB showed promising results in catalytic propane dehydrogenation, displacing the reaction towards higher propylene production and giving the best results among the different reactor configurations studied. Furthermore, the results obtained in this study were better than those reported on conventional reactors.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2013-05-14</prism:publicationDate>
	<prism:volume>3</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes3020069</prism:doi>
	<prism:startingPage>69</prism:startingPage>
		<prism:endingPage>86</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Pd-Ag Membrane Coupled to a Two-Zone Fluidized Bed Reactor (TZFBR) for Propane Dehydrogenation on a  Pt-Sn/MgAl2O4 Catalyst]]></dc:title>
    <dc:date>2013-05-14</dc:date>
	<dc:identifier>doi: 10.3390/membranes3020069</dc:identifier>
    	<dc:creator>José-Antonio Medrano</dc:creator>
		<dc:creator>Ignacio Julián</dc:creator>
		<dc:creator>Javier Herguido</dc:creator>
		<dc:creator>Miguel Menéndez</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/3/2/44">
	<title><![CDATA[Membranes, Vol. 3, Pages 44-68: Experimental Study of Membrane Fouling during Crossflow Microfiltration of Yeast and Bacteria Suspensions: Towards an Analysis at the Microscopic Level]]></title>
	<link>http://www.mdpi.com/2077-0375/3/2/44</link>
	<description>Microfiltration of model cell suspensions combining macroscopic and microscopic approaches was studied in order to better understand microbial membrane fouling mechanisms. The respective impact of Saccharomyces cerevisiae yeast and Escherichia coli bacteria on crossflow microfiltration performances was investigated using a multichannel ceramic 0.2 µm membrane. Pure yeast suspensions (5 µm ovoid cells) and mixtures of yeast and bacteria (1 to 2.5 µm rod shape cells) were considered in order to analyse the effect of interaction between these two microorganisms on fouling reversibility. The resistances varied significantly with the concentration and characteristics of the microorganisms. Membrane fouling with pure yeast suspension was mainly reversible. For yeast and bacteria mixed suspensions (6 g L−1 yeast concentration) the increase in bacteria from 0.15 to 0.30 g L−1 increased the percentage of normalized reversible resistance. At 10 g L−1 yeast concentration, the addition of bacteria tends to increase the percentage of normalized irreversible resistance. For the objective of performing local analysis of fouling, an original filtration chamber allowing direct in situ observation of the cake by confocal laser scanning microscopy (CLSM) was designed, developed and validated. This device will be used in future studies to characterize cake structure at the microscopic scale.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2013-05-10</prism:publicationDate>
	<prism:volume>3</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes3020044</prism:doi>
	<prism:startingPage>44</prism:startingPage>
		<prism:endingPage>68</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Experimental Study of Membrane Fouling during Crossflow Microfiltration of Yeast and Bacteria Suspensions: Towards an Analysis at the Microscopic Level]]></dc:title>
    <dc:date>2013-05-10</dc:date>
	<dc:identifier>doi: 10.3390/membranes3020044</dc:identifier>
    	<dc:creator>Ines Hassan</dc:creator>
		<dc:creator>Monia Ennouri</dc:creator>
		<dc:creator>Christine Lafforgue</dc:creator>
		<dc:creator>Philippe Schmitz</dc:creator>
		<dc:creator>Abdelmoneim Ayadi</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/3/2/24">
	<title><![CDATA[Membranes, Vol. 3, Pages 24-43: Development and Testing of a Fully Adaptable Membrane Bioreactor Fouling Model for a Sidestream  Configuration System]]></title>
	<link>http://www.mdpi.com/2077-0375/3/2/24</link>
	<description>A dead-end filtration model that includes the three main fouling mechanisms mentioned in Hermia (i.e., cake build-up, complete pore blocking, and pore constriction) and that was based on a constant trans-membrane pressure (TMP) operation was extensively modified so it could be used for a sidestream configuration membrane bioreactor (MBR) situation. Modifications and add-ons to this basic model included: alteration so that it could be used for varying flux and varying TMP operations; inclusion of a backwash mode; it described pore constriction (i.e., irreversible fouling) in relation to the concentration of soluble microbial products (SMP) in the liquor; and, it could be used in a cross flow scenario by the addition of scouring terms in the model formulation. The additional terms in this modified model were checked against an already published model to see if they made sense, physically speaking. Next this modified model was calibrated and validated in Matlab© using data collected by carrying out flux stepping tests on both a pilot sidestream MBR plant, and then a pilot membrane filtration unit. The model fit proved good, especially for the pilot filtration unit data. In conclusion, this model formulation is of the right level of complexity to be used for most practical MBR situations.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2013-04-24</prism:publicationDate>
	<prism:volume>3</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes3020024</prism:doi>
	<prism:startingPage>24</prism:startingPage>
		<prism:endingPage>43</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Development and Testing of a Fully Adaptable Membrane Bioreactor Fouling Model for a Sidestream  Configuration System]]></dc:title>
    <dc:date>2013-04-24</dc:date>
	<dc:identifier>doi: 10.3390/membranes3020024</dc:identifier>
    	<dc:creator>Parneet Paul</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/3/1/16">
	<title><![CDATA[Membranes, Vol. 3, Pages 16-23: Comparing and Contrasting Traditional Membrane Bioreactor Models with Novel Ones Based on Time Series Analysis]]></title>
	<link>http://www.mdpi.com/2077-0375/3/1/16</link>
	<description>The computer modelling and simulation of wastewater treatment plant and their specific technologies, such as membrane bioreactors (MBRs), are becoming increasingly useful to consultant engineers when designing, upgrading, retrofitting, operating and controlling these plant. This research uses traditional phenomenological mechanistic models based on MBR filtration and biochemical processes to measure the effectiveness of alternative and novel time series models based upon input–output system identification methods. Both model types are calibrated and validated using similar plant layouts and data sets derived for this purpose. Results prove that although both approaches have their advantages, they also have specific disadvantages as well. In conclusion, the MBR plant designer and/or operator who wishes to use good quality, calibrated models to gain a better understanding of their process, should carefully consider which model type is selected based upon on what their initial modelling objectives are. Each situation usually proves unique.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2013-02-06</prism:publicationDate>
	<prism:volume>3</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes3010016</prism:doi>
	<prism:startingPage>16</prism:startingPage>
		<prism:endingPage>23</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Comparing and Contrasting Traditional Membrane Bioreactor Models with Novel Ones Based on Time Series Analysis]]></dc:title>
    <dc:date>2013-02-06</dc:date>
	<dc:identifier>doi: 10.3390/membranes3010016</dc:identifier>
    	<dc:creator>Parneet Paul</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/3/1/1">
	<title><![CDATA[Membranes, Vol. 3, Pages 1-15: Electrodialytic Transport Properties of Anion-Exchange Membranes Prepared from Poly(vinyl alcohol) and Poly(vinyl alcohol-co-methacryloyl aminopropyl trimethyl ammonium chloride)]]></title>
	<link>http://www.mdpi.com/2077-0375/3/1/1</link>
	<description>Random-type anion-exchange membranes (AEMs) have been prepared by blending poly(vinyl alcohol) (PVA) and the random copolymer-type polycation, poly(vinyl alcohol-co-methacryloyl aminopropyl trimethyl ammonium chloride) at various molar percentages of anion-exchange groups to vinyl alcohol groups, Cpc, and by cross-linking the PVA chains with glutaraldehyde (GA) solution at various GA concentrations, CGA. The characteristics of the random-type AEMs were compared with blend-type AEMs prepared in our previous study. At equal molar percentages of the anion exchange groups, the water content of the random-type AEMs was lower than that of the blend-type AEMs. The effective charge density of the random-type AEMs increased with increasing Cpc and reached a maximum value. Further, the maximum value of the effective charge density increased with increasing CGA. The maximum value of the effective charge density, 0.42 mol/dm3, was obtained for the random-type AEM with Cpc = 4.2 mol % and CGA = 0.15 vol %. A comparison of the random-type and blend-type AEMs with almost the same Cpc showed that the random-type AEMs had lower membrane resistance than the blend-type ones. The membrane resistance and dynamic transport number of the random-type AEM with Cpc = 6.0 mol % and CGA = 0.15 vol % were 4.8 Ω cm2 and 0.83, respectively.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2013-01-02</prism:publicationDate>
	<prism:volume>3</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes3010001</prism:doi>
	<prism:startingPage>1</prism:startingPage>
		<prism:endingPage>15</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Electrodialytic Transport Properties of Anion-Exchange Membranes Prepared from Poly(vinyl alcohol) and Poly(vinyl alcohol-co-methacryloyl aminopropyl trimethyl ammonium chloride)]]></dc:title>
    <dc:date>2013-01-02</dc:date>
	<dc:identifier>doi: 10.3390/membranes3010001</dc:identifier>
    	<dc:creator>Atsushi Jikihara</dc:creator>
		<dc:creator>Reina Ohashi</dc:creator>
		<dc:creator>Yuriko Kakihana</dc:creator>
		<dc:creator>Mitsuru Higa</dc:creator>
		<dc:creator>Kenichi Kobayashi</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/855">
	<title><![CDATA[Membranes, Vol. 2, Pages 855-878: U.S. DOE Progress Towards Developing Low-Cost, High Performance, Durable Polymer Electrolyte Membranes  for Fuel Cell Applications]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/855</link>
	<description>Low cost, durable, and selective membranes with high ionic conductivity are a priority need for wide-spread adoption of polymer electrolyte membrane fuel cells (PEMFCs) and direct methanol fuel cells (DMFCs). Electrolyte membranes are a major cost component of PEMFC stacks at low production volumes. PEMFC membranes also impose limitations on fuel cell system operating conditions that add system complexity and cost. Reactant gas and fuel permeation through the membrane leads to decreased fuel cell performance, loss of efficiency, and reduced durability in both PEMFCs and DMFCs. To address these challenges, the U.S. Department of Energy (DOE) Fuel Cell Technologies Program, in the Office of Energy Efficiency and Renewable Energy, supports research and development aimed at improving ion exchange membranes for fuel cells. For PEMFCs, efforts are primarily focused on developing materials for higher temperature operation (up to 120 °C) in automotive applications. For DMFCs, efforts are focused on developing membranes with reduced methanol permeability. In this paper, the recently revised DOE membrane targets, strategies, and highlights of DOE-funded projects to develop new, inexpensive membranes that have good performance in hot and dry conditions (PEMFC) and that reduce methanol crossover (DMFC) will be discussed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-12-18</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2040855</prism:doi>
	<prism:startingPage>855</prism:startingPage>
		<prism:endingPage>878</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[U.S. DOE Progress Towards Developing Low-Cost, High Performance, Durable Polymer Electrolyte Membranes  for Fuel Cell Applications]]></dc:title>
    <dc:date>2012-12-18</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040855</dc:identifier>
    	<dc:creator>Cassidy Houchins</dc:creator>
		<dc:creator>Greg Kleen</dc:creator>
		<dc:creator>Jacob Spendelow</dc:creator>
		<dc:creator>John Kopasz</dc:creator>
		<dc:creator>David Peterson</dc:creator>
		<dc:creator>Nancy Garland</dc:creator>
		<dc:creator>Donna Ho</dc:creator>
		<dc:creator>Jason Marcinkoski</dc:creator>
		<dc:creator>Kathi Martin</dc:creator>
		<dc:creator>Reginald Tyler</dc:creator>
		<dc:creator>Dimitrios Papageorgopoulos</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/841">
	<title><![CDATA[Membranes, Vol. 2, Pages 841-854: A Study of the Effect of Heat-Treatment on the Morphology of Nafion Ionomer Dispersion for Use in the Passive Direct Methanol Fuel Cell (DMFC)]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/841</link>
	<description>Aggregation in heat-treated Nafion ionomer dispersion and 117 membrane are investigated by 1H and 19F Nuclear Magnetic Resonance (NMR) spectra, spin-lattice relaxation time, and self-diffusion coefficient measurements. Results demonstrate that heat-treatment affects the average Nafion particle size in aqueous dispersions. Measurements on heat-treated Nafion 117 membrane show changes in the 1H isotropic chemical shift and no significant changes in ionic conductivity. Scanning electron microscopy (SEM) analysis of prepared cathode catalyst layer containing the heat-treated dispersions reveals that the surface of the electrode with the catalyst ink that has been pretreated at ca. 80 °C exhibits a compact and uniform morphology. The decrease of Nafion ionomer’s size results in better contact between catalyst particles and electrolyte, higher electrochemically active surface area, as well as significant improvement in the DMFC’s performance, as verified by electrochemical analysis and single cell evaluation.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-12-06</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2040841</prism:doi>
	<prism:startingPage>841</prism:startingPage>
		<prism:endingPage>854</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[A Study of the Effect of Heat-Treatment on the Morphology of Nafion Ionomer Dispersion for Use in the Passive Direct Methanol Fuel Cell (DMFC)]]></dc:title>
    <dc:date>2012-12-06</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040841</dc:identifier>
    	<dc:creator>Ting Yuan</dc:creator>
		<dc:creator>Haifeng Zhang</dc:creator>
		<dc:creator>Zhiqing Zou</dc:creator>
		<dc:creator>Sufia Khatun</dc:creator>
		<dc:creator>Daniel Akins</dc:creator>
		<dc:creator>Yara Adam</dc:creator>
		<dc:creator>Sophia Suarez</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/804">
	<title><![CDATA[Membranes, Vol. 2, Pages 804-840: Biofouling of Water Treatment Membranes: A Review of the Underlying Causes, Monitoring Techniques and Control Measures]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/804</link>
	<description>Biofouling is a critical issue in membrane water and wastewater treatment as it greatly compromises the efficiency of the treatment processes. It is difficult to control, and significant economic resources have been dedicated to the development of effective biofouling monitoring and control strategies. This paper highlights the underlying causes of membrane biofouling and provides a review on recent developments of potential monitoring and control methods in water and wastewater treatment with the aim of identifying the remaining issues and challenges in this area.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-11-21</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2040804</prism:doi>
	<prism:startingPage>804</prism:startingPage>
		<prism:endingPage>840</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Biofouling of Water Treatment Membranes: A Review of the Underlying Causes, Monitoring Techniques and Control Measures]]></dc:title>
    <dc:date>2012-11-21</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040804</dc:identifier>
    	<dc:creator>Thang Nguyen</dc:creator>
		<dc:creator>Felicity Roddick</dc:creator>
		<dc:creator>Linhua Fan</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/783">
	<title><![CDATA[Membranes, Vol. 2, Pages 783-803: Microscopic Analysis of Current and Mechanical Properties of Nafion® Studied by Atomic Force Microscopy]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/783</link>
	<description>The conductivity of fuel cell membranes as well as their mechanical properties at the nanometer scale were characterized using advanced tapping mode atomic force microscopy (AFM) techniques. AFM produces high-resolution images under continuous current flow of the conductive structure at the membrane surface and provides some insight into the bulk conducting network in Nafion membranes. The correlation of conductivity with other mechanical properties, such as adhesion force, deformation and stiffness, were simultaneously measured with the current and provided an indication of subsurface phase separations and phase distribution at the surface of the membrane. The distribution of conductive pores at the surface was identified by the formation of water droplets. A comparison of nanostructure models with high-resolution current images is discussed in detail.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-11-16</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2040783</prism:doi>
	<prism:startingPage>783</prism:startingPage>
		<prism:endingPage>803</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Microscopic Analysis of Current and Mechanical Properties of Nafion® Studied by Atomic Force Microscopy]]></dc:title>
    <dc:date>2012-11-16</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040783</dc:identifier>
    	<dc:creator>Renate Hiesgen</dc:creator>
		<dc:creator>Stefan Helmly</dc:creator>
		<dc:creator>Ines Galm</dc:creator>
		<dc:creator>Tobias Morawietz</dc:creator>
		<dc:creator>Michael Handl</dc:creator>
		<dc:creator>K. Friedrich</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/764">
	<title><![CDATA[Membranes, Vol. 2, Pages 764-782: Validation and Analysis of Forward Osmosis CFD Model in Complex 3D Geometries]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/764</link>
	<description>In forward osmosis (FO), an osmotic pressure gradient generated across a semi-permeable membrane is used to generate water transport from a dilute feed solution into a concentrated draw solution. This principle has shown great promise in the areas of water purification, wastewater treatment, seawater desalination and power generation. To ease optimization and increase understanding of membrane systems, it is desirable to have a comprehensive model that allows for easy investigation of all the major parameters in the separation process. Here we present experimental validation of a computational fluid dynamics (CFD) model developed to simulate FO experiments with asymmetric membranes. Simulations are compared with experimental results obtained from using two distinctly different complex three-dimensional membrane chambers. It is found that the CFD model accurately describes the solute separation process and water permeation through membranes under various flow conditions. It is furthermore demonstrated how the CFD model can be used to optimize membrane geometry in such as way as to promote the mass transfer.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-11-09</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2040764</prism:doi>
	<prism:startingPage>764</prism:startingPage>
		<prism:endingPage>782</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Validation and Analysis of Forward Osmosis CFD Model in Complex 3D Geometries]]></dc:title>
    <dc:date>2012-11-09</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040764</dc:identifier>
    	<dc:creator>Mathias F. Gruber</dc:creator>
		<dc:creator>Carl J. Johnson</dc:creator>
		<dc:creator>Chuyang Tang</dc:creator>
		<dc:creator>Mogens H. Jensen</dc:creator>
		<dc:creator>Lars Yde</dc:creator>
		<dc:creator>Claus Hélix-Nielsen</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/727">
	<title><![CDATA[Membranes, Vol. 2, Pages 727-763: Investigation of Cross-Linked and Additive Containing Polymer Materials for Membranes with Improved Performance in Pervaporation and Gas Separation]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/727</link>
	<description>Pervaporation and gas separation performances of polymer membranes can be improved by crosslinking or addition of metal-organic frameworks (MOFs). Crosslinked copolyimide membranes show higher plasticization resistance and no significant loss in selectivity compared to non-crosslinked membranes when exposed to mixtures of CO2/CH4 or toluene/cyclohexane. Covalently crosslinked membranes reveal better separation performances than ionically crosslinked systems. Covalent interlacing with 3-hydroxypropyldimethylmaleimide as photocrosslinker can be investigated in situ in solution as well as in films, using transient UV/Vis and FTIR spectroscopy. The photocrosslinking yield can be determined from the FTIR-spectra. It is restricted by the stiﬀness of the copolyimide backbone, which inhibits the photoreaction due to spatial separation of the crosslinker side chains. Mixed-matrix membranes (MMMs) with MOFs as additives (fillers) have increased permeabilities and often also selectivities compared to the pure polymer. Incorporation of MOFs into polysulfone and Matrimid® polymers for MMMs gives defect-free membranes with performances similar to the best polymer membranes for gas mixtures, such as O2/N2 H2/CH4, CO2/CH4, H2/CO2, CH4/N2 and CO2/N2 (preferentially permeating gas is named first). The MOF porosity, its particle size and content in the MMM are factors to influence the permeability and the separation performance of the membranes.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-10-22</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2040727</prism:doi>
	<prism:startingPage>727</prism:startingPage>
		<prism:endingPage>763</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Investigation of Cross-Linked and Additive Containing Polymer Materials for Membranes with Improved Performance in Pervaporation and Gas Separation]]></dc:title>
    <dc:date>2012-10-22</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040727</dc:identifier>
    	<dc:creator>Katharina Hunger</dc:creator>
		<dc:creator>Nadine Schmeling</dc:creator>
		<dc:creator>Harold B. Tanh Jeazet</dc:creator>
		<dc:creator>Christoph Janiak</dc:creator>
		<dc:creator>Claudia Staudt</dc:creator>
		<dc:creator>Karl Kleinermanns</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/706">
	<title><![CDATA[Membranes, Vol. 2, Pages 706-726: Membranes for Environmentally Friendly Energy Processes]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/706</link>
	<description>Membrane separation systems require no or very little chemicals compared to standard unit operations. They are also easy to scale up, energy efficient, and already widely used in various gas and liquid separation processes. Different types of membranes such as common polymers, microporous organic polymers, fixed-site-carrier membranes, mixed matrix membranes, carbon membranes as well as inorganic membranes have been investigated for CO2 capture/removal and other energy processes in the last two decades. The aim of this work is to review the membrane systems applied in different energy processes, such as post-combustion, pre-combustion, oxyfuel combustion, natural gas sweetening, biogas upgrading, hydrogen production, volatile organic compounds (VOC) recovery and pressure retarded osmosis for power generation. Although different membranes could probably be used in a specific separation process, choosing a suitable membrane material will mainly depend on the membrane permeance and selectivity, process conditions (e.g., operating pressure, temperature) and the impurities in a gas stream (such as SO2, NOx, H2S, etc.). Moreover, process design and the challenges relevant to a membrane system are also being discussed to illustrate the membrane process feasibility for a specific application based on process simulation and economic cost estimation.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-10-18</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2040706</prism:doi>
	<prism:startingPage>706</prism:startingPage>
		<prism:endingPage>726</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Membranes for Environmentally Friendly Energy Processes]]></dc:title>
    <dc:date>2012-10-18</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040706</dc:identifier>
    	<dc:creator>Xuezhong He</dc:creator>
		<dc:creator>May-Britt Hägg</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/705">
	<title><![CDATA[Membranes, Vol. 2, Pages 705: Publisher’s Note: Withdraw and Republication of “UV-Induced Radical Photo-Polymerization: A Smart Tool for Preparing Polymer Electrolyte Membranes for Energy Storage Devices”]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/705</link>
	<description>It has been brought to the corresponding author’s attention by the administration office that some of the authors present in this paper [1] are contradicting with the rules and regulation of some of the confidential industrial projects which have been signed with strict regulations. Now it has aroused as a big trouble and, consequently, to solve this problem all the authors have determined that it should be retracted. This decision has been taken purely for bureaucratic aspect. We apologize for any inconvenience this may cause.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-10-17</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Retraction</prism:section>
	<prism:doi>10.3390/membranes2040705</prism:doi>
	<prism:startingPage>705</prism:startingPage>
		<prism:endingPage>705</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Publisher’s Note: Withdraw and Republication of “UV-Induced Radical Photo-Polymerization: A Smart Tool for Preparing Polymer Electrolyte Membranes for Energy Storage Devices”]]></dc:title>
    <dc:date>2012-10-17</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040705</dc:identifier>
    	<dc:creator>Shu-Kun Lin</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/4/687">
	<title><![CDATA[Membranes, Vol. 2, Pages 687-704: UV-Induced Radical Photo-Polymerization: A Smart Tool for Preparing Polymer Electrolyte Membranes for Energy Storage Devices]]></title>
	<link>http://www.mdpi.com/2077-0375/2/4/687</link>
	<description>In the present work, the preparation and characterization of quasi-solid polymer electrolyte membranes based on methacrylic monomers and oligomers, with the addition of organic plasticizers and lithium salt, are described. Noticeable improvements in the mechanical properties by reinforcement with natural cellulose hand-sheets or nanoscale microfibrillated cellulose fibers are also demonstrated. The ionic conductivity of the various prepared membranes is very high, with average values approaching 10-3 S cm-1 at ambient temperature. The electrochemical stability window is wide (anodic breakdown voltages &amp;gt; 4.5 V vs. Li in all the cases) along with good cyclability in lithium cells at ambient temperature. The galvanostatic cycling tests are conducted by constructing laboratory-scale lithium cells using LiFePO4 as cathode and lithium metal as anode with the selected polymer electrolyte membrane as the electrolyte separator. The results obtained demonstrate that UV induced radical photo-polymerization is a well suited method for an easy and rapid preparation of easy tunable quasi-solid polymer electrolyte membranes for energy storage devices.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-10-17</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2040687</prism:doi>
	<prism:startingPage>687</prism:startingPage>
		<prism:endingPage>704</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[UV-Induced Radical Photo-Polymerization: A Smart Tool for Preparing Polymer Electrolyte Membranes for Energy Storage Devices]]></dc:title>
    <dc:date>2012-10-17</dc:date>
	<dc:identifier>doi: 10.3390/membranes2040687</dc:identifier>
    	<dc:creator>Jijeesh R. Nair</dc:creator>
		<dc:creator>Annalisa Chiappone</dc:creator>
		<dc:creator>Matteo Destro</dc:creator>
		<dc:creator>Lara Jabbour</dc:creator>
		<dc:creator>Giuseppina Meligrana</dc:creator>
		<dc:creator>Claudio Gerbaldi</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/665">
	<title><![CDATA[Membranes, Vol. 2, Pages 665-686: Investigation of La1−xSrxCrO3−∂ (x ~ 0.1) as Membrane for Hydrogen Production]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/665</link>
	<description>Various inorganic membranes have demonstrated good capability to separate hydrogen from other gases at elevated temperatures. Hydrogen-permeable, dense, mixed proton-electron conducting ceramic oxides offer superior selectivity and thermal stability, but chemically robust candidates with higher ambipolar protonic and electronic conductivity are needed. In this work, we present for the first time the results of various investigations of La1−xSrxCrO3−∂ membranes for hydrogen production. We aim in particular to elucidate the material’s complex transport properties, involving co-ionic transport of oxide ions and protons, in addition to electron holes. This opens some new possibilities for efficient heat and mass transfer management in the production of hydrogen. Conductivity measurements as a function of pH2 at constant pO2 exhibit changes that reveal a significant hydration and presence of protons. The flux and production of hydrogen have been measured under different chemical gradients. In particular, the effect of water vapor in the feed and permeate gas stream sides was investigated with the aim of quantifying the ratio of hydrogen production by hydrogen flux from feed to permeate and oxygen flux the opposite way (“water splitting”). Deuterium labeling was used to unambiguously prove flux of hydrogen species.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-09-11</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030665</prism:doi>
	<prism:startingPage>665</prism:startingPage>
		<prism:endingPage>686</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Investigation of La1−xSrxCrO3−∂ (x ~ 0.1) as Membrane for Hydrogen Production]]></dc:title>
    <dc:date>2012-09-11</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030665</dc:identifier>
    	<dc:creator>Yngve Larring</dc:creator>
		<dc:creator>Camilla Vigen</dc:creator>
		<dc:creator>Florian Ahouanto</dc:creator>
		<dc:creator>Marie-Laure Fontaine</dc:creator>
		<dc:creator>Thijs Peters</dc:creator>
		<dc:creator>Jens B. Smith</dc:creator>
		<dc:creator>Truls Norby</dc:creator>
		<dc:creator>Rune Bredesen</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/585">
	<title><![CDATA[Membranes, Vol. 2, Pages 585-664: A Review of RedOx Cycling of Solid Oxide Fuel Cells Anode]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/585</link>
	<description>Solid oxide fuel cells are able to convert fuels, including hydrocarbons, to electricity with an unbeatable efficiency even for small systems. One of the main limitations for long-term utilization is the reduction-oxidation cycling (RedOx cycles) of the nickel-based anodes. This paper will review the effects and parameters influencing RedOx cycles of the Ni-ceramic anode. Second, solutions for RedOx instability are reviewed in the patent and open scientific literature. The solutions are described from the point of view of the system, stack design, cell design, new materials and microstructure optimization. Finally, a brief synthesis on RedOx cycling of Ni-based anode supports for standard and optimized microstructures is depicted.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-08-31</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2030585</prism:doi>
	<prism:startingPage>585</prism:startingPage>
		<prism:endingPage>664</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[A Review of RedOx Cycling of Solid Oxide Fuel Cells Anode]]></dc:title>
    <dc:date>2012-08-31</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030585</dc:identifier>
    	<dc:creator>Antonin Faes</dc:creator>
		<dc:creator>Aïcha Hessler-Wyser</dc:creator>
		<dc:creator>Amédée Zryd</dc:creator>
		<dc:creator>Jan Van herle</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/565">
	<title><![CDATA[Membranes, Vol. 2, Pages 565-584: Microbial Relevant Fouling in Membrane Bioreactors: Influencing Factors, Characterization, and Fouling Control]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/565</link>
	<description>Microorganisms in membrane bioreactors (MBRs) play important roles on degradation of organic/inorganic substances in wastewaters, while microbial deposition/growth and microbial product accumulation on membranes potentially induce membrane fouling. Generally, there is a need to characterize membrane foulants and to determine their relations to the evolution of membrane fouling in order to identify a suitable fouling control approach in MBRs. This review summarized the factors in MBRs that influence microbial behaviors (community compositions, physical properties, and microbial products). The state-of-the-art techniques to characterize biofoulants in MBRs were reported. The strategies for controlling microbial relevant fouling were discussed and the future studies on membrane fouling mechanisms in MBRs were proposed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-08-15</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2030565</prism:doi>
	<prism:startingPage>565</prism:startingPage>
		<prism:endingPage>584</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Microbial Relevant Fouling in Membrane Bioreactors: Influencing Factors, Characterization, and Fouling Control]]></dc:title>
    <dc:date>2012-08-15</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030565</dc:identifier>
    	<dc:creator>Bing Wu</dc:creator>
		<dc:creator>Anthony G. Fane</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/553">
	<title><![CDATA[Membranes, Vol. 2, Pages 553-564: Polymer Electrolytes for Lithium/Sulfur Batteries]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/553</link>
	<description>This review evaluates the characteristics and advantages of employing polymer electrolytes in lithium/sulfur (Li/S) batteries. The main highlights of this study constitute detailed information on the advanced developments for solid polymer electrolytes and gel polymer electrolytes, used in the lithium/sulfur battery. This includes an in-depth analysis conducted on the preparation and electrochemical characteristics of the Li/S batteries based on these polymer electrolytes.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-08-09</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2030553</prism:doi>
	<prism:startingPage>553</prism:startingPage>
		<prism:endingPage>564</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Polymer Electrolytes for Lithium/Sulfur Batteries]]></dc:title>
    <dc:date>2012-08-09</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030553</dc:identifier>
    	<dc:creator>Yan Zhao</dc:creator>
		<dc:creator>Yongguang Zhang</dc:creator>
		<dc:creator>Denise Gosselink</dc:creator>
		<dc:creator>The Nam Long Doan</dc:creator>
		<dc:creator>Mikhail Sadhu</dc:creator>
		<dc:creator>Ho-Jae Cheang</dc:creator>
		<dc:creator>Pu Chen</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/529">
	<title><![CDATA[Membranes, Vol. 2, Pages 529-552: Plasma Membranes Modified by Plasma Treatment or Deposition as Solid Electrolytes for Potential Application in Solid Alkaline Fuel Cells]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/529</link>
	<description>In the highly competitive market of fuel cells, solid alkaline fuel cells using liquid fuel (such as cheap, non-toxic and non-valorized glycerol) and not requiring noble metal as catalyst seem quite promising. One of the main hurdles for emergence of such a technology is the development of a hydroxide-conducting membrane characterized by both high conductivity and low fuel permeability. Plasma treatments can enable to positively tune the main fuel cell membrane requirements. In this work, commercial ADP-Morgane® fluorinated polymer membranes and a new brand of cross-linked poly(aryl-ether) polymer membranes, named AMELI-32®, both containing quaternary ammonium functionalities, have been modified by argon plasma treatment or triallylamine-based plasma deposit. Under the concomitant etching/cross-linking/oxidation effects inherent to the plasma modification, transport properties (ionic exchange capacity, water uptake, ionic conductivity and fuel retention) of membranes have been improved. Consequently, using plasma modified ADP-Morgane® membrane as electrolyte in a solid alkaline fuel cell operating with glycerol as fuel has allowed increasing the maximum power density by a factor 3 when compared to the untreated membrane.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-30</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030529</prism:doi>
	<prism:startingPage>529</prism:startingPage>
		<prism:endingPage>552</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Plasma Membranes Modified by Plasma Treatment or Deposition as Solid Electrolytes for Potential Application in Solid Alkaline Fuel Cells]]></dc:title>
    <dc:date>2012-07-30</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030529</dc:identifier>
    	<dc:creator>Marc Reinholdt</dc:creator>
		<dc:creator>Alina Ilie</dc:creator>
		<dc:creator>Stéphanie Roualdès</dc:creator>
		<dc:creator>Jérémy Frugier</dc:creator>
		<dc:creator>Mauricio Schieda</dc:creator>
		<dc:creator>Christophe Coutanceau</dc:creator>
		<dc:creator>Serguei Martemianov</dc:creator>
		<dc:creator>Valérie Flaud</dc:creator>
		<dc:creator>Eric Beche</dc:creator>
		<dc:creator>Jean Durand</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/510">
	<title><![CDATA[Membranes, Vol. 2, Pages 510-528: Electrochemical Membrane Reactors for Sustainable Chlorine Recycling]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/510</link>
	<description>Polymer electrolyte membranes have found broad application in a number of processes, being fuel cells, due to energy concerns, the main focus of the scientific community worldwide. Relatively little attention has been paid to the use of these materials in electrochemical production and separation processes. In this review, we put emphasis upon the application of Nafion membranes in electrochemical membrane reactors for chlorine recycling. The performance of such electrochemical reactors can be influenced by a number of factors including the properties of the membrane, which play an important role in reactor optimization. This review discusses the role of Nafion as a membrane, as well as its importance in the catalyst layer for the formation of the so-called three-phase boundary. The influence of an equilibrated medium on the Nafion proton conductivity and Cl− crossover, as well as the influence of the catalyst ink dispersion medium on the Nafion/catalyst self-assembly and its importance for the formation of an ionic conducting network in the catalyst layer are summarized.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-30</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2030510</prism:doi>
	<prism:startingPage>510</prism:startingPage>
		<prism:endingPage>528</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Electrochemical Membrane Reactors for Sustainable Chlorine Recycling]]></dc:title>
    <dc:date>2012-07-30</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030510</dc:identifier>
    	<dc:creator>Tanja Vidakovic-Koch</dc:creator>
		<dc:creator>Isai Gonzalez Martinez</dc:creator>
		<dc:creator>Rafael Kuwertz</dc:creator>
		<dc:creator>Ulrich Kunz</dc:creator>
		<dc:creator>Thomas Turek</dc:creator>
		<dc:creator>Kai Sundmacher</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/493">
	<title><![CDATA[Membranes, Vol. 2, Pages 493-509: Proton Content and Nature in Perovskite Ceramic Membranes for Medium Temperature Fuel Cells and Electrolysers]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/493</link>
	<description>Recent interest in environmentally friendly technology has promoted research on green house gas-free devices such as water steam electrolyzers, fuel cells and CO2/syngas converters. In such applications, proton conducting perovskite ceramics appear especially promising as electrolyte membranes. Prior to a successful industrial application, it is necessary to determine/understand their complex physical and chemical behavior, especially that related to proton incorporation mechanism, content and nature of bulk protonic species. Based on the results of quasi-elastic neutron scattering (QNS), thermogravimetric analysis (TGA), Raman and IR measurements we will show the complexity of the protonation process and the importance of differentiation between the protonic species adsorbed on a membrane surface and the bulk protons. The bulk proton content is very low, with a doping limit (~1–5 × 10−3 mole/mole), but sufficient to guarantee proton conduction below 600 °C. The bulk protons posses an ionic, covalent bond free nature and may occupy an interstitial site in the host perovskite structure.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-25</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030493</prism:doi>
	<prism:startingPage>493</prism:startingPage>
		<prism:endingPage>509</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Proton Content and Nature in Perovskite Ceramic Membranes for Medium Temperature Fuel Cells and Electrolysers]]></dc:title>
    <dc:date>2012-07-25</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030493</dc:identifier>
    	<dc:creator>Philippe Colomban</dc:creator>
		<dc:creator>Oumaya Zaafrani</dc:creator>
		<dc:creator>Aneta Slodczyk</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/478">
	<title><![CDATA[Membranes, Vol. 2, Pages 478-492: Anion- or Cation-Exchange Membranes for NaBH4/H2O2 Fuel Cells?]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/478</link>
	<description>Direct borohydride fuel cells (DBFC), which operate on sodium borohydride (NaBH4) as the fuel, and hydrogen peroxide (H2O2) as the oxidant, are receiving increasing attention. This is due to their promising use as power sources for space and underwater applications, where air is not available and gas storage poses obvious problems. One key factor to improve the performance of DBFCs concerns the type of separator used. Both anion- and cation-exchange membranes may be considered as potential separators for DBFC. In the present paper, the effect of the membrane type on the performance of laboratory NaBH4/H2O2 fuel cells using Pt electrodes is studied at room temperature. Two commercial ion-exchange membranes from Membranes International Inc., an anion-exchange membrane (AMI-7001S) and a cation-exchange membrane (CMI-7000S), are tested as ionic separators for the DBFC. The membranes are compared directly by the observation and analysis of the corresponding DBFC’s performance. Cell polarization, power density, stability, and durability tests are used in the membranes’ evaluation. Energy densities and specific capacities are estimated. Most tests conducted, clearly indicate a superior performance of the cation-exchange membranes over the anion-exchange membrane. The two membranes are also compared with several other previously tested commercial membranes. For long term cell operation, these membranes seem to outperform the stability of the benchmark Nafion membranes but further studies are still required to improve their instantaneous power load.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-19</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030478</prism:doi>
	<prism:startingPage>478</prism:startingPage>
		<prism:endingPage>492</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Anion- or Cation-Exchange Membranes for NaBH4/H2O2 Fuel Cells?]]></dc:title>
    <dc:date>2012-07-19</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030478</dc:identifier>
    	<dc:creator>Biljana Šljukić</dc:creator>
		<dc:creator>Ana L. Morais</dc:creator>
		<dc:creator>Diogo M. F. Santos</dc:creator>
		<dc:creator>César A. C. Sequeira</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/440">
	<title><![CDATA[Membranes, Vol. 2, Pages 440-477: Molecularly Imprinted Membranes]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/440</link>
	<description>Although the roots of molecularly imprinted polymers lie in the beginning of 1930s in the past century, they have had an exponential growth only 40–50 years later by the works of Wulff and especially by Mosbach. More recently, it was also proved that molecular imprinted membranes (i.e., polymer thin films) that show recognition properties at molecular level of the template molecule are used in their formation. Different procedures and potential application in separation processes and catalysis are reported. The influences of different parameters on the discrimination abilities are also discussed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-19</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2030440</prism:doi>
	<prism:startingPage>440</prism:startingPage>
		<prism:endingPage>477</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Molecularly Imprinted Membranes]]></dc:title>
    <dc:date>2012-07-19</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030440</dc:identifier>
    	<dc:creator>Francesco Trotta</dc:creator>
		<dc:creator>Miriam Biasizzo</dc:creator>
		<dc:creator>Fabrizio Caldera</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/430">
	<title><![CDATA[Membranes, Vol. 2, Pages 430-439: Poly(imide)/Organically-Modified Montmorillonite Nanocomposite as a Potential Membrane for Alkaline Fuel Cells]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/430</link>
	<description>In this work we evaluated the potentiality of a poly(imide) (PI)/organically-modified montmorillonite (O-MMT) nanocomposite membrane for the use in alkaline fuel cells. Both X-ray diffraction and scanning electron microscopy revealed a good dispersion of O-MMT into the PI matrix and preservation of the O-MMT layered structure. When compared to the pure PI, the addition of O-MMT improved thermal stability and markedly increased the capability of absorbing electrolyte and ionic conductivity of the composite. The results show that the PI/O-MMT nanocomposite is a promising candidate for alkaline fuel cell applications.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-18</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030430</prism:doi>
	<prism:startingPage>430</prism:startingPage>
		<prism:endingPage>439</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Poly(imide)/Organically-Modified Montmorillonite Nanocomposite as a Potential Membrane for Alkaline Fuel Cells]]></dc:title>
    <dc:date>2012-07-18</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030430</dc:identifier>
    	<dc:creator>Liliane C. Battirola</dc:creator>
		<dc:creator>Luiz H. S. Gasparotto</dc:creator>
		<dc:creator>Ubirajara P. Rodrigues-Filho</dc:creator>
		<dc:creator>Germano Tremiliosi-Filho</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/415">
	<title><![CDATA[Membranes, Vol. 2, Pages 415-429: Effectiveness of Water Desalination by Membrane Distillation Process]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/415</link>
	<description>The membrane distillation process constitutes one of the possibilities for a new method for water desalination. Four kinds of polypropylene membranes with different diameters of capillaries and pores, as well as wall thicknesses were used in studied. The morphology of the membrane used and the operating parameters significantly influenced process efficiency. It was found that the membranes with lower wall thickness and a larger pore size resulted in the higher yields. Increasing both feed flow rate and temperature increases the permeate flux and simultaneously the process efficiency. However, the use of higher flow rates also enhanced heat losses by conduction, which decreases the thermal efficiency. This efficiency also decreases when the salt concentration in the feed was enhanced. The influence of fouling on the process efficiency was considered.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-17</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030415</prism:doi>
	<prism:startingPage>415</prism:startingPage>
		<prism:endingPage>429</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Effectiveness of Water Desalination by Membrane Distillation Process]]></dc:title>
    <dc:date>2012-07-17</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030415</dc:identifier>
    	<dc:creator>Marek Gryta</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/395">
	<title><![CDATA[Membranes, Vol. 2, Pages 395-414: A Review of Molecular-Level Mechanism of Membrane Degradation in the Polymer Electrolyte Fuel Cell]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/395</link>
	<description>Chemical degradation of perfluorosulfonic acid (PFSA) membrane is one of the most serious problems for stable and long-term operations of the polymer electrolyte fuel cell (PEFC). The chemical degradation is caused by the chemical reaction between the PFSA membrane and chemical species such as free radicals. Although chemical degradation of the PFSA membrane has been studied by various experimental techniques, the mechanism of chemical degradation relies much on speculations from ex-situ observations. Recent activities applying theoretical methods such as density functional theory, in situ experimental observation, and mechanistic study by using simplified model compound systems have led to gradual clarification of the atomistic details of the chemical degradation mechanism. In this review paper, we summarize recent reports on the chemical degradation mechanism of the PFSA membrane from an atomistic point of view.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-10</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2030395</prism:doi>
	<prism:startingPage>395</prism:startingPage>
		<prism:endingPage>414</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[A Review of Molecular-Level Mechanism of Membrane Degradation in the Polymer Electrolyte Fuel Cell]]></dc:title>
    <dc:date>2012-07-10</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030395</dc:identifier>
    	<dc:creator>Takayoshi Ishimoto</dc:creator>
		<dc:creator>Michihisa Koyama</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/384">
	<title><![CDATA[Membranes, Vol. 2, Pages 384-394: A Composite Membrane of Caesium Salt of Heteropolyacids/Quaternary Diazabicyclo-Octane Polysulfone with Poly (Tetrafluoroethylene) for Intermediate Temperature Fuel Cells]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/384</link>
	<description>Inorganic-organic composite electrolyte membranes were fabricated from CsXH3−XPMo12O40 (CsPOMo) and quaternary diazabicyclo-octane polysulfone (QDPSU) using a polytetrafluoroethylene (PTFE) porous matrix for the application of intermediate temperature fuel cells. The CsPOMo/QDPSU/PTFE composite membrane was made proton conducting by using a relatively low phosphoric acid loading, which benefits the stability of the membrane conductivity and the mechanical strength. The casting method was used in order to build a thin and robust composite membrane. The resulting composite membrane films were characterised in terms of the elemental composition, membrane structure and morphology by EDX, FTIR and SEM. The proton conductivity of the membrane was 0.04 S cm−1 with a H3PO4 loading level of 1.8 PRU (amount of H3PO4 per repeat unit of polymer QDPSU). The fuel cell performance with the membrane gave a peak power density of 240 mW cm−2 at 150 °C and atmospheric pressure.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-10</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030384</prism:doi>
	<prism:startingPage>384</prism:startingPage>
		<prism:endingPage>394</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[A Composite Membrane of Caesium Salt of Heteropolyacids/Quaternary Diazabicyclo-Octane Polysulfone with Poly (Tetrafluoroethylene) for Intermediate Temperature Fuel Cells]]></dc:title>
    <dc:date>2012-07-10</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030384</dc:identifier>
    	<dc:creator>Chenxi Xu</dc:creator>
		<dc:creator>Xu Wang</dc:creator>
		<dc:creator>Xu Wu</dc:creator>
		<dc:creator>Yuancheng Cao</dc:creator>
		<dc:creator>Keith Scott</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/367">
	<title><![CDATA[Membranes, Vol. 2, Pages 367-383: Membranes in Lithium Ion Batteries]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/367</link>
	<description>Lithium ion batteries have proven themselves the main choice of power sources for portable electronics. Besides consumer electronics, lithium ion batteries are also growing in popularity for military, electric vehicle, and aerospace applications. The present review attempts to summarize the knowledge about some selected membranes in lithium ion batteries. Based on the type of electrolyte used, literature concerning ceramic-glass and polymer solid ion conductors, microporous filter type separators and polymer gel based membranes is reviewed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-07-04</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2030367</prism:doi>
	<prism:startingPage>367</prism:startingPage>
		<prism:endingPage>383</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Membranes in Lithium Ion Batteries]]></dc:title>
    <dc:date>2012-07-04</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030367</dc:identifier>
    	<dc:creator>Min Yang</dc:creator>
		<dc:creator>Junbo Hou</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/3/346">
	<title><![CDATA[Membranes, Vol. 2, Pages 346-366: Pure and Modified Co-Poly(amide-12-b-ethylene oxide) Membranes for Gas Separation Studied by Molecular Investigations]]></title>
	<link>http://www.mdpi.com/2077-0375/2/3/346</link>
	<description>This paper deals with a theoretical investigation of gas transport properties in a pure and modified PEBAX block copolymer membrane with N-ethyl-o/p-toluene sulfonamide (KET) as additive molecules. Molecular dynamics simulations using COMPASS force field, Gusev-Suter Transition State Theory (TST) and Monte Carlo methods were used. Bulk models of PEBAX and PEBAX/KET in different copolymer/additive compositions were assembled and analyzed to evaluate gas permeability and morphology to characterize structure-performance relationships.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-06-28</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2030346</prism:doi>
	<prism:startingPage>346</prism:startingPage>
		<prism:endingPage>366</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Pure and Modified Co-Poly(amide-12-b-ethylene oxide) Membranes for Gas Separation Studied by Molecular Investigations]]></dc:title>
    <dc:date>2012-06-28</dc:date>
	<dc:identifier>doi: 10.3390/membranes2030346</dc:identifier>
    	<dc:creator>Luana De Lorenzo</dc:creator>
		<dc:creator>Elena Tocci</dc:creator>
		<dc:creator>Annarosa Gugliuzza</dc:creator>
		<dc:creator>Enrico Drioli</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/325">
	<title><![CDATA[Membranes, Vol. 2, Pages 325-345: NMR and Electrochemical Investigation of the Transport Properties of Methanol and Water in Nafion and Clay-Nanocomposites Membranes for DMFCs]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/325</link>
	<description>Water and methanol transport behavior, solvents adsorption and electrochemical properties of filler-free Nafion and nanocomposites based on two smectite clays, were investigated using impedance spectroscopy, DMFC tests and NMR methods, including spin-lattice relaxation and pulsed-gradient spin-echo (PGSE) diffusion under variable temperature conditions. Synthetic (Laponite) and natural (Swy-2) smectite clays, with different structural and physical parameters, were incorporated into the Nafion for the creation of exfoliated nanocomposites. Transport mechanism of water and methanol appears to be influenced from the dimensions of the dispersed platelike silicate layers as well as from their cation exchange capacity (CEC). The details of the NMR results and the effect of the methanol solution concentration are discussed. Clays particles, and in particular Swy-2, demonstrate to be a potential physical barrier for methanol cross-over, reducing the methanol diffusion with an evident blocking effect yet nevertheless ensuring a high water mobility up to 130 °C and for several hours, proving the exceptional water retention property of these materials and their possible use in the DMFCs applications. Electrochemical behavior is investigated by cell resistance and polarization measurements. From these analyses it is derived that the addition of clay materials to recast Nafion decreases the ohmic losses at high temperatures extending in this way the operating range of a direct methanol fuel cell.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-06-20</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2020325</prism:doi>
	<prism:startingPage>325</prism:startingPage>
		<prism:endingPage>345</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[NMR and Electrochemical Investigation of the Transport Properties of Methanol and Water in Nafion and Clay-Nanocomposites Membranes for DMFCs]]></dc:title>
    <dc:date>2012-06-20</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020325</dc:identifier>
    	<dc:creator>Isabella Nicotera</dc:creator>
		<dc:creator>Kristina Angjeli</dc:creator>
		<dc:creator>Luigi Coppola</dc:creator>
		<dc:creator>Antonino S. Aricò</dc:creator>
		<dc:creator>Vincenzo Baglio</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/307">
	<title><![CDATA[Membranes, Vol. 2, Pages 307-324: UV-Induced Radical Photo-Polymerization: A Smart Tool for Preparing Polymer Electrolyte Membranes for Energy Storage Devices]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/307</link>
	<description>In the present work, the preparation and characterization of quasi-solid polymer electrolyte membranes based on methacrylic monomers and oligomers, with the addition of organic plasticizers and lithium salt, are described. Noticeable improvements in the mechanical properties by reinforcement with natural cellulose hand-sheets or nanoscale microfibrillated cellulose fibers are also demonstrated. The ionic conductivity of the various prepared membranes is very high, with average values approaching 10-3 S cm-1 at ambient temperature. The electrochemical stability window is wide (anodic breakdown voltages &amp;gt; 4.5 V vs. Li in all the cases) along with good cyclability in lithium cells at ambient temperature. The galvanostatic cycling tests are conducted by constructing laboratory-scale lithium cells using LiFePO4 as cathode and lithium metal as anode with the selected polymer electrolyte membrane as the electrolyte separator. The results obtained demonstrate that UV induced radical photo-polymerization is a well suited method for an easy and rapid preparation of easy tunable quasi-solid polymer electrolyte membranes for energy storage devices.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-06-19</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2020307</prism:doi>
	<prism:startingPage>307</prism:startingPage>
		<prism:endingPage>324</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[UV-Induced Radical Photo-Polymerization: A Smart Tool for Preparing Polymer Electrolyte Membranes for Energy Storage Devices]]></dc:title>
    <dc:date>2012-06-19</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020307</dc:identifier>
    	<dc:creator>Jijeesh R. Nair</dc:creator>
		<dc:creator>Annalisa Chiappone</dc:creator>
		<dc:creator>Matteo Destro</dc:creator>
		<dc:creator>Lara Jabbour</dc:creator>
		<dc:creator>Juqin Zeng</dc:creator>
		<dc:creator>Francesca Di Lupo</dc:creator>
		<dc:creator>Nadia Garino</dc:creator>
		<dc:creator>Giuseppina Meligrana</dc:creator>
		<dc:creator>Carlotta Francia</dc:creator>
		<dc:creator>Claudio Gerbaldi</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/275">
	<title><![CDATA[Membranes, Vol. 2, Pages 275-306: Membranes for Redox Flow Battery Applications]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/275</link>
	<description>The need for large scale energy storage has become a priority to integrate renewable energy sources into the electricity grid. Redox flow batteries are considered the best option to store electricity from medium to large scale applications. However, the current high cost of redox flow batteries impedes the wide spread adoption of this technology. The membrane is a critical component of redox flow batteries as it determines the performance as well as the economic viability of the batteries. The membrane acts as a separator to prevent cross-mixing of the positive and negative electrolytes, while still allowing the transport of ions to complete the circuit during the passage of current. An ideal membrane should have high ionic conductivity, low water intake and excellent chemical and thermal stability as well as good ionic exchange capacity. Developing a low cost, chemically stable membrane for redox flow cell batteries has been a major focus for many groups around the world in recent years. This paper reviews the research work on membranes for redox flow batteries, in particular for the all-vanadium redox flow battery which has received the most attention.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-06-19</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2020275</prism:doi>
	<prism:startingPage>275</prism:startingPage>
		<prism:endingPage>306</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Membranes for Redox Flow Battery Applications]]></dc:title>
    <dc:date>2012-06-19</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020275</dc:identifier>
    	<dc:creator>Helen Prifti</dc:creator>
		<dc:creator>Aishwarya Parasuraman</dc:creator>
		<dc:creator>Suminto Winardi</dc:creator>
		<dc:creator>Tuti Mariana Lim</dc:creator>
		<dc:creator>Maria Skyllas-Kazacos</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/253">
	<title><![CDATA[Membranes, Vol. 2, Pages 253-274: Synthesis, Multinuclear NMR Characterization and Dynamic Property of Organic–Inorganic Hybrid Electrolyte Membrane Based on Alkoxysilane and Poly(oxyalkylene) Diamine]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/253</link>
	<description>Organic–inorganic hybrid electrolyte membranes based on poly(propylene glycol)-block-poly(ethylene glycol)-block-poly(propylene glycol) bis(2-aminopropyl ether) complexed with LiClO4 via the co-condensation of tetraethoxysilane (TEOS) and 3-(triethoxysilyl)propyl isocyanate have been prepared and characterized. A variety of techniques such as differential scanning calorimetry (DSC), Fourier transform infrared (FTIR) spectroscopy, alternating current (AC) impedance and solid-state nuclear magnetic resonance (NMR) spectroscopy are performed to elucidate the relationship between the structural and dynamic properties of the hybrid electrolyte and the ion mobility. A VTF (Vogel-Tamman-Fulcher)-like temperature dependence of ionic conductivity is observed for all the compositions studied, implying that the diffusion of charge carriers is assisted by the segmental motions of the polymer chains. A maximum ionic conductivity value of 5.3 × 10−5 Scm−1 is obtained at 30 °C. Solid-state NMR results provide a microscopic view of the effects of salt concentrations on the dynamic behavior of the polymer chains.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-06-13</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2020253</prism:doi>
	<prism:startingPage>253</prism:startingPage>
		<prism:endingPage>274</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Synthesis, Multinuclear NMR Characterization and Dynamic Property of Organic–Inorganic Hybrid Electrolyte Membrane Based on Alkoxysilane and Poly(oxyalkylene) Diamine]]></dc:title>
    <dc:date>2012-06-13</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020253</dc:identifier>
    	<dc:creator>Diganta Saikia</dc:creator>
		<dc:creator>Yu-Chi Pan</dc:creator>
		<dc:creator>Hsien-Ming Kao</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/237">
	<title><![CDATA[Membranes, Vol. 2, Pages 237-252: Impedance Spectroscopic Investigation of Proton Conductivity in Nafion Using Transient Electrochemical Atomic Force Microscopy (AFM)]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/237</link>
	<description>Spatially resolved impedance spectroscopy of a Nafion polyelectrolyte membrane is performed employing a conductive and Pt-coated tip of an atomic force microscope as a point-like contact and electrode. The experiment is conducted by perturbing the system by a rectangular voltage step and measuring the incurred current, followed by Fourier transformation and plotting the impedance against the frequency in a conventional Bode diagram. To test the potential and limitations of this novel method, we present a feasibility study using an identical hydrogen atmosphere at a well-defined relative humidity on both sides of the membrane. It is demonstrated that good quality impedance spectra are obtained in a frequency range of 0.2–1,000 Hz. The extracted polarization curves exhibit a maximum current which cannot be explained by typical diffusion effects. Simulation based on equivalent circuits requires a Nernst element for restricted diffusion in the membrane which suggests that this effect is based on the potential dependence of the electrolyte resistance in the high overpotential region.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-06-06</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2020237</prism:doi>
	<prism:startingPage>237</prism:startingPage>
		<prism:endingPage>252</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Impedance Spectroscopic Investigation of Proton Conductivity in Nafion Using Transient Electrochemical Atomic Force Microscopy (AFM)]]></dc:title>
    <dc:date>2012-06-06</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020237</dc:identifier>
    	<dc:creator>Steffen Hink</dc:creator>
		<dc:creator>Norbert Wagner</dc:creator>
		<dc:creator>Wolfgang G. Bessler</dc:creator>
		<dc:creator>Emil Roduner</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/228">
	<title><![CDATA[Membranes, Vol. 2, Pages 228-236: Comparison of Polytetrafluoroethylene Flat-Sheet Membranes with Different Pore Sizes in Application to Submerged Membrane Bioreactor]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/228</link>
	<description>This study focused on phase separation of activated sludge mixed liquor by flat-sheet membranes of polytetrafluoroethylene (PTFE). A 20 liter working volume lab-scale MBR incorporating immersed PTFE flat-sheet membrane modules with different pore sizes (0.3, 0.5 and 1.0 μm) was operated for 19 days treating a synthetic wastewater. The experiment was interrupted twice at days 5 and 13 when the modules were removed and cleaned physically and chemically in sequence. The pure water permeate flux of each membrane module was measured before and after each cleaning step to calculate membrane resistances. Results showed that fouling of membrane modules with 0.3 μm pore size was more rapid than other membrane modules with different pore sizes (0.5 and 1.0 μm). On the other hand, it was not clear whether fouling of the 0.5 μm membrane module was more severe than that of the 1.0 μm membrane module. This was partly because of the membrane condition after chemical cleaning, which seemed to determine the fouling of those modules over the next period. When irreversible resistance (Ri) i.e., differences in membrane resistance before use and after chemical cleaning was high, the transmembrane pressure increased quickly during the next period irrespective of membrane pore size.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-06-01</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2020228</prism:doi>
	<prism:startingPage>228</prism:startingPage>
		<prism:endingPage>236</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Comparison of Polytetrafluoroethylene Flat-Sheet Membranes with Different Pore Sizes in Application to Submerged Membrane Bioreactor]]></dc:title>
    <dc:date>2012-06-01</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020228</dc:identifier>
    	<dc:creator>Tadashi Nittami</dc:creator>
		<dc:creator>Tetsuo Hitomi</dc:creator>
		<dc:creator>Kanji Matsumoto</dc:creator>
		<dc:creator>Kazuho Nakamura</dc:creator>
		<dc:creator>Takaharu Ikeda</dc:creator>
		<dc:creator>Yoshihiro Setoguchi</dc:creator>
		<dc:creator>Manabu Motoori</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/216">
	<title><![CDATA[Membranes, Vol. 2, Pages 216-227: Oxygen Selective Membranes for Li-Air (O2) Batteries]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/216</link>
	<description>Lithium-air (Li-air) batteries have a much higher theoretical energy density than conventional lithium batteries and other metal air batteries, so they are being developed for applications that require long life. Water vapor from air must be prevented from corroding the lithium (Li) metal negative electrode during discharge under ambient conditions, i.e., in humid air. One method of protecting the Li metal from corrosion is to use an oxygen selective membrane (OSM) that allows oxygen into the cell while stopping or slowing the ingress of water vapor. The desired properties and some potential materials for OSMs for Li-air batteries are discussed and the literature is reviewed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-05-11</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2020216</prism:doi>
	<prism:startingPage>216</prism:startingPage>
		<prism:endingPage>227</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Oxygen Selective Membranes for Li-Air (O2) Batteries]]></dc:title>
    <dc:date>2012-05-11</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020216</dc:identifier>
    	<dc:creator>Owen Crowther</dc:creator>
		<dc:creator>Mark Salomon</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/214">
	<title><![CDATA[Membranes, Vol. 2, Pages 214-215: Correction: Self-Assembling Peptide Surfactants A6K and A6D Adopt a-Helical Structures Useful for Membrane Protein Stabilization. Membranes 2011, 1, 314-326]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/214</link>
	<description>We would like to request a correction to the author listing. The following changes should be made in respect to the original publication of this article [1]. [...]</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-05-02</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Correction</prism:section>
	<prism:doi>10.3390/membranes2020214</prism:doi>
	<prism:startingPage>214</prism:startingPage>
		<prism:endingPage>215</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Correction: Self-Assembling Peptide Surfactants A6K and A6D Adopt a-Helical Structures Useful for Membrane Protein Stabilization. Membranes 2011, 1, 314-326]]></dc:title>
    <dc:date>2012-05-02</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020214</dc:identifier>
    	<dc:creator>Kamila Oglęcka</dc:creator>
		<dc:creator>Furen Zhuang</dc:creator>
		<dc:creator>Charlotte A. E. Hauser</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/2/198">
	<title><![CDATA[Membranes, Vol. 2, Pages 198-213: Immobilization of Mucor miehei Lipase onto Macroporous Aminated Polyethersulfone Membrane for Enzymatic Reactions]]></title>
	<link>http://www.mdpi.com/2077-0375/2/2/198</link>
	<description>Immobilization of enzymes is one of the most promising methods in enzyme performance enhancement, including stability, recovery, and reusability. However, investigation of suitable solid support in enzyme immobilization is still a scientific challenge. Polyethersulfone (PES) and aminated PES (PES–NH2) were successfully synthesized as novel materials for immobilization. Membranes with various pore sizes (from 10–600 nm) based on synthesized PES and PES–NH2 polymers were successfully fabricated to be applied as bioreactors to increase the immobilized lipase performances. The influence of pore sizes, concentration of additives, and the functional groups that are attached on the PES backbone on enzyme loading and enzyme activity was studied. The largest enzyme loading was obtained by Mucor miehei lipase immobilized onto a PES–NH2 membrane composed of 10% of PES–NH2, 8% of dibutyl phthalate (DBP), and 5% of polyethylene glycol (PEG) (872.62 µg/cm2). Hydrolytic activity of the immobilized lipases indicated that the activities of biocatalysts are not significantly decreased by immobilization. From the reusability test, the lipase immobilized onto PES–NH2 showed a better constancy than the lipase immobilized onto PES (the percent recovery of the activity of the lipases immobilized onto PES–NH2 and PES are 97.16% and 95.37%, respectively), which indicates that this novel material has the potential to be developed as a bioreactor for enzymatic reactions.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-04-12</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2020198</prism:doi>
	<prism:startingPage>198</prism:startingPage>
		<prism:endingPage>213</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Immobilization of Mucor miehei Lipase onto Macroporous Aminated Polyethersulfone Membrane for Enzymatic Reactions]]></dc:title>
    <dc:date>2012-04-12</dc:date>
	<dc:identifier>doi: 10.3390/membranes2020198</dc:identifier>
    	<dc:creator>Nurrahmi Handayani</dc:creator>
		<dc:creator>Katja Loos</dc:creator>
		<dc:creator>Deana Wahyuningrum</dc:creator>
		<dc:creator> Buchari</dc:creator>
		<dc:creator>Muhammad Ali Zulfikar</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/1/134">
	<title><![CDATA[Membranes, Vol. 2, Pages 134-197: Light Responsive Polymer Membranes: A Review]]></title>
	<link>http://www.mdpi.com/2077-0375/2/1/134</link>
	<description>In recent years, stimuli responsive materials have gained significant attention in membrane separation processes due to their ability to change specific properties in response to small external stimuli, such as light, pH, temperature, ionic strength, pressure, magnetic field, antigen, chemical composition, and so on. In this review, we briefly report recent progresses in light-driven materials and membranes. Photo-switching mechanisms, valved-membrane fabrication and light-driven properties are examined. Advances and perspectives of light responsive polymer membranes in biotechnology, chemistry and biology areas are discussed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-03-02</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2010134</prism:doi>
	<prism:startingPage>134</prism:startingPage>
		<prism:endingPage>197</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Light Responsive Polymer Membranes: A Review]]></dc:title>
    <dc:date>2012-03-02</dc:date>
	<dc:identifier>doi: 10.3390/membranes2010134</dc:identifier>
    	<dc:creator>Fiore Pasquale Nicoletta</dc:creator>
		<dc:creator>Daniela Cupelli</dc:creator>
		<dc:creator>Patrizia Formoso</dc:creator>
		<dc:creator>Giovanni De Filpo</dc:creator>
		<dc:creator>Valentina Colella</dc:creator>
		<dc:creator>Annarosa Gugliuzza</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/1/118">
	<title><![CDATA[Membranes, Vol. 2, Pages 118-133: Mechanisms of Membrane Curvature Generation in Membrane Traffic]]></title>
	<link>http://www.mdpi.com/2077-0375/2/1/118</link>
	<description>During the vesicular trafficking process, cellular membranes undergo dynamic morphological changes, in particular at the vesicle generation and fusion steps. Changes in membrane shape are regulated by small GTPases, coat proteins and other accessory proteins, such as BAR domain-containing proteins. In addition, membrane deformation entails changes in the lipid composition as well as asymmetric distribution of lipids over the two leaflets of the membrane bilayer. Given that P4-ATPases, which catalyze unidirectional flipping of lipid molecules from the exoplasmic to the cytoplasmic leaflets of the bilayer, are crucial for the trafficking of proteins in the secretory and endocytic pathways, changes in the lipid composition are involved in the vesicular trafficking process. Membrane remodeling is under complex regulation that involves the composition and distribution of lipids as well as assembly of proteins.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-02-29</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2010118</prism:doi>
	<prism:startingPage>118</prism:startingPage>
		<prism:endingPage>133</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Mechanisms of Membrane Curvature Generation in Membrane Traffic]]></dc:title>
    <dc:date>2012-02-29</dc:date>
	<dc:identifier>doi: 10.3390/membranes2010118</dc:identifier>
    	<dc:creator>Hye-Won Shin</dc:creator>
		<dc:creator>Hiroyuki Takatsu</dc:creator>
		<dc:creator>Kazuhisa Nakayama</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/1/91">
	<title><![CDATA[Membranes, Vol. 2, Pages 91-117: The BAR Domain Superfamily Proteins from Subcellular Structures to Human Diseases]]></title>
	<link>http://www.mdpi.com/2077-0375/2/1/91</link>
	<description>Eukaryotic cells have complicated membrane systems. The outermost plasma membrane contains various substructures, such as invaginations and protrusions, which are involved in endocytosis and cell migration. Moreover, the intracellular membrane compartments, such as autophagosomes and endosomes, are essential for cellular viability. The Bin-Amphiphysin-Rvs167 (BAR) domain superfamily proteins are important players in membrane remodeling through their structurally determined membrane binding surfaces. A variety of BAR domain superfamily proteins exist, and each family member appears to be involved in the formation of certain subcellular structures or intracellular membrane compartments. Most of the BAR domain superfamily proteins contain SH3 domains, which bind to the membrane scission molecule, dynamin, as well as the actin regulatory WASP/WAVE proteins and several signal transduction molecules, providing possible links between the membrane and the cytoskeleton or other machineries. In this review, we summarize the current information about each BAR superfamily protein with an SH3 domain(s). The involvement of BAR domain superfamily proteins in various diseases is also discussed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-02-27</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2010091</prism:doi>
	<prism:startingPage>91</prism:startingPage>
		<prism:endingPage>117</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[The BAR Domain Superfamily Proteins from Subcellular Structures to Human Diseases]]></dc:title>
    <dc:date>2012-02-27</dc:date>
	<dc:identifier>doi: 10.3390/membranes2010091</dc:identifier>
    	<dc:creator>Fatemeh Safari</dc:creator>
		<dc:creator>Shiro Suetsugu</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/1/70">
	<title><![CDATA[Membranes, Vol. 2, Pages 70-90: Development of Hydrogels and Biomimetic Regulators as Tissue Engineering Scaffolds]]></title>
	<link>http://www.mdpi.com/2077-0375/2/1/70</link>
	<description>This paper reviews major research and development issues relating to hydrogels as scaffolds for tissue engineering, the article starts with a brief introduction of tissue engineering and hydrogels as extracellular matrix mimics, followed by a description of the various types of hydrogels and preparation methods, before a discussion of the physical and chemical properties that are important to their application. There follows a short comment on the trends of future research and development. Throughout the discussion there is an emphasis on the genetic understanding of bone tissue engineering application.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-02-14</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2010070</prism:doi>
	<prism:startingPage>70</prism:startingPage>
		<prism:endingPage>90</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Development of Hydrogels and Biomimetic Regulators as Tissue Engineering Scaffolds]]></dc:title>
    <dc:date>2012-02-14</dc:date>
	<dc:identifier>doi: 10.3390/membranes2010070</dc:identifier>
    	<dc:creator>Junbin Shi</dc:creator>
		<dc:creator>Malcolm M. Q. Xing</dc:creator>
		<dc:creator>Wen Zhong</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/1/40">
	<title><![CDATA[Membranes, Vol. 2, Pages 40-69: Thin Hydrogel Films for Optical Biosensor Applications]]></title>
	<link>http://www.mdpi.com/2077-0375/2/1/40</link>
	<description>Hydrogel materials consisting of water-swollen polymer networks exhibit a large number of specific properties highly attractive for a variety of optical biosensor applications. This properties profile embraces the aqueous swelling medium as the basis of biocompatibility, non-fouling behavior, and being not cell toxic, while providing high optical quality and transparency. The present review focuses on some of the most interesting aspects of surface-attached hydrogel films as active binding matrices in optical biosensors based on surface plasmon resonance and optical waveguide mode spectroscopy. In particular, the chemical nature, specific properties, and applications of such hydrogel surface architectures for highly sensitive affinity biosensors based on evanescent wave optics are discussed. The specific class of responsive hydrogel systems, which can change their physical state in response to externally applied stimuli, have found large interest as sophisticated materials that provide a complex behavior to hydrogel-based sensing devices.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-02-08</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2010040</prism:doi>
	<prism:startingPage>40</prism:startingPage>
		<prism:endingPage>69</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Thin Hydrogel Films for Optical Biosensor Applications]]></dc:title>
    <dc:date>2012-02-08</dc:date>
	<dc:identifier>doi: 10.3390/membranes2010040</dc:identifier>
    	<dc:creator>Anca Mateescu</dc:creator>
		<dc:creator>Yi Wang</dc:creator>
		<dc:creator>Jakub Dostalek</dc:creator>
		<dc:creator>Ulrich Jonas</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/1/16">
	<title><![CDATA[Membranes, Vol. 2, Pages 16-39: Stimuli Responsive Ionogels for Sensing Applications—An Overview]]></title>
	<link>http://www.mdpi.com/2077-0375/2/1/16</link>
	<description>This overview aims to summarize the existing potential of “Ionogels” as a platform to develop stimuli responsive materials. Ionogels are a class of materials that contain an Ionic Liquid (IL) confined within a polymer matrix. Recently defined as “a solid interconnected network spreading throughout a liquid phase”, the ionogel therefore combines the properties of both its solid and liquid components. ILs are low melting salts that exist as liquids composed entirely of cations and anions at or around 100 °C. Important physical properties of these liquids such as viscosity, density, melting point and conductivity can be altered to suit a purpose by choice of the cation/anion. Here we provide an overview to highlight the literature thus far, detailing the encapsulation of IL and responsive materials within these polymeric structures. Exciting applications in the areas of optical and electrochemical sensing, solid state electrolytes and actuating materials shall be discussed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2012-02-07</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes2010016</prism:doi>
	<prism:startingPage>16</prism:startingPage>
		<prism:endingPage>39</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Stimuli Responsive Ionogels for Sensing Applications—An Overview]]></dc:title>
    <dc:date>2012-02-07</dc:date>
	<dc:identifier>doi: 10.3390/membranes2010016</dc:identifier>
    	<dc:creator>Andrew Kavanagh</dc:creator>
		<dc:creator>Robert Byrne</dc:creator>
		<dc:creator>Dermot Diamond</dc:creator>
		<dc:creator>Kevin J. Fraser</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/2/1/1">
	<title><![CDATA[Membranes, Vol. 2, Pages 1-15: Physical Characterization of Mouse Deep Vein Thrombosis Derived Microparticles by Differential Filtration with Nanopore Filters]]></title>
	<link>http://www.mdpi.com/2077-0375/2/1/1</link>
	<description>With the objective of making advancements in the area of pro-thrombotic microparticle characterization in cardiovascular biology, we present a novel method to separate blood circulating microparticles using a membrane-based, nanopore filtration system. In this qualitative study, electron microscopy observations of these pro-thrombotic mouse microparticles, as well as mouse platelets and leukocytes obtained using a mouse inferior vena cava ligation model of deep-vein thrombosis are presented. In particular, we present mouse microparticle morphology and microstructure using SEM and TEM indicating that they appear to be mostly spherical with diameters in the 100 to 350 nm range. The nanopore filtration technique presented is focused on the development of novel methodologies to isolate and characterize blood circulating microparticles that can be used in conjunction with other methodologies. We believe that determination of microparticle size and structure is a critical step for the development of reliable assays with clinical or research application in thrombosis and it will contribute to the field of nanomedicine in thrombosis.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-12-27</prism:publicationDate>
	<prism:volume>2</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes2010001</prism:doi>
	<prism:startingPage>1</prism:startingPage>
		<prism:endingPage>15</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Physical Characterization of Mouse Deep Vein Thrombosis Derived Microparticles by Differential Filtration with Nanopore Filters]]></dc:title>
    <dc:date>2011-12-27</dc:date>
	<dc:identifier>doi: 10.3390/membranes2010001</dc:identifier>
    	<dc:creator>Antonio Peramo</dc:creator>
		<dc:creator>Jose A. Diaz</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/394">
	<title><![CDATA[Membranes, Vol. 1, Pages 394-411: Membrane Compartment Occupied by Can1 (MCC) and Eisosome Subdomains of the Fungal Plasma Membrane]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/394</link>
	<description>Studies on the budding yeast Saccharomyces cerevisiae have revealed that fungal plasma membranes are organized into different subdomains. One new domain termed MCC/eisosomes consists of stable punctate patches that are distinct from lipid rafts. The MCC/eisosome domains correspond to furrows in the plasma membrane that are about 300 nm long and 50 nm deep. The MCC portion includes integral membrane proteins, such as the tetraspanners Sur7 and Nce102. The adjacent eisosome includes proteins that are peripherally associated with the membrane, including the BAR domains proteins Pil1 and Lsp1 that are thought to promote membrane curvature. Genetic analysis of the MCC/eisosome components indicates these domains broadly affect overall plasma membrane organization. The mechanisms regulating the formation of MCC/eisosomes in model organisms will be reviewed as well as the role of these plasma membrane domains in fungal pathogenesis and response to antifungal drugs.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-12-13</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes1040394</prism:doi>
	<prism:startingPage>394</prism:startingPage>
		<prism:endingPage>411</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Membrane Compartment Occupied by Can1 (MCC) and Eisosome Subdomains of the Fungal Plasma Membrane]]></dc:title>
    <dc:date>2011-12-13</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040394</dc:identifier>
    	<dc:creator>Lois M. Douglas</dc:creator>
		<dc:creator>Hong X. Wang</dc:creator>
		<dc:creator>Lifang Li</dc:creator>
		<dc:creator>James B. Konopka</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/354">
	<title><![CDATA[Membranes, Vol. 1, Pages 354-393: The Role of the Transmembrane RING Finger Proteins in Cellular and Organelle Function]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/354</link>
	<description>A large number of RING finger (RNF) proteins are present in eukaryotic cells and the majority of them are believed to act as E3 ubiquitin ligases. In humans, 49 RNF proteins are predicted to contain transmembrane domains, several of which are specifically localized to membrane compartments in the secretory and endocytic pathways, as well as to mitochondria and peroxisomes. They are thought to be molecular regulators of the organization and integrity of the functions and dynamic architecture of cellular membrane and membranous organelles. Emerging evidence has suggested that transmembrane RNF proteins control the stability, trafficking and activity of proteins that are involved in many aspects of cellular and physiological processes. This review summarizes the current knowledge of mammalian transmembrane RNF proteins, focusing on their roles and significance.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-12-09</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes1040354</prism:doi>
	<prism:startingPage>354</prism:startingPage>
		<prism:endingPage>393</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[The Role of the Transmembrane RING Finger Proteins in Cellular and Organelle Function]]></dc:title>
    <dc:date>2011-12-09</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040354</dc:identifier>
    	<dc:creator>Nobuhiro Nakamura</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/345">
	<title><![CDATA[Membranes, Vol. 1, Pages 345-353: Effect of Counter Electrode in Electroformation of Giant Vesicles]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/345</link>
	<description>Electroformation of cell-sized lipid membrane vesicles (giant vesicles, GVs), from egg yolk phosphatidylcholine, was examined varying the shape of the counter electrode. Instead of a planar ITO (indium tin oxide) electrode commonly used, platinum wire mesh was employed as a counter electrode facing lipid deposit on a planar formation electrode. The modification did not significantly alter GV formation, and many GVs of 30–50 µm, some as large as 100 µm, formed as with the standard setup, indicating that a counter electrode does not have to be a complete plane. When the counter electrode was reduced to a set of two parallel platinum wires, GV formation deteriorated. Some GVs formed, but only in close proximity to the counter electrode. Lower electric voltage with this setup no longer yielded GVs. Instead, a large onion-like multilamellar structure was observed. The deteriorated GV formation and the formation of a multilamellar structure seemed to indicate the weakened effect of the electric field on lipid deposit due to insufficient coverage with a small counter electrode. Irregular membranous objects formed by spontaneous swelling of lipid without electric voltage gradually turned into multilamellar structure upon following application of voltage. No particular enhancement of GV formation was observed when lipid deposit on a wire formation electrode was used in combination with a large planar counter electrode.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-11-24</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Technical Note</prism:section>
	<prism:doi>10.3390/membranes1040345</prism:doi>
	<prism:startingPage>345</prism:startingPage>
		<prism:endingPage>353</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Effect of Counter Electrode in Electroformation of Giant Vesicles]]></dc:title>
    <dc:date>2011-11-24</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040345</dc:identifier>
    	<dc:creator>Yukihisa Okumura</dc:creator>
		<dc:creator>Shuuhei Oana</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/327">
	<title><![CDATA[Membranes, Vol. 1, Pages 327-344: Membrane Bioreactor Technology for the Development of Functional Materials from Sea-Food Processing Wastes and Their Potential Health Benefits]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/327</link>
	<description>Sea-food processing wastes and underutilized species of fish are a potential source of functional and bioactive compounds. A large number of bioactive substances can be produced through enzyme-mediated hydrolysis. Suitable enzymes and the appropriate bioreactor system are needed to incubate the waste materials. Membrane separation is a useful technique to extract, concentrate, separate or fractionate the compounds. The use of membrane bioreactors to integrate a reaction vessel with a membrane separation unit is emerging as a beneficial method for producing bioactive materials such as peptides, chitooligosaccharides and polyunsaturated fatty acids from diverse seafood-related wastes. These bioactive compounds from membrane bioreactor technology show diverse biological activities such as antihypertensive, antimicrobial, antitumor, anticoagulant, antioxidant and radical scavenging properties. This review discusses the application of membrane bioreactor technology for the production of value-added functional materials from sea-food processing wastes and their biological activities in relation to health benefits.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-10-25</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes1040327</prism:doi>
	<prism:startingPage>327</prism:startingPage>
		<prism:endingPage>344</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Membrane Bioreactor Technology for the Development of Functional Materials from Sea-Food Processing Wastes and Their Potential Health Benefits]]></dc:title>
    <dc:date>2011-10-25</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040327</dc:identifier>
    	<dc:creator>Se-Kwon Kim</dc:creator>
		<dc:creator>Mahinda Senevirathne</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/314">
	<title><![CDATA[Membranes, Vol. 1, Pages 314-326: Self-Assembling Peptide Surfactants A6K and A6D Adopt a-Helical Structures Useful for Membrane Protein Stabilization]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/314</link>
	<description>Elucidation of membrane protein structures have been greatly hampered by difficulties in producing adequately large quantities of the functional protein and stabilizing them. A6D and A6K are promising solutions to the problem and have recently been used for the rapid production of membrane-bound G protein-coupled receptors (GPCRs). We propose that despite their short lengths, these peptides can adopt α-helical structures through interactions with micelles formed by the peptides themselves. These α-helices are then able to stabilize α-helical motifs which many membrane proteins contain. We also show that A6D and A6K can form β-sheets and appear as weak hydrogels at sufficiently high concentrations. Furthermore, A6D and A6K together in sodium dodecyl sulfate (SDS) can form expected β-sheet structures via a surprising α-helical intermediate.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-10-21</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1040314</prism:doi>
	<prism:startingPage>314</prism:startingPage>
		<prism:endingPage>326</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Self-Assembling Peptide Surfactants A6K and A6D Adopt a-Helical Structures Useful for Membrane Protein Stabilization]]></dc:title>
    <dc:date>2011-10-21</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040314</dc:identifier>
    	<dc:creator>Furen Zhuang</dc:creator>
		<dc:creator>Kamila Oglęcka</dc:creator>
		<dc:creator>Charlotte A. E. Hauser</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/299">
	<title><![CDATA[Membranes, Vol. 1, Pages 299-313: Liquid Phase Micro-Extraction of Linear Alkylbenzene Sulfonate Anionic Surfactants in Aqueous Samples]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/299</link>
	<description>Hollow fiber liquid phase micro-extraction (LPME) of linear alkylbenzene sulfonates (LAS) from aqueous samples was studied. Ion pair extraction of C10, C11, C12 and C13 homologues was facilitated with trihexylamine as ion-pairing agent, using di-n-hexylether as solvent for the supported liquid membrane (SLM). Effects of extraction time, acceptor buffer concentration, stirring speed, sample volume, NaCl and humic acids were studied. At 10–50 µg L−1 linear R2-coefficients were 0.99 for C10 and C11 and 0.96 for C12. RSD was typically ~15%. Three observations were especially made. Firstly, LPME for these analytes was unusually slow with maximum enrichment observed after 15–24 h (depending on sample volume). Secondly, the enrichment depended on LAS sample concentration with 35–150 times enrichment below ~150 µg L−1 and 1850–4400 times enrichment at 1 mg L−1. Thirdly, lower homologues were enriched more than higher homologues at low sample concentrations, with reversed conditions at higher concentrations. These observations may be due to the fact that LAS and the amine counter ion themselves influence the mass transfer at the water-SLM interface. The observations on LPME of LAS may aid in LPME application to other compounds with surfactant properties or in surfactant enhanced membrane extraction of other compounds.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-10-13</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1040299</prism:doi>
	<prism:startingPage>299</prism:startingPage>
		<prism:endingPage>313</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Liquid Phase Micro-Extraction of Linear Alkylbenzene Sulfonate Anionic Surfactants in Aqueous Samples]]></dc:title>
    <dc:date>2011-10-13</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040299</dc:identifier>
    	<dc:creator>Niklas Larsson</dc:creator>
		<dc:creator>Paulina Otrembska</dc:creator>
		<dc:creator>Mercedes Villar</dc:creator>
		<dc:creator>Jan Åke Jönsson</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/275">
	<title><![CDATA[Membranes, Vol. 1, Pages 275-298: Fabrication and Biocompatibility of Electrospun Silk Biocomposites]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/275</link>
	<description>Silk fibroin has attracted great interest in tissue engineering because of its outstanding biocompatibility, biodegradability and minimal inflammatory reaction. In this study, two kinds of biocomposites based on regenerated silk fibroin are fabricated by electrospinning and post-treatment processes, respectively. Firstly, regenerated silk fibroin/tetramethoxysilane (TMOS) hybrid nanofibers with high hydrophilicity are prepared, which is superior for fibroblast attachment. The electrospinning process causes adjacent fibers to ‘weld’ at contact points, which can be proved by scanning electron microscope (SEM). The water contact angle of silk/tetramethoxysilane (TMOS) composites shows a sharper decrease than pure regenerated silk fibroin nanofiber, which has a great effect on the early stage of cell attachment behavior. Secondly, a novel tissue engineering scaffold material based on electrospun silk fibroin/nano-hydroxyapatite (nHA) biocomposites is prepared by means of an effective calcium and phosphate (Ca–P) alternate soaking method. nHA is successfully produced on regenerated silk fibroin nanofiber within several min without any pre-treatments. The osteoblastic activities of this novel nanofibrous biocomposites are also investigated by employing osteoblastic-like MC3T3-E1 cell line. The cell functionality such as alkaline phosphatase (ALP) activity is ameliorated on mineralized silk nanofibers. All these results indicate that this silk/nHA biocomposite scaffold material may be a promising biomaterial for bone tissue engineering.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-10-10</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1040275</prism:doi>
	<prism:startingPage>275</prism:startingPage>
		<prism:endingPage>298</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Fabrication and Biocompatibility of Electrospun Silk Biocomposites]]></dc:title>
    <dc:date>2011-10-10</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040275</dc:identifier>
    	<dc:creator>Kai Wei</dc:creator>
		<dc:creator>Byoung-Suhk Kim</dc:creator>
		<dc:creator>Ick-Soo Kim</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/4/265">
	<title><![CDATA[Membranes, Vol. 1, Pages 265-274: Formation of Oligovesicular Vesicles by Micromanipulation]]></title>
	<link>http://www.mdpi.com/2077-0375/1/4/265</link>
	<description>Cell-sized lipid bilayer membrane vesicles (giant vesicles, GVs) or semi-vesicles were formed from egg yolk phosphatidylcholine on a platinum electrode under applied electric voltage by electroformation. Micromanipulation of the semi-vesicle by first pressing its membrane with a glass microneedle and then withdrawing the needle left a GV in the interior of the vesicle. During the process, an aqueous solution of Ficoll that filled the needle was introduced into the newly formed inner vesicle and remained encapsulated. Approximately 50% of attempted micromanipulation resulted in the formation of an inner daughter vesicle, “microvesiculation”. By repeating the microvesiculation process, multiple inner GVs could be formed in a single parent semi-vesicle. A semi-vesicle with inner GVs could be detached from the electrode by scraping with a microneedle, yielding an oligovesicular vesicle (OVV) with desired inner aqueous contents. Microvesiculation of a GV held on the tip of a glass micropipette was also possible, and this also produced an OVV. Breaking the membrane of the parent semi-vesicle by micromanipulation with a glass needle after microvesiculation, released the inner GVs. This protocol may be used for controlled formation of GVs with desired contents.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-09-26</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1040265</prism:doi>
	<prism:startingPage>265</prism:startingPage>
		<prism:endingPage>274</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Formation of Oligovesicular Vesicles by Micromanipulation]]></dc:title>
    <dc:date>2011-09-26</dc:date>
	<dc:identifier>doi: 10.3390/membranes1040265</dc:identifier>
    	<dc:creator>Yukihisa Okumura</dc:creator>
		<dc:creator>Tohru Ohmiya</dc:creator>
		<dc:creator>Toshiki Yamazaki</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/3/249">
	<title><![CDATA[Membranes, Vol. 1, Pages 249-264: Functionality in Electrospun Nanofibrous Membranes Based on Fiber’s Size, Surface Area, and Molecular Orientation]]></title>
	<link>http://www.mdpi.com/2077-0375/1/3/249</link>
	<description>Electrospinning is a versatile method for forming continuous thin fibers based on an electrohydrodynamic process. This method has the following advantages: (i) the ability to produce thin fibers with diameters in the micrometer and nanometer ranges; (ii) one-step forming of the two- or three-dimensional nanofiber network assemblies (nanofibrous membranes); and (iii) applicability for a broad spectrum of molecules, such as synthetic and biological polymers and polymerless sol-gel systems. Electrospun nanofibrous membranes have received significant attention in terms of their practical applications. The major advantages of nanofibers or nanofibrous membranes are the functionalities based on their nanoscaled-size, highly specific surface area, and highly molecular orientation. These functionalities of the nanofibrous membranes can be controlled by their fiber diameter, surface chemistry and topology, and internal structure of the nanofibers. This report focuses on our studies and describes fundamental aspects and applications of electrospun nanofibrous membranes.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-08-26</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes1030249</prism:doi>
	<prism:startingPage>249</prism:startingPage>
		<prism:endingPage>264</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Functionality in Electrospun Nanofibrous Membranes Based on Fiber’s Size, Surface Area, and Molecular Orientation]]></dc:title>
    <dc:date>2011-08-26</dc:date>
	<dc:identifier>doi: 10.3390/membranes1030249</dc:identifier>
    	<dc:creator>Hidetoshi Matsumoto</dc:creator>
		<dc:creator>Akihiko Tanioka</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/3/232">
	<title><![CDATA[Membranes, Vol. 1, Pages 232-248: Recent Trends in Nanofibrous Membranes and Their Suitability for Air and Water Filtrations]]></title>
	<link>http://www.mdpi.com/2077-0375/1/3/232</link>
	<description>In recent decades, engineered membranes have become a viable separation technology for a wide range of applications in environmental, food and biomedical fields. Membranes are now competitive compared to conventional techniques such as adsorption, ion exchangers and sand filters. The main advantage of membrane technology is the fact that it works without the addition of any chemicals, with relatively high efficiency and low energy consumption with well arranged process conductions. Hence they are widely utilized in biotechnology, food and drink manufacturing, air filtration and medical uses such as dialysis for kidney failure patients. Membranes from nanofibrous materials possess high surface area to volume ratio, fine tunable pore sizes and their ease of preparation prompted both industry and academic researchers to study their use in many applications. In this paper, modern concepts and current research progress on various nanofibrous membranes, such as water and air filtration media, are presented.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-08-22</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Review</prism:section>
	<prism:doi>10.3390/membranes1030232</prism:doi>
	<prism:startingPage>232</prism:startingPage>
		<prism:endingPage>248</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Recent Trends in Nanofibrous Membranes and Their Suitability for Air and Water Filtrations]]></dc:title>
    <dc:date>2011-08-22</dc:date>
	<dc:identifier>doi: 10.3390/membranes1030232</dc:identifier>
    	<dc:creator>Ramalingam Balamurugan</dc:creator>
		<dc:creator>Subramanian Sundarrajan</dc:creator>
		<dc:creator>Seeram Ramakrishna</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/3/217">
	<title><![CDATA[Membranes, Vol. 1, Pages 217-231: Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device]]></title>
	<link>http://www.mdpi.com/2077-0375/1/3/217</link>
	<description>Nickel (II) preconcentration and speciation analysis using a hollow fiber supported liquid membrane (HFSLM) device was studied. A counterflow of protons coupled to complexation with formate provided the driving force of the process, while Kelex 100 was employed as carrier. The influence of variables related to module configuration (acceptor pH and carrier concentration) and to the sample properties (donor pH) on the preconcentration factor, E, was simultaneously studied and optimized using a 3 factor Doehlert matrix response surface methodology. The effect of metal concentration was studied as well. Preconcentration factors as high as 4240 were observed  depending on the values of the different variables. The effects of the presence of inorganic anions (NO2-, SO42-, Cl-, NO3-, CO32-, CN-) and dissolved organic matter (DOM) in the form of humic acids were additionally considered in order to carry out a speciation analysis study. Nickel preconcentration was observed to be independent of both effects, except when cyanide was present in the donor phase. A characterization of the transport regime was performed through the analysis of the dependence of E on the temperature. E increases with the increase in temperature according to the equation E(K) = -8617.3 + 30.5T with an activation energy of 56.7 kJ mol-1 suggesting a kinetic-controlled regime. Sample depletion ranged from 12 to 1.2% depending on the volume of the donor phase (100 to 1000 mL, respectively).</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-08-18</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1030217</prism:doi>
	<prism:startingPage>217</prism:startingPage>
		<prism:endingPage>231</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device]]></dc:title>
    <dc:date>2011-08-18</dc:date>
	<dc:identifier>doi: 10.3390/membranes1030217</dc:identifier>
    	<dc:creator>Ana Nelly Bautista-Flores</dc:creator>
		<dc:creator>Eduardo Rodríguez De San Miguel</dc:creator>
		<dc:creator>Josefina de Gyves</dc:creator>
		<dc:creator>Jan Åke Jönsson</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/3/195">
	<title><![CDATA[Membranes, Vol. 1, Pages 195-216: Monitoring Protein Fouling on Polymeric Membranes Using Ultrasonic Frequency-Domain Reflectometry]]></title>
	<link>http://www.mdpi.com/2077-0375/1/3/195</link>
	<description>Novel signal-processing protocols were used to extend the in situ sensitivity of ultrasonic frequency-domain reflectometry (UFDR) for real-time monitoring of microfiltration (MF) membrane fouling during protein purification. Different commercial membrane materials, with a nominal pore size of 0.2 µm, were challenged using bovine serum albumin (BSA) and amylase as model proteins. Fouling induced by these proteins was observed in flat-sheet membrane filtration cells operating in a laminar cross-flow regime. The detection of membrane-associated proteins using UFDR was determined by applying rigorous statistical methodology to reflection spectra of ultrasonic signals obtained during membrane fouling. Data suggest that the total power reflected from membrane surfaces changes in response to protein fouling at concentrations as low as 14 μg/cm2, and results indicate that ultrasonic spectra can be leveraged to detect and monitor protein fouling on commercial MF membranes.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-08-10</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1030195</prism:doi>
	<prism:startingPage>195</prism:startingPage>
		<prism:endingPage>216</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Monitoring Protein Fouling on Polymeric Membranes Using Ultrasonic Frequency-Domain Reflectometry]]></dc:title>
    <dc:date>2011-08-10</dc:date>
	<dc:identifier>doi: 10.3390/membranes1030195</dc:identifier>
    	<dc:creator>Elmira Kujundzic</dc:creator>
		<dc:creator>Alan R. Greenberg</dc:creator>
		<dc:creator>Robin Fong</dc:creator>
		<dc:creator>Mark Hernandez</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/3/184">
	<title><![CDATA[Membranes, Vol. 1, Pages 184-194: Electroformation of Giant Vesicles on a Polymer Mesh]]></title>
	<link>http://www.mdpi.com/2077-0375/1/3/184</link>
	<description>Electroformation of cell-sized lipid membrane vesicles (giant vesicles, GVs) from egg yolk phosphatidylcholine under applied electric voltage was examined on a substrate of a polymer mesh placed between two planar indium tin oxide coated glass electrodes. Under appropriate conditions, GVs were formed in good yield on meshes of various polymer materials, namely, hydrophobic poly(propylene), poly(ethylene terephthalate), a carbon fiber/nylon composite, and relatively hydrophilic nylon. Arranging threads in a mesh structure with appropriate openings improved GV formation compared to simply increasing the number of threads. For optimal electroformation of GVs, the size and shape of a mesh opening were crucial. With a too large opening, GV formation deteriorated. When the sides of an opening were partially missing, GV formation did not occur efficiently. With an adequate opening, a deposited lipid solution could fill the opening, and a relatively uniform lipid deposit formed on the surface of threads after evaporation of the solvent. This could supply a sufficient amount of lipids to the opening and also prevent a lipid deposit from becoming too thick for electroformation. As a result, good GV formation was often observed in openings filled with swelled lipid.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-07-15</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1030184</prism:doi>
	<prism:startingPage>184</prism:startingPage>
		<prism:endingPage>194</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Electroformation of Giant Vesicles on a Polymer Mesh]]></dc:title>
    <dc:date>2011-07-15</dc:date>
	<dc:identifier>doi: 10.3390/membranes1030184</dc:identifier>
    	<dc:creator>Yukihisa Okumura</dc:creator>
		<dc:creator>Takuya Sugiyama</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/3/162">
	<title><![CDATA[Membranes, Vol. 1, Pages 162-183: Thinking in Terms of Structure-Activity-Relationships (T-SAR): A Tool to Better Understand Nanofiltration Membranes]]></title>
	<link>http://www.mdpi.com/2077-0375/1/3/162</link>
	<description>A frontier to be conquered in the field of membrane technology is related to the very limited scientific base for the rational and task-specific design of membranes. This is especially true for nanofiltration membranes with properties that are based on several solute-membrane interaction mechanisms. “Thinking in terms of Structure-Activity-Relationships” (T-SAR) is a methodology which applies a systematic analysis of a chemical entity based on its structural formula. However, the analysis become more complex with increasing size of the molecules considered. In this study, T-SAR was combined with classical membrane characterization methods, resulting in a new methodology which allowed us not only to explain membrane characteristics, but also provides evidence for the importance of the chemical structure for separation performance. We demonstrate an application of the combined approach and its potential to discover stereochemistry, molecular interaction potentials, and reactivity of two FilmTec nanofiltration membranes (NF-90 and NF-270). Based on these results, it was possible to predict both properties and performance in the recovery of hydrophobic ionic liquids from aqueous solution.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-07-15</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1030162</prism:doi>
	<prism:startingPage>162</prism:startingPage>
		<prism:endingPage>183</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Thinking in Terms of Structure-Activity-Relationships (T-SAR): A Tool to Better Understand Nanofiltration Membranes]]></dc:title>
    <dc:date>2011-07-15</dc:date>
	<dc:identifier>doi: 10.3390/membranes1030162</dc:identifier>
    	<dc:creator>José F. Fernández</dc:creator>
		<dc:creator>Bernd Jastorff</dc:creator>
		<dc:creator>Reinhold Störmann</dc:creator>
		<dc:creator>Stefan Stolte</dc:creator>
		<dc:creator>Jorg Thöming</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/3/149">
	<title><![CDATA[Membranes, Vol. 1, Pages 149-161: Comparative Composition and Antioxidant Activity of Peptide Fractions Obtained by Ultrafiltration of Egg Yolk Protein Enzymatic Hydrolysates]]></title>
	<link>http://www.mdpi.com/2077-0375/1/3/149</link>
	<description>The objective of the study was to compare the antioxidant activity of two distinct hydrolysates and their peptide fractions prepared by ultrafiltration (UF) using membranes with molecular weight cut-off of 5 and 1 kDa. The hydrolysates were a delipidated egg yolk protein concentrate (EYP) intensively hydrolyzed with a combination of two bacterial proteases, and a phosphoproteins (PPP) extract partially hydrolyzed with trypsin. Antioxidant activity, as determined by the oxygen radical absorbance capacity (ORAC) assay, was low for EYP and PPP hydrolysates with values of 613.1 and 489.2 µM TE×g−1 protein, respectively. UF-fractionation of EYP hydrolysate increased slightly the antioxidant activity in permeate fractions (720.5–867.8 µM TE×g−1 protein). However, ORAC values were increased by more than 3-fold in UF-fractions prepared from PPP hydrolysate, which were enriched in peptides with molecular weight lower than 5 kDa. These UF-fractions were characterized by their lower N/P atomic ratio and higher phosphorus content compared to the same UF-fractions obtained from EYP-TH. They also contained high amounts of His, Met, Leu, and Phe, which are recognized as antioxidant amino acids, but also high content in Lys and Arg which both represent target amino acids of trypsin used for the hydrolysis of PPP.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-07-06</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1030149</prism:doi>
	<prism:startingPage>149</prism:startingPage>
		<prism:endingPage>161</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Comparative Composition and Antioxidant Activity of Peptide Fractions Obtained by Ultrafiltration of Egg Yolk Protein Enzymatic Hydrolysates]]></dc:title>
    <dc:date>2011-07-06</dc:date>
	<dc:identifier>doi: 10.3390/membranes1030149</dc:identifier>
    	<dc:creator>Bertrand P. Chay Pak Ting</dc:creator>
		<dc:creator>Yoshinori Mine</dc:creator>
		<dc:creator>Lekh R. Juneja</dc:creator>
		<dc:creator>Tsutomu Okubo</dc:creator>
		<dc:creator>Sylvie F. Gauthier</dc:creator>
		<dc:creator>Yves Pouliot</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/2/132">
	<title><![CDATA[Membranes, Vol. 1, Pages 132-148: Electrochemical Impedance Spectroscopy—A Simple Method for the Characterization of Polymer Inclusion Membranes Containing Aliquat 336]]></title>
	<link>http://www.mdpi.com/2077-0375/1/2/132</link>
	<description>Electrochemical impedance spectroscopy (EIS) has been used to estimate the non-frequency dependent (static) dielectric constants of base polymers such as poly(vinyl chloride) (PVC), cellulose triacetate (CTA) and polystyrene (PS). Polymer inclusion membranes (PIMs) containing different amounts of PVC or CTA, along with the room temperature ionic liquid Aliquat 336 and plasticizers such as trisbutoxyethyl phosphate (TBEP), dioctyl sebecate (DOS) and 2-nitrophenyloctyl ether (NPOE) have been investigated. In this study, the complex and abstract method of EIS has been applied in a simple and easy to use way, so as to make the method accessible to membrane scientists and engineers who may not possess the detailed knowledge of electrochemistry and interfacial science needed for a rigorous interpretation of EIS results. The EIS data reported herein are internally consistent with a percolation threshold in the dielectric constant at high concentrations of Aliquat 336, which illustrates the suitability of the EIS technique since membrane percolation with ion exchangers is a well-known phenomenon.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-06-23</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1020132</prism:doi>
	<prism:startingPage>132</prism:startingPage>
		<prism:endingPage>148</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Electrochemical Impedance Spectroscopy—A Simple Method for the Characterization of Polymer Inclusion Membranes Containing Aliquat 336]]></dc:title>
    <dc:date>2011-06-23</dc:date>
	<dc:identifier>doi: 10.3390/membranes1020132</dc:identifier>
    	<dc:creator>Michelle O’Rourke</dc:creator>
		<dc:creator>Noel Duffy</dc:creator>
		<dc:creator>Roland De Marco</dc:creator>
		<dc:creator>Ian Potter</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/2/119">
	<title><![CDATA[Membranes, Vol. 1, Pages 119-131: Experimental Study of Fouling and Cleaning of Sintered Stainless Steel Membrane in Electro-Microfiltration of Calcium Salt Particles]]></title>
	<link>http://www.mdpi.com/2077-0375/1/2/119</link>
	<description>Sintered stainless steel (SSS) microfiltration membranes, which served as electrode directly, were used for the experiment of separating Alamin, a calcium salt and protein containing particles, found in dairy processing. Fouling and cleaning of the SSS membranes under the application of an external electric field were studied. The imposed electric field was found, diverging the pH of permeate and retentate. This in turn altered the solubility of the calcium salt and impacted the performance of electro microfiltration membrane. Using electric field as an enhanced cleaning-in-place (CIP) method in back flushing SSS membrane was also studied.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-05-30</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1020119</prism:doi>
	<prism:startingPage>119</prism:startingPage>
		<prism:endingPage>131</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Experimental Study of Fouling and Cleaning of Sintered Stainless Steel Membrane in Electro-Microfiltration of Calcium Salt Particles]]></dc:title>
    <dc:date>2011-05-30</dc:date>
	<dc:identifier>doi: 10.3390/membranes1020119</dc:identifier>
    	<dc:creator>Frank G. F. Qin</dc:creator>
		<dc:creator>John Mawson</dc:creator>
		<dc:creator>Xin An Zeng</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/2/109">
	<title><![CDATA[Membranes, Vol. 1, Pages 109-118: Electroformation of Giant Vesicles on Indium Tin Oxide (ITO)-Coated Poly(ethylene terephthalate) (PET) Electrodes]]></title>
	<link>http://www.mdpi.com/2077-0375/1/2/109</link>
	<description>Electroformation of cell-sized lipid membrane vesicles (giant vesicles, GVs) from egg yolk phosphatidylcholine was examined using a poly(ethylene terephthalate) sheet coated with indium tin oxide (ITO-PET) as the electrode material. With sinusoidal ac voltage, GV formation occurred in a similar manner to that on an ITO-glass electrode widely used in electroformation. Difference in the specific electrical resistance of ITO-PET did not significantly affect electroformation. The present results indicate that ITO-PET may be used as more flexible and less expensive electrode material in electroformation. In order to obtain insights into electroformation, other electric voltage forms, static dc and dc pulses, were also tested in place of commonly used sinusoidal ac. Under the present conditions, the best GV formation was observed with dc pulses of negative polarity. The result with static dc demonstrated that the mechanical vibration of swelling lipid seen with sinusoidal ac voltage was not essential for GV formation. On the positive electrode, the electroswelling of lipid mainly yielded non-spherical membranous objects. Pre-application of positive dc voltage on lipid hindered GV formation in electroswelling of the lipid with ac.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-05-26</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1020109</prism:doi>
	<prism:startingPage>109</prism:startingPage>
		<prism:endingPage>118</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Electroformation of Giant Vesicles on Indium Tin Oxide (ITO)-Coated Poly(ethylene terephthalate) (PET) Electrodes]]></dc:title>
    <dc:date>2011-05-26</dc:date>
	<dc:identifier>doi: 10.3390/membranes1020109</dc:identifier>
    	<dc:creator>Yukihisa Okumura</dc:creator>
		<dc:creator>Yuuichi Iwata</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/2/98">
	<title><![CDATA[Membranes, Vol. 1, Pages 98-108: Effect of Ammonium- and Phosphonium-Based Ionic Liquids on the Separation of Lactic Acid by Supported Ionic Liquid Membranes (SILMs)]]></title>
	<link>http://www.mdpi.com/2077-0375/1/2/98</link>
	<description>Biodegradable polymers have attracted much attention from an environmental point of view. Optically pure lactic acid that can be prepared by fermentation is one of the important raw materials for biodegradable polymer. The separation and purification of lactic acid from the fermentation broth are the major portions of the production costs. We proposed the application of supported ionic liquid membranes to recovering lactic acid. In this paper, the effect of ionic liquids, such as Aliquat 336, CYPHOS IL-101, CYPHOS IL-102, CYPHOS IL-104, CYPHOS IL-109 and CYPHOS IL-111 on the lactic acid permeation have been studied. Aliquat 336, CYPHOS IL-101 and CYPHOS IL-102 were found to be the best membrane solvents as far as membrane stability and permeation of lactic acid are concerned. CYPHOS IL-109 and CYPHOS IL-111 were found to be unsuitable, as they leak out from the pores of the supported liquid membrane (SLM), thereby allowing free transport of lactic acid as well as hydrochloric acid. CYPHOS IL-102 was found to be the most adequate (Permeation rate = 60.41%) among these ionic liquids as far as the separation of lactic acid is concerned. The permeation mechanisms, by which ionic liquid-water complexes act as the carrier of lactate and hydrochloric acid, were proposed. The experimental permeation results have been obtained as opposed to the expected values from the solution-diffusion mechanism.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-05-13</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1020098</prism:doi>
	<prism:startingPage>98</prism:startingPage>
		<prism:endingPage>108</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Effect of Ammonium- and Phosphonium-Based Ionic Liquids on the Separation of Lactic Acid by Supported Ionic Liquid Membranes (SILMs)]]></dc:title>
    <dc:date>2011-05-13</dc:date>
	<dc:identifier>doi: 10.3390/membranes1020098</dc:identifier>
    	<dc:creator>Michiaki Matsumoto</dc:creator>
		<dc:creator>Abhishek Panigrahi</dc:creator>
		<dc:creator>Yuuki Murakami</dc:creator>
		<dc:creator>Kazuo Kondo</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/2/91">
	<title><![CDATA[Membranes, Vol. 1, Pages 91-97: Membrane Characterization by Microscopic and Scattering Methods: Multiscale Structure]]></title>
	<link>http://www.mdpi.com/2077-0375/1/2/91</link>
	<description>Several microscopic and scattering techniques at different observation scales (from atomic to macroscopic) were used to characterize both surface and bulk properties of four new flat-sheet polyethersulfone (PES) membranes (10, 30, 100 and 300 kDa) and new 100 kDa hollow fibers (PVDF). Scanning Electron Microscopy (SEM) with “in lens” detection was used to obtain information on the pore sizes of the skin layers at the atomic scale. White Light Interferometry (WLI) and Atomic Force Microscopy (AFM) using different scales (for WLI: windows: 900 × 900 µm2 and 360 × 360 µm2; number of points: 1024; for AFM: windows: 50 × 50 µm2 and 5 × 5 µm2; number of points: 512) showed that the membrane roughness increases markedly with the observation scale and that there is a continuity between the different scan sizes for the determination of the RMS roughness. High angular resolution ellipsometric measurements were used to obtain the signature of each cut-off and the origin of the scattering was identified as coming from the membrane bulk.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-04-13</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>2</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1020091</prism:doi>
	<prism:startingPage>91</prism:startingPage>
		<prism:endingPage>97</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Membrane Characterization by Microscopic and Scattering Methods: Multiscale Structure]]></dc:title>
    <dc:date>2011-04-13</dc:date>
	<dc:identifier>doi: 10.3390/membranes1020091</dc:identifier>
    	<dc:creator>Rahma Tamime</dc:creator>
		<dc:creator>Yvan Wyart</dc:creator>
		<dc:creator>Laure Siozade</dc:creator>
		<dc:creator>Isabelle Baudin</dc:creator>
		<dc:creator>Carole Deumie</dc:creator>
		<dc:creator>Karl Glucina</dc:creator>
		<dc:creator>Philippe Moulin</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/80">
	<title><![CDATA[Membranes, Vol. 1, Pages 80-90: Volatile Organic Compound (VOC) Removal by Vapor Permeation at Low VOC Concentrations: Laboratory Scale Results and Modeling for Scale Up]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/80</link>
	<description>Petroleum transformation industries have applied membrane processes for solvent and hydrocarbon recovery as an economic alternative to reduce their emissions and reuse evaporated components. Separation of the volatile organic compounds (VOCs) (toluene-propylene-butadiene) from air was performed using a poly dimethyl siloxane (PDMS)/α-alumina membrane. The experimental set-up followed the constant pressure/variable flow set-up and was operated at ~21 °C. The membrane is held in a stainless steel module and has a separation area of 55 × 10−4 m². Feed stream was set to atmospheric pressure and permeate side to vacuum between 3 and 5 mbar. To determine the performance of the module, the removed fraction of VOC was analyzed by Gas Chromatography/Flame Ionization Detector (GC/FID). The separation of the binary, ternary and quaternary hydrocarbon mixtures from air was performed at different flow rates and more especially at low concentrations. The permeate flux, permeance, enrichment factor, separation efficiency and the recovery extent of the membrane were determined as a function of these operating conditions. The permeability coefficients and the permeate flux through the composite PDMS-alumina membrane follow the order given by the Hildebrand parameter: toluene &amp;gt; 1,3-butadiene &amp;gt; propylene. The simulated data for the binary VOC/air mixtures showed fairly good agreement with the experimental results in the case of 1,3-butadiene and propylene. The discrepancies observed for toluene permeation could be minimized by taking into account the effects of the porous support and an influence of the concentration polarization. Finally, the installation of a 0.02 m2 membrane module would reduce 95% of the VOC content introduced at real concentration conditions used in the oil industry.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-03-03</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010080</prism:doi>
	<prism:startingPage>80</prism:startingPage>
		<prism:endingPage>90</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Volatile Organic Compound (VOC) Removal by Vapor Permeation at Low VOC Concentrations: Laboratory Scale Results and Modeling for Scale Up]]></dc:title>
    <dc:date>2011-03-03</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010080</dc:identifier>
    	<dc:creator>Georgette Rebollar-Perez</dc:creator>
		<dc:creator>Emilie Carretier</dc:creator>
		<dc:creator>Nicolas Lesage</dc:creator>
		<dc:creator>Philippe Moulin</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/70">
	<title><![CDATA[Membranes, Vol. 1, Pages 70-79: Continuous Membrane-Based Screening System for Biocatalysis]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/70</link>
	<description>The use of membrane reactors for enzymatic and co-factor regenerating reactions offers versatile advantages such as higher conversion rates and space-time-yields and is therefore often applied in industry. However, currently available screening and kinetics characterization systems are based on batch and fed-batch operated reactors and were developed for whole cell biotransformations rather than for enzymatic catalysis. Therefore, the data obtained from such systems has only limited transferability for continuous membrane reactors. The aim of this study is to evaluate and to improve a novel screening and characterization system based on the membrane reactor concept using the enzymatic hydrolysis of cellulose as a model reaction. Important aspects for the applicability of the developed system such as long-term stability and reproducibility of continuous experiments were very high. The concept used for flow control and fouling suppression allowed control of the residence time with a high degree of precision (±1% accuracy) in a long-term study (&amp;gt;100 h).</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-02-25</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010070</prism:doi>
	<prism:startingPage>70</prism:startingPage>
		<prism:endingPage>79</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Continuous Membrane-Based Screening System for Biocatalysis]]></dc:title>
    <dc:date>2011-02-25</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010070</dc:identifier>
    	<dc:creator>Evgenij Lyagin</dc:creator>
		<dc:creator>Anja Drews</dc:creator>
		<dc:creator>Subhamoy Bhattacharya</dc:creator>
		<dc:creator>Matthias Kraume</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/59">
	<title><![CDATA[Membranes, Vol. 1, Pages 59-69: Characteristics of Filter Cake Exfoliation in Upward Ultrafiltration of Nanoparticle Suspensions]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/59</link>
	<description>Downward and upward ultrafiltration (UF) was performed using the suspensions of nanosized colloidal silica with different particle diameters and their filtration rates were compared. In downward UF, the filtration rate decreases as the particle diameter decreases because the specific filtration resistance of the filter cake becomes significantly higher. In contrast, the filtration rate in upward UF increases with the decrease in the particle diameter because the filter cake consisting of small particles is exfoliated much more easily under the influence of gravity than that of large ones. In order to evaluate the characteristics of the filter cake exfoliation, the steady filtration rate in the upward mode was measured. The steady filtration rate has a tendency to decrease with particle concentration as well as mean particle diameter. Therefore, when the small particles are added into a given concentration of large particle suspension, the mean particle diameter decreases and the total particle concentration increases due to the dosage of small particles. This results in a maximum of the steady filtration rate at a certain dosage of small particles. Moreover, an estimation equation was proposed for predicting the steady filtration rate in upward UF of colloidal silica suspensions with various mean particle diameters and total particle concentrations.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-01-20</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010059</prism:doi>
	<prism:startingPage>59</prism:startingPage>
		<prism:endingPage>69</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Characteristics of Filter Cake Exfoliation in Upward Ultrafiltration of Nanoparticle Suspensions]]></dc:title>
    <dc:date>2011-01-20</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010059</dc:identifier>
    	<dc:creator>Yasuhito Mukai</dc:creator>
		<dc:creator>Aya Nishio</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/48">
	<title><![CDATA[Membranes, Vol. 1, Pages 48-58: Direct Contact Membrane Distillation of Dairy Process Streams]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/48</link>
	<description>Membrane distillation (MD) was applied for the concentration of a range of dairy streams, such as whole milk, skim milk and whey. MD of a pure lactose solution was also investigated. Direct contact MD (DCMD) mode experiments were carried out in continuous concentration mode, keeping the warm feed/retentate and cold permeate stream temperatures at 54 °C and 5 °C respectively. Performance in terms of flux and retention was assessed. The flux was found to decrease with an increase of dry-matter concentration in the feed. Retention of dissolved solids was found to be close to 100% and independent of the dry-matter concentration in the feed. Fourier Transform Infrared Spectroscopy (FTIR) of the fouled membranes confirms organics being present in the fouling layer.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2011-01-04</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010048</prism:doi>
	<prism:startingPage>48</prism:startingPage>
		<prism:endingPage>58</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Direct Contact Membrane Distillation of Dairy Process Streams]]></dc:title>
    <dc:date>2011-01-04</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010048</dc:identifier>
    	<dc:creator>Angela Hausmann</dc:creator>
		<dc:creator>Peter Sanciolo</dc:creator>
		<dc:creator>Todor Vasiljevic</dc:creator>
		<dc:creator>Elankovan Ponnampalam</dc:creator>
		<dc:creator>Nohemi Quispe-Chavez</dc:creator>
		<dc:creator>Mike Weeks</dc:creator>
		<dc:creator>Mikel Duke</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/37">
	<title><![CDATA[Membranes, Vol. 1, Pages 37-47: Synthesis of Carbon Nanotube (CNT) Composite Membranes]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/37</link>
	<description>Carbon nanotubes are attractive approach for designing of new membranes for advanced molecular separation because of their unique transport properties and ability to mimic biological protein channels. In this work the synthetic approach for fabrication of carbon nanotubes (CNTs) composite membranes is presented. The method is based on growth of multi walled carbon nanotubes (MWCNT) using chemical vapour deposition (CVD) on the template of nanoporous alumina (PA) membranes. The influence of experimental conditions including carbon precursor, temperature, deposition time, and PA template on CNT growth process and quality of fabricated membranes was investigated. The synthesis of CNT/PA composites with controllable nanotube dimensions such as diameters (30–150 nm), and thickness (5–100 µm), was demonstrated. The chemical composition and morphological characteristics of fabricated CNT/PA composite membranes were investigated by various characterisation techniques including scanning electron microscopy (SEM), energy-dispersive x-ray spectroscopy (EDXS), high resolution transmission electron microscopy (HRTEM) and x-ray diffraction (XRD). Transport properties of prepared membranes were explored by diffusion of dye (Rose Bengal) used as model of hydrophilic transport molecule.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2010-12-27</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010037</prism:doi>
	<prism:startingPage>37</prism:startingPage>
		<prism:endingPage>47</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Synthesis of Carbon Nanotube (CNT) Composite Membranes]]></dc:title>
    <dc:date>2010-12-27</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010037</dc:identifier>
    	<dc:creator>Tariq Altalhi</dc:creator>
		<dc:creator>Milena Ginic-Markovic</dc:creator>
		<dc:creator>Ninghui Han</dc:creator>
		<dc:creator>Stephen Clarke</dc:creator>
		<dc:creator>Dusan Losic</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/25">
	<title><![CDATA[Membranes, Vol. 1, Pages 25-36: Control of Porosity and Pore Size of Metal Reinforced Carbon Nanotube Membranes]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/25</link>
	<description>Membranes are crucial in modern industry and both new technologies and materials need to be designed to achieve higher selectivity and performance. Exotic materials such as nanoparticles offer promising perspectives, and combining both their very high specific surface area and the possibility to incorporate them into macrostructures have already shown to substantially increase the membrane performance. In this paper we report on the fabrication and engineering of metal-reinforced carbon nanotube (CNT) Bucky-Paper (BP) composites with tuneable porosity and surface pore size. A BP is an entangled mesh non-woven like structure of nanotubes. Pure CNT BPs present both very high porosity (&amp;gt;90%) and specific surface area (&amp;gt;400 m2/g). Furthermore, their pore size is generally between 20–50 nm making them promising candidates for various membrane and separation applications. Both electro-plating and electroless plating techniques were used to plate different series of BPs and offered various degrees of success. Here we will report mainly on electroless plated gold/CNT composites. The benefit of this method resides in the versatility of the plating and the opportunity to tune both average pore size and porosity of the structure with a high degree of reproducibility. The CNT BPs were first oxidized by short UV/O3 treatment, followed by successive immersion in different plating solutions. The morphology and properties of these samples has been investigated and their performance in air permeation and gas adsorption will be reported.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2010-12-21</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010025</prism:doi>
	<prism:startingPage>25</prism:startingPage>
		<prism:endingPage>36</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Control of Porosity and Pore Size of Metal Reinforced Carbon Nanotube Membranes]]></dc:title>
    <dc:date>2010-12-21</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010025</dc:identifier>
    	<dc:creator>Ludovic Dumee</dc:creator>
		<dc:creator>Leonora Velleman</dc:creator>
		<dc:creator>Kallista Sears</dc:creator>
		<dc:creator>Matthew Hill</dc:creator>
		<dc:creator>Jurg Schutz</dc:creator>
		<dc:creator>Niall Finn</dc:creator>
		<dc:creator>Mikel Duke</dc:creator>
		<dc:creator>Stephen Gray</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/13">
	<title><![CDATA[Membranes, Vol. 1, Pages 13-24: A Model for Transport Phenomena in a Cross-Flow Ultrafiltration Module with Microchannels]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/13</link>
	<description>Cross-flow ultrafiltration of macromolecular solutions in a module with microchannels is expected to have the advantages of fast diffusion from the membrane surface and a high ratio of membrane surface area to feed liquid volume. Cross-flow ultrafiltration modules with microchannels are expected to be used for separation and refining and as membrane reactors in microchemical processes. Though these modules can be applied as a separator connected with a micro-channel reactor or a membrane reactor, there have been few papers on their performance. The purpose of this study was to clarify the relationship between operational conditions and performance of cross-flow ultrafiltration devices with microchannels. In this study, Poly Vinyl Pyrrolidone (PVP) aqueous solution was used as a model solute of macromolecules such as enzymes. Cross-flow ultrafiltration experiments were carried out under constant pressure conditions, varying other operational conditions. The permeate flux decreased in the beginning of each experiment. After enough time passed, the permeate flux reached a constant value. The performance of the module was discussed based on the constant values of the flux. It was observed that the permeate flux increased with increasing transmembrane pressure (TMP) and feed flow rate, and decreased with an increase of feed liquid concentration. A model of the transport phenomena in the feed liquid side channel and the permeation through the membrane was developed based on the concentration and velocity distributions in the feed side channel. The experimental results were compared with those based on the model and the performance of the ultrafiltration module is discussed.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2010-12-16</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010013</prism:doi>
	<prism:startingPage>13</prism:startingPage>
		<prism:endingPage>24</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[A Model for Transport Phenomena in a Cross-Flow Ultrafiltration Module with Microchannels]]></dc:title>
    <dc:date>2010-12-16</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010013</dc:identifier>
    	<dc:creator>Aiko Nishimoto</dc:creator>
		<dc:creator>Shiro Yoshikawa</dc:creator>
		<dc:creator>Shinichi Ookawara</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/3">
	<title><![CDATA[Membranes, Vol. 1, Pages 3-12: The Fabrication of Biomimetic Chitosan Scaffolds by Using SBF Treatment with Different Crosslinking Agents]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/3</link>
	<description>In this study, a chitosan substrate was modified by simulated body fluid (SBF) treatment, in which the effect of the chosen crosslinking agent was investigated. Two crosslinking agents, glutaraldehyde (GA) and sodium tripolyphosphate (TPP), were used before the SBF process. By using TPP as the crosslinking agent, the Ca/P ratio and the degree of crystallinity were very close to the natural bone matrix. On the contrary, the substrate properties were very different from natural bone when the crosslinking agent GA was used. The results indicate that the produced substrates were  biomimetic when the TPP was applied. On the SBF-modified chitosan substrates with TPP crosslinking, the cultured osteoblastic cells expressed better proliferation, mitochondria activity and differentiation ability. The chitosan crosslinked using TPP was a good template in the SBF process, which resulted in a highly biomimetic layer. This biomimetic substrate possesses excellent biocompatibility and osteoconduction ability, promising high potential in the promotion of bone tissue engineering.</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2010-12-15</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Article</prism:section>
	<prism:doi>10.3390/membranes1010003</prism:doi>
	<prism:startingPage>3</prism:startingPage>
		<prism:endingPage>12</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[The Fabrication of Biomimetic Chitosan Scaffolds by Using SBF Treatment with Different Crosslinking Agents]]></dc:title>
    <dc:date>2010-12-15</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010003</dc:identifier>
    	<dc:creator>Chung-Tun Liao</dc:creator>
		<dc:creator>Ming-Hua Ho</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
        <item rdf:about="http://www.mdpi.com/2077-0375/1/1/1">
	<title><![CDATA[Membranes, Vol. 1, Pages 1-2: Welcome to Membranes — A New Open Access Journal on Membrane Separation and Technology]]></title>
	<link>http://www.mdpi.com/2077-0375/1/1/1</link>
	<description>Membrane separation, from its infancy as a predominantly laboratory technique in the middle of the last century, has advanced with remarkable speed and now underpins a range of mature industrial technologies. [...]</description>

	<prism:publicationName>Membranes</prism:publicationName>
	<prism:publicationDate>2010-12-12</prism:publicationDate>
	<prism:volume>1</prism:volume>
	<prism:number>1</prism:number>
	<prism:section>Editorial</prism:section>
	<prism:doi>10.3390/membranes1010001</prism:doi>
	<prism:startingPage>1</prism:startingPage>
		<prism:endingPage>2</prism:endingPage>
		<prism:issn>2077-0375</prism:issn>
	
	<dc:title><![CDATA[Welcome to Membranes — A New Open Access Journal on Membrane Separation and Technology]]></dc:title>
    <dc:date>2010-12-12</dc:date>
	<dc:identifier>doi: 10.3390/membranes1010001</dc:identifier>
    	<dc:creator>Spas D. Kolev</dc:creator>
	
	<cc:license rdf:resource="http://creativecommons.org/licenses/by/3.0/" />
</item>
    
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	<cc:permits rdf:resource="http://creativecommons.org/ns#DerivativeWorks" />
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