393 research outputs found

    Vanadium Supported on Alumina and/or Zirconia Catalysts for the Selective Transformation of Ethane and Methanol

    Full text link
    [EN] Vanadium supported on pure (Al2O3, ZrO2) or mixed zirconia-alumina (with Al/(Al + Zr) ratio of 0.75 or 0.25) catalysts have been prepared by wet impregnation, using homemade prepared supports. The catalysts have been characterized and tested in the oxidative dehydrogenation (ODH) of ethane and in the methanol aerobic transformation. The catalytic performance strongly depends on the nature of the metal oxide support. Thus, activity decreases in the order: VOx/ZrO2 > VOx/(Al,Zr-oxides) > VOx/Al2O3. On the other hand, at low and medium ethane conversions, the selectivity to ethylene presents an opposite trend: VOx/Al2O3 > VOx/(Al,Zr-oxides) > VOx/ZrO2. The different selectivity to ethylene at high conversion is due to the lower/higher initial ethylene formation and to the extent of the ethylene decomposition. Interestingly, VOx/(Al,Zr-oxides) with low Zr-loading present the lowest ethylene decomposition. The catalytic results obtained mainly depend on the nature of the supports whereas the role of the dispersion of vanadium species is unclear. In methanol oxidation, the catalysts tested present similar catalytic activity regardless of the support (Al2O3, ZrO2 or mixed Al2O3-ZrO2) but strong differences in the selectivity to the reaction products. Thus, dimethyl ether was mainly observed on alumina-supported vanadium oxide catalysts (which is associated to the presence of acidic sites on the surface of the catalyst, as determined by TPD-NH3). Formaldehyde was the main reaction product on catalysts supported on Zr-containing oxides (which can be related to a low presence of acid sites). In this article, the importance of the presence of acid sites in ethane ODH, which can be estimated using the methanol transformation reaction, is also discussed.The authors would like to acknowledge the DGICYT (CTQ2015-68951-C3-1-R and MAT2017-84118-C2-1-R projects), the Secretary of State for International Cooperation in Spain (Project AP/040992/11) and FEDER for financial support. B.S. also thanks the University of Valencia (UV-INV-AE16-484416).Benomar, S.; Masso Ramírez, A.; Solsona Espriu, BE.; Isaadi, R.; López Nieto, JM. (2018). Vanadium Supported on Alumina and/or Zirconia Catalysts for the Selective Transformation of Ethane and Methanol. Catalysts. 8(4):1-18. https://doi.org/10.3390/catal8040126S11884Chieregato, A., López Nieto, J. M., & Cavani, F. (2015). Mixed-oxide catalysts with vanadium as the key element for gas-phase reactions. Coordination Chemistry Reviews, 301-302, 3-23. doi:10.1016/j.ccr.2014.12.003Nieto, J. M. L. (2006). The selective oxidative activation of light alkanes. From supported vanadia to multicomponent bulk V-containing catalysts. Topics in Catalysis, 41(1-4), 3-15. doi:10.1007/s11244-006-0088-4Wachs, I. E. (2013). Catalysis science of supported vanadium oxide catalysts. Dalton Transactions, 42(33), 11762. doi:10.1039/c3dt50692dJames, O. O., Mandal, S., Alele, N., Chowdhury, B., & Maity, S. (2016). Lower alkanes dehydrogenation: Strategies and reaction routes to corresponding alkenes. Fuel Processing Technology, 149, 239-255. doi:10.1016/j.fuproc.2016.04.016Blasco, T., & Nieto, J. M. L. (1997). Oxidative dyhydrogenation of short chain alkanes on supported vanadium oxide catalysts. Applied Catalysis A: General, 157(1-2), 117-142. doi:10.1016/s0926-860x(97)00029-xKung, H. H., & Kung, M. C. (1997). Oxidative dehydrogenation of alkanes over vanadium-magnesium-oxides. Applied Catalysis A: General, 157(1-2), 105-116. doi:10.1016/s0926-860x(97)00028-8Cavani, F., & Trifirò, F. (1997). Some aspects that affect the selective oxidation of paraffins. Catalysis Today, 36(4), 431-439. doi:10.1016/s0920-5861(96)00234-9Bañares, M. A. (1999). Supported metal oxide and other catalysts for ethane conversion: a review. Catalysis Today, 51(2), 319-348. doi:10.1016/s0920-5861(99)00053-xBhasin, M. ., McCain, J. ., Vora, B. ., Imai, T., & Pujadó, P. . (2001). Dehydrogenation and oxydehydrogenation of paraffins to olefins. Applied Catalysis A: General, 221(1-2), 397-419. doi:10.1016/s0926-860x(01)00816-xCavani, F., Ballarini, N., & Cericola, A. (2007). Oxidative dehydrogenation of ethane and propane: How far from commercial implementation? Catalysis Today, 127(1-4), 113-131. doi:10.1016/j.cattod.2007.05.009Gärtner, C. A., van Veen, A. C., & Lercher, J. A. (2013). Oxidative Dehydrogenation of Ethane: Common Principles and Mechanistic Aspects. ChemCatChem, 5(11), 3196-3217. doi:10.1002/cctc.201200966Galli, A., López Nieto, J. M., Dejoz, A., & Vazquez, M. I. (1995). The effect of potassium on the selective oxidation ofn-butane and ethane over Al2O3-supported vanadia catalysts. Catalysis Letters, 34(1-2), 51-58. doi:10.1007/bf00808321Argyle, M. D., Chen, K., Bell, A. T., & Iglesia, E. (2002). Ethane Oxidative Dehydrogenation Pathways on Vanadium Oxide Catalysts. The Journal of Physical Chemistry B, 106(21), 5421-5427. doi:10.1021/jp0144552Dinse, A., Ozarowski, A., Hess, C., Schomäcker, R., & Dinse, K.-P. (2008). Potential of High-Frequency EPR for Investigation of Supported Vanadium Oxide Catalysts. The Journal of Physical Chemistry C, 112(45), 17664-17671. doi:10.1021/jp807159fChen, K., Bell, A. T., & Iglesia, E. (2002). The Relationship between the Electronic and Redox Properties of Dispersed Metal Oxides and Their Turnover Rates in Oxidative Dehydrogenation Reactions. Journal of Catalysis, 209(1), 35-42. doi:10.1006/jcat.2002.3620López Nieto, J. M., Soler, J., Concepción, P., Herguido, J., Menéndez, M., & Santamarı́a, J. (1999). Oxidative Dehydrogenation of Alkanes over V-based Catalysts: Influence of Redox Properties on Catalytic Performance. Journal of Catalysis, 185(2), 324-332. doi:10.1006/jcat.1999.2467Argyle, M. D., Chen, K., Iglesia, E., & Bell, A. T. (2005). In situ UV−Visible Spectroscopic Measurements of Kinetic Parameters and Active Sites for Catalytic Oxidation of Alkanes on Vanadium Oxides†. The Journal of Physical Chemistry B, 109(6), 2414-2420. doi:10.1021/jp040166cAl-Ghamdi, S. A., & de Lasa, H. I. (2014). Propylene production via propane oxidative dehydrogenation over VOx/γ-Al2O3 catalyst. Fuel, 128, 120-140. doi:10.1016/j.fuel.2014.02.033SOLSONA, B., DEJOZ, A., GARCIA, T., CONCEPCION, P., NIETO, J., VAZQUEZ, M., & NAVARRO, M. (2006). Molybdenum–vanadium supported on mesoporous alumina catalysts for the oxidative dehydrogenation of ethane. Catalysis Today, 117(1-3), 228-233. doi:10.1016/j.cattod.2006.05.025Chen, S., Ma, F., Xu, A., Wang, L., Chen, F., & Lu, W. (2014). Study on the structure, acidic properties of V–Zr nanocrystal catalysts in oxidative dehydrogenation of propane. Applied Surface Science, 289, 316-325. doi:10.1016/j.apsusc.2013.10.158Elbadawi, A. H., Ba-Shammakh, M. S., Al-Ghamdi, S., Razzak, S. A., & Hossain, M. M. (2016). Reduction kinetics and catalytic activity of VO x /γ-Al 2 O 3 -ZrO 2 for gas phase oxygen free ODH of ethane. Chemical Engineering Journal, 284, 448-457. doi:10.1016/j.cej.2015.08.048Rostom, S., & de Lasa, H. I. (2017). Propane Oxidative Dehydrogenation Using Consecutive Feed Injections and Fluidizable VOx/γAl2O3 and VOx/ZrO2–γAl2O3 Catalysts. Industrial & Engineering Chemistry Research, 56(45), 13109-13124. doi:10.1021/acs.iecr.7b01369HERACLEOUS, E., & LEMONIDOU, A. (2006). Ni–Nb–O mixed oxides as highly active and selective catalysts for ethene production via ethane oxidative dehydrogenation. Part I: Characterization and catalytic performance. Journal of Catalysis, 237(1), 162-174. doi:10.1016/j.jcat.2005.11.002Skoufa, Z., Heracleous, E., & Lemonidou, A. A. (2015). On ethane ODH mechanism and nature of active sites over NiO-based catalysts via isotopic labeling and methanol sorption studies. Journal of Catalysis, 322, 118-129. doi:10.1016/j.jcat.2014.11.014Ipsakis, D., Heracleous, E., Silvester, L., Bukur, D. B., & Lemonidou, A. A. (2017). Reduction and oxidation kinetic modeling of NiO-based oxygen transfer materials. Chemical Engineering Journal, 308, 840-852. doi:10.1016/j.cej.2016.09.114Delgado, D., Solsona, B., Ykrelef, A., Rodríguez-Gómez, A., Caballero, A., Rodríguez-Aguado, E., … López Nieto, J. M. (2017). Redox and Catalytic Properties of Promoted NiO Catalysts for the Oxidative Dehydrogenation of Ethane. The Journal of Physical Chemistry C, 121(45), 25132-25142. doi:10.1021/acs.jpcc.7b07066Solsona, B., Concepción, P., López Nieto, J. M., Dejoz, A., Cecilia, J. A., Agouram, S., … Rodríguez Castellón, E. (2016). Nickel oxide supported on porous clay heterostructures as selective catalysts for the oxidative dehydrogenation of ethane. Catalysis Science & Technology, 6(10), 3419-3429. doi:10.1039/c5cy01811kGärtner, C. A., van Veen, A. C., & Lercher, J. A. (2014). Oxidative Dehydrogenation of Ethane on Dynamically Rearranging Supported Chloride Catalysts. Journal of the American Chemical Society, 136(36), 12691-12701. doi:10.1021/ja505411sTatibouët, J. M. (1997). Methanol oxidation as a catalytic surface probe. Applied Catalysis A: General, 148(2), 213-252. doi:10.1016/s0926-860x(96)00236-0Forzatti, P., Tronconi, E., Elmi, A. S., & Busca, G. (1997). Methanol oxidation over vanadia-based catalysts. Applied Catalysis A: General, 157(1-2), 387-408. doi:10.1016/s0926-860x(97)00026-4Wachs, I. E., Chen, Y., Jehng, J.-M., Briand, L. E., & Tanaka, T. (2003). Molecular structure and reactivity of the Group V metal oxides. Catalysis Today, 78(1-4), 13-24. doi:10.1016/s0920-5861(02)00337-1Shah, P. R., Baldychev, I., Vohs, J. M., & Gorte, R. J. (2009). Comparison of redox isotherms for vanadia supported on zirconia and titania. Applied Catalysis A: General, 361(1-2), 13-17. doi:10.1016/j.apcata.2009.03.036Baldychev, I., Gorte, R. J., & Vohs, J. M. (2010). The impact of redox properties on the reactivity of V2O5/Al2O3 catalysts. Journal of Catalysis, 269(2), 397-403. doi:10.1016/j.jcat.2009.11.022Hess, C. (2009). Nanostructured Vanadium Oxide Model Catalysts for Selective Oxidation Reactions. ChemPhysChem, 10(2), 319-326. doi:10.1002/cphc.200800585Smith, M. A., Zoelle, A., Yang, Y., Rioux, R. M., Hamilton, N. G., Amakawa, K., … Trunschke, A. (2014). Surface roughness effects in the catalytic behavior of vanadia supported on SBA-15. Journal of Catalysis, 312, 170-178. doi:10.1016/j.jcat.2014.01.011Wang, N., Qiu, J., Wu, J., You, K., & Luo, H. (2015). A Comparison of the Redox Properties of Bulk Vanadium Mixed Oxide Catalysts. Catalysis Letters, 145(9), 1792-1797. doi:10.1007/s10562-015-1584-6Beck, B., Harth, M., Hamilton, N. G., Carrero, C., Uhlrich, J. J., Trunschke, A., … Schomäcker, R. (2012). Partial oxidation of ethanol on vanadia catalysts on supporting oxides with different redox properties compared to propane. Journal of Catalysis, 296, 120-131. doi:10.1016/j.jcat.2012.09.008KIM, T., & WACHS, I. (2008). CH3OH oxidation over well-defined supported V2O5/Al2O3 catalysts: Influence of vanadium oxide loading and surface vanadium–oxygen functionalities. Journal of Catalysis, 255(2), 197-205. doi:10.1016/j.jcat.2008.02.007Baldychev, I., Vohs, J. M., & Gorte, R. J. (2011). The effect of support on redox properties and methanol-oxidation activity of vanadia catalysts. Applied Catalysis A: General, 391(1-2), 86-91. doi:10.1016/j.apcata.2010.05.051Zhang, F., Chupas, P. J., Lui, S. L. A., Hanson, J. C., Caliebe, W. A., Lee, P. L., & Chan, S.-W. (2007). In situ Study of the Crystallization from Amorphous to Cubic Zirconium Oxide:  Rietveld and Reverse Monte Carlo Analyses. Chemistry of Materials, 19(13), 3118-3126. doi:10.1021/cm061739wPieck, C. L., del Val, S., López Granados, M., Bañares, M. A., & Fierro, J. L. G. (2002). Bulk and Surface Structures of V2O5/ZrO2Systems and Their Relevance foro-Xylene Oxidation. Langmuir, 18(7), 2642-2648. doi:10.1021/la0114631Soriano, M. D., Rodríguez-Castellón, E., García-González, E., & López Nieto, J. M. (2014). Catalytic behavior of NaV6O15 bronze for partial oxidation of hydrogen sulfide. Catalysis Today, 238, 62-68. doi:10.1016/j.cattod.2014.02.030Kanervo, J. M., Harlin, M. E., Krause, A. O. I., & Bañares, M. A. (2003). Characterisation of alumina-supported vanadium oxide catalysts by kinetic analysis of H2-TPR data. Catalysis Today, 78(1-4), 171-180. doi:10.1016/s0920-5861(02)00326-7Hess, C., Tzolova-Müller, G., & Herbert, R. (2007). The Influence of Water on the Dispersion of Vanadia Supported on Silica SBA-15:  A Combined XPS and Raman Study. The Journal of Physical Chemistry C, 111(26), 9471-9479. doi:10.1021/jp071392

    Optimizing both catalyst preparation and catalytic behaviour for the oxidative dehydrogenation of ethane of Ni-Sn-O catalysts

    Full text link
    [EN] Bulk Ni-Sn-O catalysts have been synthesized, tested in the oxidative dehydrogenation of ethane and characterized by several physicochemical techniques. The catalysts have been prepared by evaporation of the corresponding salts using several additives in the synthesis gel, i.e. ammonium hydroxide, nitric acid, glyoxylic acid or oxalic acid, in the synthesis gel. The catalysts were finally calcined at 500 degrees C in air. Important changes in the catalytic behaviour have been observed depending on the additive. In fact, an important improvement in the catalytic performance is observed especially when some additives, such as glyoxylic or oxalic acid, are used. Thus the productivity to ethylene multiplies by 6 compared to the reference Ni-Sn-O catalyst if appropriate templates are used, and this is the result of an improvement in both the catalytic activity and the selectivity to ethylene. This improved performance has been explained in terms of the decrease of the crystallite size (and the increase in the surface area of catalyst) as well as the modification of the lattice parameter of nickel oxide.The authors would like to acknowledge the DGICYT in Spain (CTQ2015-68951-C3-1-R and CTQ2012-37925-C03-2) for financial support. We also thank the University of Valencia and SCSIE-UV for assistanceSolsona Espriu, BE.; López Nieto, JM.; Agouram, S.; Soriano Rodríguez, MD.; Dejoz, A.; Vázquez, MI.; Concepción Heydorn, P. (2016). Optimizing both catalyst preparation and catalytic behaviour for the oxidative dehydrogenation of ethane of Ni-Sn-O catalysts. Topics in Catalysis. 59(17-18):1564-1572. https://doi.org/10.1007/s11244-016-0674-zS156415725917-18Heracleous E, Lee AF, Wilson K, Lemonidou AA (2005) J Catal 231:159–171Heracleous E, Lemonidou AA (2006) J Catal 237:162–174Savova B, Loridant S, Filkova D, Millet JMM (2010) Appl Catal A 390:148–157Heracleous E, Lemonidou AA (2010) J Catal 270:67–75Solsona B, Nieto JML, Concepcion P, Dejoz A, Ivars F, Vazquez MI (2011) J Catal 280:28–39Skoufa Z, Heracleous E, Lemonidou AA (2012) Catal Today 192:169–176Zhu H, Ould-Chikh S, Anjum DH, Sun M, Biausque G, Basset JM, Caps V (2012) J Catal 285:292–303Skoufa Z, Heracleous E, Lemonidou AA (2012) Chem Eng Sci 84:48–56Zhu H, Rosenfeld DC, Anjum DH, Caps V, Basset JM (2015) ChemSusChem 8:1254–1263Heracleous E, Lemonidou AA (2015) J Catal 322:118–129Solsona B, Concepcion P, Demicol B, Hernandez S, Delgado JJ, Calvino JJ, Nieto JML (2012) J Catal 295:104–114Nieto JML, Solsona B, Grasselli RK, Concepción P (2014) Top Catal 57:1248–1255Popescu I, Skoufa Z, Heracleous E, Lemonidou AA, Marcu IC (2015) PCCP 17:8138–8147Zhang X, Gong Y, Yu G, Xie Y (2002) J Mol Catal A 180:293–298Popescu I, Skoufa Z, Heracleous E, Lemonidou A, Marcu I-C (2015) Phys Chem Chem Phys 17:8138–8147Nakamura KI, Miyake T, Konishi T, Suzuki T (2006) J Mol Catal A 260:144–151Solsona B, Dejoz AM, Vazquez MI, Ivars F, Nieto JML (2009) Top Catal 52:751–757Bortolozzi JP, Gutierrez LB, Ulla MA (2013) Appl Catal A 452:179–188Takeguchi T, Furukawa S, Inoue M (2001) J Catal 202:14–24Richardson JT, Turk B, Twigg MV (1996) Appl Catal 148:97–112Biju V, Khadar MA (2002) J Nanopart Res 4:247–253Van Veenendaal MA, Sawatzky GA (1993) Phys Rev Lett 70:2459–2462Vedrine JC, Hollinger G, Duc TM (1978) J Phys Chem 82:1515–1520Salagre P, Fierro JLG, Medina F, Sueiras JE (1996) J Mol Catal A 106:125–13

    NiO diluted in high surface area TiO2 as efficient catalysts for the oxidative dehydrogenation of ethane

    Full text link
    [EN] Catalysts consisting of NiO diluted in high surface area TiO2 can be as efficient in the oxidative dehydrogenation of ethane as the most selective NiO-promoted catalysts reported previously in the literature. By selecting the titania matrix and the NiO loading, yields to ethylene over 40% have been obtained. In the present article, three different titanium oxides (TiO2) have been employed as supports or diluters of nickel oxide and have been tested in the oxidative dehydrogenation of ethane to ethylene. All TiO2 used present anatase as the main crystalline phase and different surface areas of 11,55 and 85 m(2) g(-1). It has been observed that by selecting an appropriate nickel loading and the titanium oxide extremely high selectivity towards ethylene can be obtained. Thus, nickel oxide supported on TiO2 with high surface areas (i.e. 55 and 85 m(2) g(-1)) have resulted to give the best catalytic performance although the optimal nickel loading is different for each case. The optimal catalyst has been obtained for NiO-loadings up to 5-10 theoretical monolayers regardless of the TiO2 employed. Free TiO2 is inactive whereas unsupported NiO is active and unselective (forming mainly carbon dioxide) and, therefore, unmodified NiO particles have to be avoided in order to obtain the optimal catalytic performance. The use of low surface area titania (11 m(2) g(-1)) have led to the lowest selectivity to olefin due to the presence of an excess of free NiO particles. (C) 2017 Elsevier B.V. All rights reserved.The authors would like to acknowledge the DGICYT in Spain CTQ2012-37925-C03-2, CTQ2015-68951-C3-1-R, CTQ2015-68951-C3-3-R and SEV-2012-0267 Projects for financial support. D.D. also thanks Severo Ochoa Excellence fellowship (SVP-2014-068669). We also thank the University of Valencia (UV-INV-AE-16-484416 project) and SCSIE-UV for assistanceSanchis, R.; Delgado-Muñoz, D.; Agouram, S.; Soriano Rodríguez, MD.; Vázquez, MI.; Rodriguez-Castellon, E.; Solsona, B.... (2017). NiO diluted in high surface area TiO2 as efficient catalysts for the oxidative dehydrogenation of ethane. Applied Catalysis A General. 536:18-26. https://doi.org/10.1016/j.apcata.2017.02.012S182653

    Corrigendum: Structural Brain Network Reorganization and Social Cognition Related to Adverse Perinatal Condition from Infancy to Early Adolescence

    Get PDF
    In the original article, we omitted a reference to Réveillon et al. (2016) regarding the description of the neuropsychological tests performed by the children and the association between IUGR and hyperactivity/inattention symptoms. This reference is cited in the description of the third cohort (Section Materials and Methods. Subjects) and in the Correlation between Network Metrics and Neuropsychological Score section, as appeared below. We also had neglected to thank the invaluable contribution of the team involved in recruitment, imaging acquisition, and neuropsychological testing. The revised version of the acknowledgments is provided below. The authors apologize for the oversight. These errors do not change the scientific conclusions of the article in any way

    Utilización de servicios sanitarios en ancianos (España 2006-2012): influencia del nivel de salud y de la clase social

    Get PDF
    Objetivo Conocer la utilización de servicios sanitarios de Atención Primaria (AP), Atención Especializada (AE), hospitalizaciones, Hospital de Día y Urgencias, y la hiperfrecuentación en ancianos en España, analizando la influencia del estado de salud, sexo, clase social y evolución temporal. Diseño Estudio transversal en 2 fases. Emplazamiento España. Participantes Personas encuestadas en la Encuesta Nacional de Salud 2006 y 2011-12. Mediciones principales Como variables de salud se utilizaron la salud percibida y diagnosticada (número y tipo de diagnósticos). La clase social se obtuvo a partir de la última ocupación del sustentador principal (clases manuales y no manuales). Se realizaron análisis de regresión logística, ajustando por sexo, edad, nivel de salud, clase social y año, calculando su capacidad predictiva. ResultadosEl porcentaje de población mayor que utiliza consultas médicas descendió en el periodo estudiado. Las mujeres trabajadoras manuales presentaron la mayor prevalencia de mala salud (mala salud percibida en el 2006: 70,6%). La mala salud se asoció a mayor utilización de servicios sanitarios. La salud percibida fue mejor predictor de utilización de servicios y de hiperfrecuentación que la diagnosticada, con la mayor capacidad predictiva para AE (C = 0,676). Los ancianos de clases sociales bajas utilizaron con más frecuencia AP y Urgencias, mientras que la utilización de AE y Hospital de Día fue mayor en clases altas. Conclusiones Existen diferencias en salud y utilización de servicios sanitarios en mayores según clase social. Resulta necesario prestar atención a la salud percibida como predictor de la utilización de servicios sanitarios y revisar la accesibilidad-equidad de nuestros servicios

    Kainate-Triggered Currents in Xenopus Oocytes Injected with Chick Retinal Membrane Fragments: Effect of Guanine Nucleotides

    Get PDF
    PURPOSE. To electrophysiologically characterize ␣-amino-3-hydroxy-5-methyl-4-isoxazolepropionate (AMPA)/kainate receptors in chick retinal membrane fragments, incorporated into Xenopus oocytes by direct microinjection. METHODS. A 6-day retinal membrane suspension was injected into Xenopus oocytes by use of an electronic nanoliter injector. Fifteen to 40 hours after injection, the oocytes were assayed for kainate-elicited inward currents, under voltage-clamp conditions (membrane potential held at Ϫ70 mV). The structural incorporation of the retinal membrane fragments into the oocyte membrane was verified by specific immunofluorescent staining. RESULTS. Chick retinal membrane fragments were efficiently grafted onto Xenopus oocytes after microinjection, with 22.9% Ϯ 7.6% of the oocyte membrane being stained with anti-chick retina antibody. Part of the retinal material was seen as patches of relatively uniform size (292.1 Ϯ 72.3 m 2 ). Bath-applied kainate induced dose-dependent (EC 50 : 64 Ϯ 7 M), nondesensitizing inward currents (15-90 nA) in the chimeric Xenopus oocytes. Sham-injected oocytes did not respond to kainate. Kainate-driven currents were blocked by 6,7-dinitroquinoxaline-2,3-dione (DNQX) and 1-(4-aminopropyl)-4-methyl-7,8-methylenedioxy-5H-2,3-benzodiazepine hydrochloride (GYKI 52466), but not by ␥-D-glutamylaminomethyl sulfonic acid (GAMS) or aminophosphonoheptanoate (AP7), suggesting the involvement of AMPA receptors in the observed responses. Guanine nucleotides (GNs) also blocked kainate currents in a concentration-dependent manner. CONCLUSIONS. An alternative oocyte microinjection technique to analyze the electrophysiological properties of glutamate receptors in chick retinal membranes is described. The results show the functional activity of putative AMPA-preferring receptors from chick retina and confirm, in the chick retinal model, the antagonistic behavior of guanine nucleotides toward glutamate receptors and their potential role as neuropro- These results add to the accumulated evidence on the antagonistic behavior of guanine nucleotides (GNs) at ionotropic glutamate receptors, in very diverse experimental setups, including agonist displacement, electrophysiological recording and neuroprotection paradigms. 21,22 MATERIALS AND METHODS Chick Retinal Membrane Preparation All experiments with animals (chicks, Xenopus, and rabbits) followed our institutional guidelines for care and handling of laboratory animals, in full agreement with the ARVO Statement for the Use of Animals in Ophthalmic and Vision Research. Six-day-old white leghorn chicks were used as the source of retinal membrane fragments. Lysed membranes, prepared as described, 7 were resuspended in 10 mM HEPES (pH 7.4), containing 140 mM KCl and 20 mM NaCl, at a protein concentration of 2 mg/mL, stored in liquid nitrogen, and thawed and sonicated for 10 seconds in an ice water bath just before injection. A control solution without membranes was similarly processed and used for sham-injected control chicks. Oocyte Preparation and Injection Mature female Xenopus laevis were obtained from the Centre d'Elevage des Xénopes, CRBM (Montpellier, France), and kept in chlorine-free fresh water, at 22°C. Discrete ovary portions were removed from anesthetized frogs 23 and stage-V/VI oocytes 24 were individually dissected and kept, at 15°C to 17°C, in sterile modified Barth's solution (10 mM HEPES [pH 7.4], 88 mM NaCl, 1 mM KCl, 0.33 mM Ca(NO 3 ) 2 , 0.41 mM CaCl 2 , 0.82 mM MgSO 4 , and 2.4 mM NaHCO 3 ) supplemented with penicillin (100 IU/mL) and streptomycin (0.1 mg/mL). Oocytes were further treated with collagenase (clostridiopeptidase A: EC3.4.24.3; type IA, 0.5 mg/mL; Sigma-Aldrich, St. Louis, MO), for 50 minutes at room temperature, to remove enveloping cells. 25 From th

    Eastern Mediterranean water outflow during the Younger Dryas was twice that of the present day

    Get PDF
    Eastern Mediterranean deep-intermediate convection was highly sensitive to varying inputs of fresh water fluxes associated with increased rainfall during the African Humid period (15-6 kyr Before Present). Here we investigate changes in the water-outflow from the Eastern Mediterranean Sea since the last deglaciation using neodymium isotope ratios. Our results indicate enhanced outflow during the Younger Dryas, two times higher than present-day outflow and about three times higher than during the last Sapropel. We propose that the increased outflow into the western Mediterranean over the Younger Dryas was the result of the combined effect of 1) enhanced climate-driven convection in the Aegean Sea and 2) reduced convection of western deep water during this period. Our results provide solid evidence for an enhanced Younger Dryas westward flow of Eastern Mediterranean sourced waters in consonance with an intensification of Mediterranean water-outflow during a weakened state of the Atlantic circulatio

    Low temperature total oxidation of toluene by bimetallic Au-Ir catalysts

    Get PDF
    Intimate contact between gold and iridium nanoparticles supported on TiO2 provides a synergetic effect leading to low temperature VOC oxidation activity.The authors would like to acknowledge the UK Engineering and Physical Science Research Council (EPSRC, grant number EP/L020432/2), PAPIIT-UNAM (IN105416 grant) and CONACYT-APN (1216 grant) for funding
    corecore