Littérature scientifique sur le sujet « Adsorption and ion exchange »
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Articles de revues sur le sujet "Adsorption and ion exchange"
Song, Fujiao, Yan Cao, Yunxia Zhao, Ruiyu Jiang, Qi Xu, Jinlong Yan et Qin Zhong. « Ion-Exchanged ZIF-67 Synthesized by One-Step Method for Enhancement of CO2 Adsorption ». Journal of Nanomaterials 2020 (17 février 2020) : 1–11. http://dx.doi.org/10.1155/2020/1508574.
Texte intégralTheodoridou, E., A. D. Jannakoudakis, P. D. Jannakoudakis et S. Antoniadou. « Electrochemically oxidized carbon fibres as an adsorbent for the attachment of dissolved substances. Adsorption of nitro compounds and ion-exchange of heavy metals ». Canadian Journal of Chemistry 69, no 12 (1 décembre 1991) : 1881–85. http://dx.doi.org/10.1139/v91-272.
Texte intégralNoor, Ehteram A., et Fatma M. Al-Solmi. « Analysis of Adsorption, Ion Exchange, Thermodynamic Behaviour of Some Organic Cations on Dowex 50WX4-50/H+Cation Exchanger in Aqueous Solutions ». E-Journal of Chemistry 8, s1 (2011) : S171—S188. http://dx.doi.org/10.1155/2011/963603.
Texte intégralWu, Yu-Chi, Yu-Hong Wei et Ho-Shing Wu. « Adsorption and Desorption Behavior of Ectoine Using Dowex® HCR-S Ion-Exchange Resin ». Processes 9, no 11 (18 novembre 2021) : 2068. http://dx.doi.org/10.3390/pr9112068.
Texte intégralWesselingh, J. A., et J. C. Bosma. « Protein ion-exchange adsorption kinetics ». AIChE Journal 47, no 7 (juillet 2001) : 1571–80. http://dx.doi.org/10.1002/aic.690470710.
Texte intégralBaes, Aloysius U., Tetsuji Okuda, Wataru Nishijima, Eiji Shoto et Mitsumasa Okada. « Adsorption and ion exchange of some groundwater anion contaminants in an amine modified coconut coir ». Water Science and Technology 35, no 7 (1 avril 1997) : 89–95. http://dx.doi.org/10.2166/wst.1997.0264.
Texte intégralXue, Mei, Fen Rong Liu et Huan Liu. « Adsorption of Thiophene Out of Model Gasoline Using Metal Ion-Exchanged Zeolite ». Advanced Materials Research 391-392 (décembre 2011) : 945–49. http://dx.doi.org/10.4028/www.scientific.net/amr.391-392.945.
Texte intégralSomya, Amita. « Studies on Pectin-Tin(IV) Phosphate : A New Biopolymer Doped Hybrid Ion Exchanger, An Efficacious Ion Exchanger in Water Purification Process ». Asian Journal of Chemistry 35, no 5 (2023) : 1237–42. http://dx.doi.org/10.14233/ajchem.2023.27600.
Texte intégralTang, Yu Bin, Fang Yu, Fang Yan Chen et Cheng Chen. « Research on Adsorption of Pb2+ on to Microspheres Prepared by Rectorite and Humic Acid ». Advanced Materials Research 233-235 (mai 2011) : 1972–80. http://dx.doi.org/10.4028/www.scientific.net/amr.233-235.1972.
Texte intégralTran, Hoai-Lam, Maw-Suey Kuo, Wein-Duo Yang et Yu-Chang Huang. « Study on Modification of NaX Zeolites : The Cobalt (II)-Exchange Kinetics and Surface Property Changes under Thermal Treatment ». Journal of Chemistry 2016 (2016) : 1–7. http://dx.doi.org/10.1155/2016/1789680.
Texte intégralThèses sur le sujet "Adsorption and ion exchange"
Watkins, E. James. « Foulant adsorption onto ion exchange membranes ». Diss., Georgia Institute of Technology, 1999. http://hdl.handle.net/1853/7062.
Texte intégralLeonard, Danièle. « Adsorption of bile acids by ion-exchange resins ». Thesis, McGill University, 1989. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=74309.
Texte intégralIon-exchange resins were prepared by solid phase peptide synthesis with active sites chosen to resemble those of cholestyramine. They were produced by coupling 4-(aminomethyl)benzoic acid, 4-aminophenylacetic acid or 4-(aminomethyl)phenylacetic acid to the backbone. The ion-exchange resins were prepared both as primary amines and in the quaternized form. The cholestyramine-like sorbents were synthesized with systematic changes in the structure, to determine which structural parts of cholestyramine are involved in the adsorption process. As compared to cholestyramine, both sets of resins were remarkably ineffective in adsorbing bile acids in vitro. It was found that the nature of the backbone determines the accessibility to the active site; that the resins with the methylene group positioned between the phenyl group and the amino group have higher adsorption capacity for glycocholic acid; and that quaternization increases the adsorption capacity. The two latter observations indicate the importance of the basicity of the active site. Therefore, in cholestyramine, the backbone is such that it permits the transfer of ionic species and the quaternary ammonium group is involved in the interaction with bile acids.
Computer modelling showed that the cholestyramine pendants are close to one another and are separated by benzene rings, thus leaving too little space between them to allow a bile acid molecule to interact with the benzene rings. Therefore, the bile acids must interact with the quaternary ammonium group, leaving the bile acid molecule inside the cavity where they interact with one another to form micelles. The possible modes of interactions of bile acids with the synthesized resins are more numerous since the pendants are not as close together. (Abstract shortened by UMI.)
Arcanjo, Maria Rosiene Antunes. « Study on the adsorption of lactic acid by ion exchange chromatography ». Universidade Federal do CearÃ, 2014. http://www.teses.ufc.br/tde_busca/arquivo.php?codArquivo=13346.
Texte intégralCurrently the demand for renewable fuels has increased a lot. Thus, biodiesel is an alternative to oil and its derivatives, since its production is cheaper, there is a reduction in emissions, and is considered a renewable energy. Due to government incentives that drive the production of biodiesel, such fuel has been produced on a large scale. Of all the raw material used for producing biodiesel via transesterification, 10 % in mass is converted into glycerin, excess demand and absorption capacity of the current markets. In this context, it is of fundamental importance to develop alternative technologies and innovative at the same time to consume this surplus of crude glycerin. The production of lactic acid by hydrothermal conversion of glycerol is an alternative that adds significantly to the productivity of the biodiesel industry value, besides the production of an organic acid that is widely used industrially. This organic acid exists as two optical isomers, D - lactic acid and L- lactic acid. Presently, it has become an important monomer in the plastics industry, and polymerized biodegradable plastics such as poly-L- lactic acid and copolymers of lactic acid. Therefore, there is a continued interest in a more efficient process for the production of lactic acid as well as for their recovery and purification. Thus, the aim of this study was to conduct a study on the adsorption of lactic acid (derived from the conversion of glycerol resulting from biodiesel production) by ion exchange by Amberlite IRA 67 and IRA 96. Different eluents were evaluated at various concentrations in order to obtain a higher efficiency in removing lactic acid adsorbents studied. From the breakthrough curves obtained with different concentrations of lactic power (60-302 g/L) acid the adsorption isotherms were constructed at temperatures of 30 ÂC, 40 ÂC and 60 ÂC. With data from lactic acid concentration for each condition studied, became the model fit the Langmuir adsorption isotherm. Studies on the purification column fixed bed with mono-component solutions, binary mixtures and real mixture were also performed. It was concluded that the application of the proposed methodology for the purification of lactic acid in a fixed-bed column showed better results when the condition (temperature = 30 ÂC) was used in both adsorbents. As the Amberlite IRA 96, the adsorbent showed better performance in the adsorption of lactic acid.
Atualmente a procura por combustÃveis renovÃveis tem aumentado muito. Deste modo, o biodiesel surge como alternativa em relaÃÃo ao petrÃleo e seus derivados, jà que sua produÃÃo à mais barata, hà uma diminuiÃÃo na emissÃo de poluentes, e à considerada uma energia renovÃvel. Devido aos incentivos governamentais que impulsionam a produÃÃo de biodiesel, tal combustÃvel tem sido produzido em larga escala. De toda a matÃria-prima utilizada para a produÃÃo de biodiesel, atravÃs de transesterificaÃÃo, 10% em massa à convertida em glicerina, excedendo a demanda e capacidade de absorÃÃo dos mercados atuais. Neste contexto, à de fundamental importÃncia o desenvolvimento de tecnologias alternativas e ao mesmo tempo inovadoras para consumir este excedente de glicerina bruta. A produÃÃo de Ãcido lÃtico por conversÃo hidrotÃrmica do glicerol à uma alternativa que agrega um valor significativo para a produtividade da indÃstria de biodiesel, alÃm da produÃÃo de um Ãcido orgÃnico que à amplamente utilizado industrialmente. Esse Ãcido orgÃnico existe como dois isÃmeros Ãpticos, D-Ãcido lÃtico e L-Ãcido lÃtico. Atualmente, tem se tornado um importante monÃmero na indÃstria de plÃsticos, sendo polimerizado em plÃsticos biodegradÃveis, tal como poli-L-Ãcido lÃtico e seus copolÃmeros de Ãcido lÃtico. Por isso hà um interesse contÃnuo em um processo mais eficiente para a produÃÃo de Ãcido lÃtico, assim como para a sua recuperaÃÃo e purificaÃÃo. Dessa maneira, o objetivo desse trabalho foi realizar um estudo sobre a adsorÃÃo de Ãcido lÃtico (oriundo da conversÃo do glicerol resultante da produÃÃo do biodiesel) por cromatografia de troca iÃnica pelas resinas Amberlite IRA 67 e IRA 96. Foram avaliados diferentes eluentes em concentraÃÃes diversas, afim de se obter uma maior eficiÃncia na remoÃÃo de Ãcido lÃtico dos adsorventes estudados. A partir das curvas de ruptura obtidas com diferentes concentraÃÃes de alimentaÃÃo de Ãcido lÃtico (60-302 g/L) foram construÃdas as isotermas de adsorÃÃo nas temperaturas de 30ÂC, 40ÂC e 60ÂC. Com os dados de concentraÃÃo de Ãcido lÃtico para cada condiÃÃo estudada, fez-se o ajuste do modelo da isoterma de adsorÃÃo de Langmuir. Estudos sobre a purificaÃÃo em coluna de leito fixo com soluÃÃes monocomponentes, misturas binÃrias e mistura real tambÃm foram realizados. Concluiu-se que a aplicaÃÃo da metodologia proposta para purificaÃÃo do Ãcido lÃtico em coluna de leito fixo mostrou melhores resultados quando a condiÃÃo (temperatura=30ÂC) foi utilizada em ambos os adsorventes. Sendo a resina Amberlite IRA 96, o adsorvente que mostrou melhor eficiÃncia na adsorÃÃo do Ãcido lÃtico.
Bowley, Michael Allan. « The adsorption of colloidal material to highly porous ion-exchange resins ». Master's thesis, University of Cape Town, 1985. http://hdl.handle.net/11427/23171.
Texte intégralLöfgren, Rebecka. « Metal ion adsorption of highly mesoporous magnesium carbonate ». Thesis, Uppsala universitet, Nanoteknologi och funktionella material, 2019. http://urn.kb.se/resolve?urn=urn:nbn:se:uu:diva-388827.
Texte intégralBurcher-Jones, Cody Owen. « Mineralogical and ion-exchange leaching study of a Rare Earth Element (REE) bearing ion-adsorption clay deposit ». Master's thesis, Faculty of Engineering and the Built Environment, 2018. http://hdl.handle.net/11427/30161.
Texte intégralLangford, John F. Jr. « Effects of adsorbent structure and adsorption on transport phenomena in ion-exchange chromatography ». Access to citation, abstract and download form provided by ProQuest Information and Learning Company ; downloadable PDF file, 250 p, 2007. http://proquest.umi.com/pqdweb?did=1251904681&sid=1&Fmt=2&clientId=8331&RQT=309&VName=PQD.
Texte intégralDietrich, Theo Henry. « The removal of heavy metals from dilute aqueous streams by the use of ion exchange resins ». Thesis, Cape Technikon, 1998. http://hdl.handle.net/20.500.11838/887.
Texte intégralIon exchange resins are widely used to remove or concentrate heavy metals from aqueous solutions or slurries.This thesis attempts to properly evaluate the interaction between ion exchange resins and heavy metals at trace metal concentrations.The durability of the resins and their effectiveness in real slurries were also investigated. In this study, a chelating resin, as well as a cation, and anion exchange resin was contacted with aqueous solutions of heavy metals in both free and complexed form. Zinc, nickel and copper cyanide complexes were adsorbed onto the anion exchange resin, while the chelating and cation exchange resins were contacted with zinc and nickel nitrates, and cupric sulphate. All the tests were conducted in batch stirred tank reactors. All the metal cyanide complexes behaved in a similar manner when contacted with the anion exchange resins. These tests were p~rf0nned under variations in temperature, stirring speed, pH., ionic strength and . initial metal 90E~entrations. Fitting of a dual resistance model to the profiles for thetlptllk:e" of the complexes, show that both film diffusion and intraparticle diffusion rates were improved with an increase in temperature, and that film diffusion rates improved with an increase in stirring speed. A high ionic strength negatively affected equilibrium loading as well as diffusional rates.It was found that at these low concentrations, the diffusional rates improves with a decrease in the external metal concentration. A comparative study involving the chelating and cation·exchange resins were performed, during which the resins were contacted with the metals in free fonn. It was found that at high metal concentrations, the chelating resin induced a rate limiting effect, but at trace concentrations, this effect is virtually negated. Whereas the cation exchange resin exhibited little selectivity in adsorbing the metals, it was found that the chelating resin prefers the metals in the eu > Ni > Zn. The chelating resin proved to be no less durable then the cation exchange resin, and both slightly lost their ability to adsorb the metal cations as a result of the effects of an inert coarse sand slurry.Tests performed with a real ore leachate, showed the cation exchange resin to be efficient at a low pH , but also relatively non selective, since the adsorption of copper from the leachate was greatly reduced due to the presence of other heavy metals.
Chartrand, Zachary Guy. « The Selective Ion-Exchange Removal of Ammonia from Mining Wastewater ». Thesis, Université d'Ottawa / University of Ottawa, 2018. http://hdl.handle.net/10393/37543.
Texte intégralMarinetti, Andrea. « Recovery of Carboxylic acids from anaerobic fermented broth through ionic exchange processes ». Master's thesis, Alma Mater Studiorum - Università di Bologna, 2019.
Trouver le texte intégralLivres sur le sujet "Adsorption and ion exchange"
LeVan, M. Douglas. Adsorption and ion exchange. New York : McGraw-Hill, 2008.
Trouver le texte intégral1949-, Ausikaitis J. P., Myers Alan L. 1932-, Sweed Norman H. 1943-, American Institute of Chemical Engineers. Meeting et American Institute of Chemical Engineers. Group 2 (Diffusional Operations and Processes), dir. Adsorption and ion exchange : Recent developments. New York, N.Y : American Institute of Chemical Engineers, 1985.
Trouver le texte intégral1949-, LeVan M. Douglas, Knaebel Kent S. 1951-, Sircar Shivaji 1944-, Wankat Phillip C. 1944- et Bolden W. B, dir. Adsorption and ion exchange : Fundamentals and applications. New York, N.Y : American Institute of Chemical Engineers, 1988.
Trouver le texte intégral1936-, Ma Y. H., Ausikaitis J. P. 1949- et National Meeting of AIChE (1987 : Houston, Tex.), dir. Recent progress in adsorption and ion exchange. New York, N.Y : American Institute of Chemical Engineers, 1987.
Trouver le texte intégralNational Risk Management Research Laboratory (U.S.). Sustainable Technology Division., dir. Metals Adsorption Workshop : May 5-6, 1998, Cincinnati, Ohio. Cincinnati, OH : Sustainable Technology Division, National Risk Management Research Laboratory, Office of Research and Development, U.S. Environmental Protection Agency, 1998.
Trouver le texte intégralNational Risk Management Research Laboratory (U.S.). Sustainable Technology Division, dir. Metals Adsorption Workshop : May 5-6, 1998, Cincinnati, Ohio. Cincinnati, OH : Sustainable Technology Division, National Risk Management Research Laboratory, Office of Research and Development, U.S. Environmental Protection Agency, 1998.
Trouver le texte intégralL, Pratt S., Thomas C. W, U.S. Nuclear Regulatory Commission. Division of Risk Analysis and Applications. et Pacific Northwest National Laboratory (U.S.), dir. Adsorption and desorption behavior of selected 10 CFR Part 61 radionuclides from ion exchange resin by waters of different chemical composition. Washington, DC : Division of Risk Analysis and Applications, Office of Nuclear Regulatory Research, U.S. Nuclear Regulatory Commission, 2000.
Trouver le texte intégralVolesky, Bohumil. Sorption and biosorption. St. Lambert, Québec : BV Sorbex, 2003.
Trouver le texte intégralUlewicz, Małgorzata. Separacja jonów metali nieżelaznych w procesie transportu przez ciekłe membrany zawierające związki makrocykliczne. Częstochowa : Wydawn. Wydziału Inżynierii Procesowej, Materiałowej i Fizyki Stosowanej, Politechniki Częstochowskiej, 2011.
Trouver le texte intégralHelfferich, Friedrich G. Ion exchange. New York : Dover Publications, 1995.
Trouver le texte intégralChapitres de livres sur le sujet "Adsorption and ion exchange"
Mersmann, Alfons, Matthias Kind et Johann Stichlmair. « Adsorption, Chromatography, Ion Exchange ». Dans Thermal Separation Technology, 483–560. Berlin, Heidelberg : Springer Berlin Heidelberg, 2011. http://dx.doi.org/10.1007/978-3-642-12525-6_9.
Texte intégralTang, L. X., R. W. Lovitt, J. R. Conder et M. G. Jones. « Determination of Adsorption/Desorption Kinetics of Proteins on Ion Exchange Media ». Dans Ion Exchange Advances, 222–28. Dordrecht : Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_29.
Texte intégralAbe, Mitsuo, Yasuo Tanaka et Masamichi Tsuji. « Adsorption and Desorption Behaviour of Arsenic Compounds on Various Inorganic Ion Exchangers ». Dans Ion Exchange Advances, 326–33. Dordrecht : Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_43.
Texte intégralStreat, M., et J. K. Nair. « Adsorption of Trace Metals on Modified Activated Carbons ». Dans Ion Exchange Advances, 264–71. Dordrecht : Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_35.
Texte intégralde Andrade, Deborah C., João M. M. Henrique, E. V. Dos Santos et Fernanda L. de Souza. « Adsorption and Ion Exchange Permeable Reactive Barriers ». Dans Environmental Pollution, 343–67. Cham : Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-68140-1_14.
Texte intégralSilva, F. R. C., et C. C. Santana. « Adsorption of Inulinases in Ion-Exchange Columns ». Dans Twenty-First Symposium on Biotechnology for Fuels and Chemicals, 1063–78. Totowa, NJ : Humana Press, 2000. http://dx.doi.org/10.1007/978-1-4612-1392-5_83.
Texte intégralScott, J. A., S. J. Palmer et G. K. Sage. « Metal Adsorption by Bacterial Capsular Polysaccharide Coatings ». Dans Recent Developments in Ion Exchange, 332–38. Dordrecht : Springer Netherlands, 1987. http://dx.doi.org/10.1007/978-94-009-3449-8_32.
Texte intégralMorton, Philip H., et Andrew Lyddiatt. « Direct Recovery of Protein Products from Whole Fermentation Broths : A role for ion exchange adsorption in fluidised beds. » Dans Ion Exchange Advances, 237–44. Dordrecht : Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_31.
Texte intégralInoue, Katsutoshi, Kazuharu Yoshizuka et Yoshinari Baba. « Ion Exchange Adsorption of Metal Ions on Amine and Pyridine Types of Chelating Resins ». Dans Recent Developments in Ion Exchange, 255–63. Dordrecht : Springer Netherlands, 1990. http://dx.doi.org/10.1007/978-94-009-0777-5_24.
Texte intégralNoble, J. B., G. H. Cowan, W. P. Sweetenham et H. A. Chase. « The Application of Modelling to the Prediction of Adsorption in Batch-Stirred Tanks, Packed-Bed and Fluidised-Bed Columns in Biotechnological Separations ». Dans Ion Exchange Advances, 214–21. Dordrecht : Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_28.
Texte intégralActes de conférences sur le sujet "Adsorption and ion exchange"
Chan, K. C., Christopher Y. H. Chao, G. N. Sze-To et K. S. Hui. « Development of New Zeolite 13X/CaCl2 Composite Adsorbent for Air-Conditioning Application ». Dans ASME 2011 5th International Conference on Energy Sustainability. ASMEDC, 2011. http://dx.doi.org/10.1115/es2011-54052.
Texte intégralZheng, Tingting, Qiang Gan, Jinxin Qian et Changgen Feng. « Thermodynamics of Pb2+ Adsorption on Amino Ion Exchange Fiber ». Dans 2014 International Conference on Materials Science and Energy Engineering (CMSEE 2014). WORLD SCIENTIFIC, 2015. http://dx.doi.org/10.1142/9789814678971_0012.
Texte intégralWu, Haoran, Shun Yao, Yan Wang et Hang Song. « Adsorption of Ionic Liquids from Cellulosic Hydrolysate by Ion-exchange Resin ». Dans 2015 Asia-Pacific Energy Equipment Engineering Research Conference. Paris, France : Atlantis Press, 2015. http://dx.doi.org/10.2991/ap3er-15.2015.61.
Texte intégralSych, Oleksandr, Svyatoslav Vuchkan, Hanna Vasylyeva, Myroslav Karbovanets et Marianna Yevych. « THE USE OF NATURAL ZEOLITES OF TRANSCARPATHIA TO SOLVE ENVIRONMENTAL PROBLEMS ». Dans 22nd SGEM International Multidisciplinary Scientific GeoConference 2022. STEF92 Technology, 2022. http://dx.doi.org/10.5593/sgem2022v/6.2/s24.05.
Texte intégralAziz, Muhammad Afiq Afandi Abdul, Malek Selamat, Ismail Ibrahim, Hamdan Yahya et Aspaniza Ahmad. « Enhancing ion – Exchange leaching of rare earth elements from Malaysian ion adsorption clay sources by using commercial surfactant ». Dans INTERNATIONAL CONFERENCE ON ELECTRONICS, ENGINEERING PHYSICS, AND EARTH SCIENCE. AIP Publishing, 2024. http://dx.doi.org/10.1063/5.0193105.
Texte intégralCurvelo Santana, José Carlos, Joana Paula Menezes Biazus, Roberto Rodrigues de Souza et ELIAS BASILE TAMBOURGI. « ION-EXCHANGE EFFECT ON THE PURIFICATION OF AMYLASES FROM MAIZE MALT BY EXPANDED BED ADSORPTION ». Dans Simpósio Nacional de Bioprocessos e Simpósio de Hidrólise Enzimática de Biomassa. Campinas - SP, Brazil : Galoá, 2015. http://dx.doi.org/10.17648/sinaferm-2015-34116.
Texte intégralEnascuta, Cristina-Emanuela, Elena-Emilia Oprescu, Catalina Calin, Gabriel Vasilievici et Cristina Popa. « ADSORPTION OF NITRATE ON MAGNETIC MICROALGAL BIOCHAR ». Dans 22nd SGEM International Multidisciplinary Scientific GeoConference 2022. STEF92 Technology, 2022. http://dx.doi.org/10.5593/sgem2022/6.1/s25.07.
Texte intégralDzinun, Hazlini, et Mohd Hafiz Dzarfan Othman. « A Review on Modification of Zeolite for Photocatalytic Applications ». Dans Conference on Center of Diploma Studies (CeDS) 2020/1. Penerbit UTHM, 2020. http://dx.doi.org/10.30880/mari.2020.01.01.002.
Texte intégralJIANG, H., W. TANG, J. P. ZHANG, B. Y. ZHAO et Y. C. XIE. « STUDIES ON THE ADSORPTION PROPERTIES OF ION-EXCHANGED LOW SILICA X ZEOLITE ». Dans Proceedings of the Third Pacific Basin Conference. WORLD SCIENTIFIC, 2003. http://dx.doi.org/10.1142/9789812704320_0022.
Texte intégralYOSHIDA, HIROYUKI, et WILMER GALINADA. « ADSORPTION OF H3PO4, NaH2PO4, Na2HPO4, AND Na3PO4 ON STRONGLY BASIC ION EXCHANGER ». Dans Proceedings of the Second Pacific Basin Conference. WORLD SCIENTIFIC, 2000. http://dx.doi.org/10.1142/9789812793331_0139.
Texte intégralRapports d'organisations sur le sujet "Adsorption and ion exchange"
Mattigod, Shas V., Elizabeth C. Golovich, Dawn M. Wellman, Elsa A. Cordova et Ronald M. Smith. Uranium Adsorption on Ion-Exchange Resins - Batch Testing. Office of Scientific and Technical Information (OSTI), décembre 2010. http://dx.doi.org/10.2172/1009765.
Texte intégralVorres, K. S. Ion exchange and adsorption on low rank coals for liquefaction. Office of Scientific and Technical Information (OSTI), septembre 1994. http://dx.doi.org/10.2172/10179944.
Texte intégralParker, Kent E., Elizabeth C. Golovich et Dawn M. Wellman. Iodine adsorption on ion-exchange resins and activated carbons : batch testing. Office of Scientific and Technical Information (OSTI), septembre 2014. http://dx.doi.org/10.2172/1163822.
Texte intégralWaisner, Scott, Victor Medina, Charles Ellison, Jose Mattei-Sosa, John Brasher, Jacob Lalley et Christopher Griggs. Design, construction, and testing of the PFAS Effluent Treatment System (PETS), a mobile ion exchange–based system for the treatment of per-, poly-fluorinated alkyl substances (PFAS) contaminated water. Engineer Research and Development Center (U.S.), mars 2022. http://dx.doi.org/10.21079/11681/43823.
Texte intégralBalmer, M. L., et B. C. Bunker. Inorganic ion exchange evaluation and design : Silicotitanate ion exchange waste conversion. Office of Scientific and Technical Information (OSTI), mars 1995. http://dx.doi.org/10.2172/85908.
Texte intégralWallace, R. M. Ion Exchange Membrane Processes. Office of Scientific and Technical Information (OSTI), octobre 2002. http://dx.doi.org/10.2172/804675.
Texte intégralYen, S. N., J. A. Pike, R. A. Jacobs, M. R. Poirier, B. M. Sahawneh et R. K. Leugemors. Evaluation of Alternate Ion Exchange Designs for CST Non-Elutable Ion Exchange Process. Office of Scientific and Technical Information (OSTI), juin 2001. http://dx.doi.org/10.2172/782667.
Texte intégralJPH Sukamto, ML Lilga et RK Orth. Electrically Switched Cesium Ion Exchange. Office of Scientific and Technical Information (OSTI), octobre 1998. http://dx.doi.org/10.2172/1118.
Texte intégralLilga, M. A., R. J. Orth, J. P. H. Sukamto, D. T. Schwartz, S. M. Haight et J. D. Genders. Electrically switched cesium ion exchange. Office of Scientific and Technical Information (OSTI), avril 1997. http://dx.doi.org/10.2172/495697.
Texte intégralDuhn, E. F. Ion exchange technology assessment report. Office of Scientific and Technical Information (OSTI), janvier 1992. http://dx.doi.org/10.2172/6420524.
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