Auswahl der wissenschaftlichen Literatur zum Thema „Adsorption and ion exchange“
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Zeitschriftenartikel zum Thema "Adsorption and ion exchange"
Song, Fujiao, Yan Cao, Yunxia Zhao, Ruiyu Jiang, Qi Xu, Jinlong Yan und Qin Zhong. „Ion-Exchanged ZIF-67 Synthesized by One-Step Method for Enhancement of CO2 Adsorption“. Journal of Nanomaterials 2020 (17.02.2020): 1–11. http://dx.doi.org/10.1155/2020/1508574.
Der volle Inhalt der QuelleTheodoridou, E., A. D. Jannakoudakis, P. D. Jannakoudakis und 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, Nr. 12 (01.12.1991): 1881–85. http://dx.doi.org/10.1139/v91-272.
Der volle Inhalt der QuelleNoor, Ehteram A., und 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.
Der volle Inhalt der QuelleWu, Yu-Chi, Yu-Hong Wei und Ho-Shing Wu. „Adsorption and Desorption Behavior of Ectoine Using Dowex® HCR-S Ion-Exchange Resin“. Processes 9, Nr. 11 (18.11.2021): 2068. http://dx.doi.org/10.3390/pr9112068.
Der volle Inhalt der QuelleWesselingh, J. A., und J. C. Bosma. „Protein ion-exchange adsorption kinetics“. AIChE Journal 47, Nr. 7 (Juli 2001): 1571–80. http://dx.doi.org/10.1002/aic.690470710.
Der volle Inhalt der QuelleBaes, Aloysius U., Tetsuji Okuda, Wataru Nishijima, Eiji Shoto und Mitsumasa Okada. „Adsorption and ion exchange of some groundwater anion contaminants in an amine modified coconut coir“. Water Science and Technology 35, Nr. 7 (01.04.1997): 89–95. http://dx.doi.org/10.2166/wst.1997.0264.
Der volle Inhalt der QuelleXue, Mei, Fen Rong Liu und Huan Liu. „Adsorption of Thiophene Out of Model Gasoline Using Metal Ion-Exchanged Zeolite“. Advanced Materials Research 391-392 (Dezember 2011): 945–49. http://dx.doi.org/10.4028/www.scientific.net/amr.391-392.945.
Der volle Inhalt der QuelleSomya, 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, Nr. 5 (2023): 1237–42. http://dx.doi.org/10.14233/ajchem.2023.27600.
Der volle Inhalt der QuelleTang, Yu Bin, Fang Yu, Fang Yan Chen und 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.
Der volle Inhalt der QuelleTran, Hoai-Lam, Maw-Suey Kuo, Wein-Duo Yang und 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.
Der volle Inhalt der QuelleDissertationen zum Thema "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.
Der volle Inhalt der QuelleLeonard, 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.
Der volle Inhalt der QuelleIon-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.
Der volle Inhalt der QuelleCurrently 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.
Der volle Inhalt der QuelleLöfgren, 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.
Der volle Inhalt der QuelleBurcher-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.
Der volle Inhalt der QuelleLangford, 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.
Der volle Inhalt der QuelleDietrich, 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.
Der volle Inhalt der QuelleIon 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.
Der volle Inhalt der QuelleMarinetti, Andrea. „Recovery of Carboxylic acids from anaerobic fermented broth through ionic exchange processes“. Master's thesis, Alma Mater Studiorum - Università di Bologna, 2019.
Den vollen Inhalt der Quelle findenBücher zum Thema "Adsorption and ion exchange"
LeVan, M. Douglas. Adsorption and ion exchange. New York: McGraw-Hill, 2008.
Den vollen Inhalt der Quelle finden1949-, Ausikaitis J. P., Myers Alan L. 1932-, Sweed Norman H. 1943-, American Institute of Chemical Engineers. Meeting und American Institute of Chemical Engineers. Group 2 (Diffusional Operations and Processes), Hrsg. Adsorption and ion exchange: Recent developments. New York, N.Y: American Institute of Chemical Engineers, 1985.
Den vollen Inhalt der Quelle finden1949-, LeVan M. Douglas, Knaebel Kent S. 1951-, Sircar Shivaji 1944-, Wankat Phillip C. 1944- und Bolden W. B, Hrsg. Adsorption and ion exchange: Fundamentals and applications. New York, N.Y: American Institute of Chemical Engineers, 1988.
Den vollen Inhalt der Quelle finden1936-, Ma Y. H., Ausikaitis J. P. 1949- und National Meeting of AIChE (1987 : Houston, Tex.), Hrsg. Recent progress in adsorption and ion exchange. New York, N.Y: American Institute of Chemical Engineers, 1987.
Den vollen Inhalt der Quelle findenNational Risk Management Research Laboratory (U.S.). Sustainable Technology Division., Hrsg. 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.
Den vollen Inhalt der Quelle findenNational Risk Management Research Laboratory (U.S.). Sustainable Technology Division, Hrsg. 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.
Den vollen Inhalt der Quelle findenL, Pratt S., Thomas C. W, U.S. Nuclear Regulatory Commission. Division of Risk Analysis and Applications. und Pacific Northwest National Laboratory (U.S.), Hrsg. 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.
Den vollen Inhalt der Quelle findenVolesky, Bohumil. Sorption and biosorption. St. Lambert, Québec: BV Sorbex, 2003.
Den vollen Inhalt der Quelle findenUlewicz, 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.
Den vollen Inhalt der Quelle findenHelfferich, Friedrich G. Ion exchange. New York: Dover Publications, 1995.
Den vollen Inhalt der Quelle findenBuchteile zum Thema "Adsorption and ion exchange"
Mersmann, Alfons, Matthias Kind und Johann Stichlmair. „Adsorption, Chromatography, Ion Exchange“. In Thermal Separation Technology, 483–560. Berlin, Heidelberg: Springer Berlin Heidelberg, 2011. http://dx.doi.org/10.1007/978-3-642-12525-6_9.
Der volle Inhalt der QuelleTang, L. X., R. W. Lovitt, J. R. Conder und M. G. Jones. „Determination of Adsorption/Desorption Kinetics of Proteins on Ion Exchange Media“. In Ion Exchange Advances, 222–28. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_29.
Der volle Inhalt der QuelleAbe, Mitsuo, Yasuo Tanaka und Masamichi Tsuji. „Adsorption and Desorption Behaviour of Arsenic Compounds on Various Inorganic Ion Exchangers“. In Ion Exchange Advances, 326–33. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_43.
Der volle Inhalt der QuelleStreat, M., und J. K. Nair. „Adsorption of Trace Metals on Modified Activated Carbons“. In Ion Exchange Advances, 264–71. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_35.
Der volle Inhalt der Quellede Andrade, Deborah C., João M. M. Henrique, E. V. Dos Santos und Fernanda L. de Souza. „Adsorption and Ion Exchange Permeable Reactive Barriers“. In Environmental Pollution, 343–67. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-68140-1_14.
Der volle Inhalt der QuelleSilva, F. R. C., und C. C. Santana. „Adsorption of Inulinases in Ion-Exchange Columns“. In 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.
Der volle Inhalt der QuelleScott, J. A., S. J. Palmer und G. K. Sage. „Metal Adsorption by Bacterial Capsular Polysaccharide Coatings“. In Recent Developments in Ion Exchange, 332–38. Dordrecht: Springer Netherlands, 1987. http://dx.doi.org/10.1007/978-94-009-3449-8_32.
Der volle Inhalt der QuelleMorton, Philip H., und Andrew Lyddiatt. „Direct Recovery of Protein Products from Whole Fermentation Broths: A role for ion exchange adsorption in fluidised beds.“ In Ion Exchange Advances, 237–44. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_31.
Der volle Inhalt der QuelleInoue, Katsutoshi, Kazuharu Yoshizuka und Yoshinari Baba. „Ion Exchange Adsorption of Metal Ions on Amine and Pyridine Types of Chelating Resins“. In Recent Developments in Ion Exchange, 255–63. Dordrecht: Springer Netherlands, 1990. http://dx.doi.org/10.1007/978-94-009-0777-5_24.
Der volle Inhalt der QuelleNoble, J. B., G. H. Cowan, W. P. Sweetenham und 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“. In Ion Exchange Advances, 214–21. Dordrecht: Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2864-3_28.
Der volle Inhalt der QuelleKonferenzberichte zum Thema "Adsorption and ion exchange"
Chan, K. C., Christopher Y. H. Chao, G. N. Sze-To und K. S. Hui. „Development of New Zeolite 13X/CaCl2 Composite Adsorbent for Air-Conditioning Application“. In ASME 2011 5th International Conference on Energy Sustainability. ASMEDC, 2011. http://dx.doi.org/10.1115/es2011-54052.
Der volle Inhalt der QuelleZheng, Tingting, Qiang Gan, Jinxin Qian und Changgen Feng. „Thermodynamics of Pb2+ Adsorption on Amino Ion Exchange Fiber“. In 2014 International Conference on Materials Science and Energy Engineering (CMSEE 2014). WORLD SCIENTIFIC, 2015. http://dx.doi.org/10.1142/9789814678971_0012.
Der volle Inhalt der QuelleWu, Haoran, Shun Yao, Yan Wang und Hang Song. „Adsorption of Ionic Liquids from Cellulosic Hydrolysate by Ion-exchange Resin“. In 2015 Asia-Pacific Energy Equipment Engineering Research Conference. Paris, France: Atlantis Press, 2015. http://dx.doi.org/10.2991/ap3er-15.2015.61.
Der volle Inhalt der QuelleSych, Oleksandr, Svyatoslav Vuchkan, Hanna Vasylyeva, Myroslav Karbovanets und Marianna Yevych. „THE USE OF NATURAL ZEOLITES OF TRANSCARPATHIA TO SOLVE ENVIRONMENTAL PROBLEMS“. In 22nd SGEM International Multidisciplinary Scientific GeoConference 2022. STEF92 Technology, 2022. http://dx.doi.org/10.5593/sgem2022v/6.2/s24.05.
Der volle Inhalt der QuelleAziz, Muhammad Afiq Afandi Abdul, Malek Selamat, Ismail Ibrahim, Hamdan Yahya und Aspaniza Ahmad. „Enhancing ion – Exchange leaching of rare earth elements from Malaysian ion adsorption clay sources by using commercial surfactant“. In INTERNATIONAL CONFERENCE ON ELECTRONICS, ENGINEERING PHYSICS, AND EARTH SCIENCE. AIP Publishing, 2024. http://dx.doi.org/10.1063/5.0193105.
Der volle Inhalt der QuelleCurvelo Santana, José Carlos, Joana Paula Menezes Biazus, Roberto Rodrigues de Souza und ELIAS BASILE TAMBOURGI. „ION-EXCHANGE EFFECT ON THE PURIFICATION OF AMYLASES FROM MAIZE MALT BY EXPANDED BED ADSORPTION“. In 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.
Der volle Inhalt der QuelleEnascuta, Cristina-Emanuela, Elena-Emilia Oprescu, Catalina Calin, Gabriel Vasilievici und Cristina Popa. „ADSORPTION OF NITRATE ON MAGNETIC MICROALGAL BIOCHAR“. In 22nd SGEM International Multidisciplinary Scientific GeoConference 2022. STEF92 Technology, 2022. http://dx.doi.org/10.5593/sgem2022/6.1/s25.07.
Der volle Inhalt der QuelleDzinun, Hazlini, und Mohd Hafiz Dzarfan Othman. „A Review on Modification of Zeolite for Photocatalytic Applications“. In Conference on Center of Diploma Studies (CeDS) 2020/1. Penerbit UTHM, 2020. http://dx.doi.org/10.30880/mari.2020.01.01.002.
Der volle Inhalt der QuelleJIANG, H., W. TANG, J. P. ZHANG, B. Y. ZHAO und Y. C. XIE. „STUDIES ON THE ADSORPTION PROPERTIES OF ION-EXCHANGED LOW SILICA X ZEOLITE“. In Proceedings of the Third Pacific Basin Conference. WORLD SCIENTIFIC, 2003. http://dx.doi.org/10.1142/9789812704320_0022.
Der volle Inhalt der QuelleYOSHIDA, HIROYUKI, und WILMER GALINADA. „ADSORPTION OF H3PO4, NaH2PO4, Na2HPO4, AND Na3PO4 ON STRONGLY BASIC ION EXCHANGER“. In Proceedings of the Second Pacific Basin Conference. WORLD SCIENTIFIC, 2000. http://dx.doi.org/10.1142/9789812793331_0139.
Der volle Inhalt der QuelleBerichte der Organisationen zum Thema "Adsorption and ion exchange"
Mattigod, Shas V., Elizabeth C. Golovich, Dawn M. Wellman, Elsa A. Cordova und Ronald M. Smith. Uranium Adsorption on Ion-Exchange Resins - Batch Testing. Office of Scientific and Technical Information (OSTI), Dezember 2010. http://dx.doi.org/10.2172/1009765.
Der volle Inhalt der QuelleVorres, K. S. Ion exchange and adsorption on low rank coals for liquefaction. Office of Scientific and Technical Information (OSTI), September 1994. http://dx.doi.org/10.2172/10179944.
Der volle Inhalt der QuelleParker, Kent E., Elizabeth C. Golovich und Dawn M. Wellman. Iodine adsorption on ion-exchange resins and activated carbons: batch testing. Office of Scientific and Technical Information (OSTI), September 2014. http://dx.doi.org/10.2172/1163822.
Der volle Inhalt der QuelleWaisner, Scott, Victor Medina, Charles Ellison, Jose Mattei-Sosa, John Brasher, Jacob Lalley und 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.), März 2022. http://dx.doi.org/10.21079/11681/43823.
Der volle Inhalt der QuelleBalmer, M. L., und B. C. Bunker. Inorganic ion exchange evaluation and design: Silicotitanate ion exchange waste conversion. Office of Scientific and Technical Information (OSTI), März 1995. http://dx.doi.org/10.2172/85908.
Der volle Inhalt der QuelleWallace, R. M. Ion Exchange Membrane Processes. Office of Scientific and Technical Information (OSTI), Oktober 2002. http://dx.doi.org/10.2172/804675.
Der volle Inhalt der QuelleYen, S. N., J. A. Pike, R. A. Jacobs, M. R. Poirier, B. M. Sahawneh und R. K. Leugemors. Evaluation of Alternate Ion Exchange Designs for CST Non-Elutable Ion Exchange Process. Office of Scientific and Technical Information (OSTI), Juni 2001. http://dx.doi.org/10.2172/782667.
Der volle Inhalt der QuelleJPH Sukamto, ML Lilga und RK Orth. Electrically Switched Cesium Ion Exchange. Office of Scientific and Technical Information (OSTI), Oktober 1998. http://dx.doi.org/10.2172/1118.
Der volle Inhalt der QuelleLilga, M. A., R. J. Orth, J. P. H. Sukamto, D. T. Schwartz, S. M. Haight und J. D. Genders. Electrically switched cesium ion exchange. Office of Scientific and Technical Information (OSTI), April 1997. http://dx.doi.org/10.2172/495697.
Der volle Inhalt der QuelleDuhn, E. F. Ion exchange technology assessment report. Office of Scientific and Technical Information (OSTI), Januar 1992. http://dx.doi.org/10.2172/6420524.
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