Bibliographies thématiques / Solvent-solvent

Littérature scientifique sur le sujet « Solvent-solvent »

Auteur : Grafiati
Publié le 18 mai 2024

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Articles de revues sur le sujet "Solvent-solvent"

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Zhou, Shi-Qi. « Influence of Solvent-Solvent and Solute-Solvent Interaction Properties on Solvent-Mediated Potential ». Communications in Theoretical Physics 44, no 2 (août 2005) : 365–70. http://dx.doi.org/10.1088/6102/44/2/365.

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Grigorescu, Gabriela, Silvia Ioan et Bogdan C. Simionescu. « Solvent/solvent/polymer ternary systems ». Polymer Bulletin 31, no 1 (juillet 1993) : 123–27. http://dx.doi.org/10.1007/bf00298774.

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Chan, Joel, Joseph Chee Chang, Tom Hope, Dafna Shahaf et Aniket Kittur. « SOLVENT ». Proceedings of the ACM on Human-Computer Interaction 2, CSCW (novembre 2018) : 1–21. http://dx.doi.org/10.1145/3274300.

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Luca, Alfio A. Tamburello, Philippe Hébert, Pierre F. Brevet et Hubert H. Girault. « Surface second-harmonic generation at air/solvent and solvent/solvent interfaces ». J. Chem. Soc., Faraday Trans. 91, no 12 (1995) : 1763–68. http://dx.doi.org/10.1039/ft9959101763.

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da Silva, Domingas C., Ingrid Ricken, Marcos A. do R. Silva et Vanderlei G. Machado. « Solute-solvent and solvent-solvent interactions in the preferential solvation of Brooker's merocyanine in binary solvent mixtures ». Journal of Physical Organic Chemistry 15, no 7 (2002) : 420–27. http://dx.doi.org/10.1002/poc.519.

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Souvignet, Isabelle, et Susan V. Olesik. « Solvent-Solvent and Solute-Solvent Interactions in Liquid Methanol/Carbon Dioxide Mixtures ». Journal of Physical Chemistry 99, no 45 (novembre 1995) : 16800–16803. http://dx.doi.org/10.1021/j100045a048.

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Vrentas, J. S., C. M. Vrentas et N. Faridi. « Effect of Solvent Size on Solvent Self-Diffusion in Polymer−Solvent Systems ». Macromolecules 29, no 9 (janvier 1996) : 3272–76. http://dx.doi.org/10.1021/ma9511356.

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Villacampa, Manuel, Elena Diaz de Apodaca, Jose R. Quintana et Issa Katime. « Diblock Copolymer Micelles in Solvent Binary Mixtures. 2. Selective Solvent/Good Solvent ». Macromolecules 28, no 12 (juin 1995) : 4144–49. http://dx.doi.org/10.1021/ma00116a014.

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Kohl, Stephan W., Frank W. Heinemann, Markus Hummert, Walter Bauer et Andreas Grohmann. « Solvent dependent reactivity : solvent activation vs. solvent coordination in alkylphosphane iron complexes ». Dalton Transactions, no 47 (2006) : 5583. http://dx.doi.org/10.1039/b610792c.

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YAMAGUCHI, T., et Y. KIMURA. « Effects of solute-solvent and solvent-solvent attractive interactions on solute diffusion ». Molecular Physics 98, no 19 (10 octobre 2000) : 1553–63. http://dx.doi.org/10.1080/00268970009483361.

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Thèses sur le sujet "Solvent-solvent"

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Chun-Te, Lin Justin. « Organic solvent nanofiltration membrane cascades for solvent exchange and purification ». Thesis, Imperial College London, 2008. http://hdl.handle.net/10044/1/11977.

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Męcfel-Marczewski, Joanna. « Self Incompatible Solvent ». Doctoral thesis, Universitätsbibliothek Chemnitz, 2010. http://nbn-resolving.de/urn:nbn:de:bsz:ch1-201001195.

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In dieser Arbeit wird das neue Prinzip der „Selbstinkompatiblen Lösungsmittel“ vorgestellt. Es wird theoretisch abgeleitet, dass eine Mischung aus zwei Substanzen mit ungünstigen Wechselwirkungen bereitwillig eine weitere Substanz aufnehmen sollte, die diese ungünstigen Wechselwirkungen durch Verdünnen vermindert. Dies sollte umso stärker ausgeprägt sein, je ungünstiger die Wechselwirkungen zwischen den beiden ersten Substanzen sind. Da sich jedoch Substanzen mit sehr ungünstigen Wechselwirkungen physikalisch nicht mischen, entstand die Idee, diese Substanzen durch eine kovalente Bindung aneinander zu binden. Ein solches Molekül, das aus zwei inkompatiblen Hälften besteht, wird im Folgendem Selbstinkompatibles Lösungsmittel genannt. Die in dieser Arbeit gewählten Substanzen zeigen mäßige Inkompatibilität, deshalb ist ein Vergleich zwischen einfachen physikalischen Mischungen und kovalent verknüpften Molekülhälften noch möglich. Dieses Prinzip wird für binäre und ternäre Mischungen quantitativ berechnet und experimentell in drei Serien von Experimenten bestätigt: i) unter Verwendung von Lösungskalorimetrie und Bestimmung der Wechselwirkungsparameter zwischen Komponente 3 und einer bereits hergestellt physikalischen binären Mischung aus Komponente 1 und 2, ii) unter Verwendung von Lösungskalorimetrie und Bestimmung der Wechselwirkungsparameter zwischen Komponente 3 und den selbstinkompatiblen Losungsmitteln, die den in (i) gewählten Mischungen entsprechen und iii) aus der Sättigungslöslichkeit der Komponente 3 in den entsprechenden selbstinkompatiblen Lösungsmitteln. In diesen drei verschiedenen Messserien wird stets der gleichen Trend beobachtet: Die Selbstinkompatibilität eines Lösungsmittels begünstigt den Lösevorgang
In this thesis a new principle of Self Incompatible Solvent is introduced. It is shown theoretically that a preexisting mixture of two substances (compound 1 and 2) with unfavorable interactions will readily dissolve a third compound because it diminishes the unfavorable interaction between the compound 1 and 2 by dilution. This behavior should be the stronger the more unfavorable the interactions between compound 1 and 2 are. However, substances with strong unfavorable interactions will not mix. Therefore the idea pursued here is to enforce the desired preexisting mixture for example by linking compound 1 covalently to compound 2. Such a molecule that is composed of two incompatible parts is called Self Incompatible Solvent in this work. In this thesis examples of incompatible compounds that show moderate incompatibility are chosen, therefore it was possible to do a comparison between simple physical mixtures and covalently linked incompatible molecules. The theoretical prediction of the theory is compared with experiments. This principle is calculated quantitatively for binary and ternary mixtures and compared with the experimental results in three distinct series of experiments: i) by using solution calorimetry and calculation of the interaction parameters between compounds 3 and the preexisting binary mixture of compound 1 and 2, ii) by using solution calorimetry and calculation of the interaction parameters between compound 3 and the Self Incompatible Solvent that correspond to the mixtures used in (i) and iii) from the saturation solubility of compound 3 in the Self Incompatible Solvent. The results obtained from the theoretical prediction and these obtained from the three different series of experiments show the same trend: the self incompatibility of the solvent improves the dissolution process
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Rodarte, Alma Isabel Marín. « Predispersed solvent extraction ». Thesis, Virginia Tech, 1988. http://hdl.handle.net/10919/45173.

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A new solvent extraction method has been developed for the extraction of metal and organic ions from very dilute aqueous solutions. The new method, which has been named Predispersed Solvent Extraction (POSE), is based on the principle that 1 there is no need to comminute both phases. All that is necessary is to comminute the solvent phase prior to contacting it with the feed. This is done by converting the solvent into aphrons, which are micron-sized globules encapsulated in a soapy film. Since the aphrons are so small, it takes a long time for the solvent to rise to the surface under the influence of gravity alone. Therefore, the separation is expedited by piggy-back flotation of the aphrons on specially prepared gas bubbles, which are somewhat larger than aphrons and are called colloidal gas aphrons (CGA).

Copper, uranium and chromium ions, and alizarin yellow were extracted from very dilute aqueous solutions using PDSE. Tests were performed in a vertical glass column in both batch and continuous modes, and in a continuous horizontal trough. The new solvent extraction procedure worked very efficiently and very quickly under laboratory conditions. Higher than 99% extraction was achieved in many of the tests performed.


Master of Science
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Xu, Zhuang. « PARTITIONING OF SOLVENT MOLECULES SURROUNGDING POLYMER CHIANS IN SOLVENT-SHIFTING PROCESS ». University of Akron / OhioLINK, 2019. http://rave.ohiolink.edu/etdc/view?acc_num=akron1555690517286259.

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Wang, Nan. « CO2 Separation - from Aqueous Amine Solvent to Ionic Liquid-based solvent ». Licentiate thesis, Luleå tekniska universitet, Energivetenskap, 2021. http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-84244.

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Tarkan, Haci Mustafa. « Air-assisted solvent extraction ». Thesis, McGill University, 2006. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=102735.

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Air-Assisted Solvent Extraction (AASX) is a novel concept that uses a solvent-coated bubble to contact the organic and aqueous phases. The advantages over conventional solvent extraction (SX) are high solvent to aqueous contact area with reduced solvent volume and ease of phase separation due to the buoyancy imparted by the air core. This opens the way to treat dilute solutions (<1 g/L), such as effluents.
The novel contribution in this thesis is the production of solvent-coated bubbles by exploiting foaming properties of kerosene-based solvents.
The basic set-up is a chamber to generate foam which is injected through a capillary (orifice diameter 2.5 mm) to produce solvent-coated bubbles (ca. 4.4 mm) which release into the aqueous phase. This generates a solvent specific surface area of ca. 3000 cm-1, equivalent to solvent droplets of ca. 20 mum. Demonstrating the process on dilute Cu solutions (down to 25 mg/L), high aqueous/organic ratios (ca. 75:1) and extractions are achieved. The solvent readily disengages to accumulate at the surface of the aqueous solution.
The LIX family of extractants imparts some foaming to kerosene based solvents but D2EHPA does not. An extensive experimental program determined that 1.5 ppm silicone oil provided the necessary foaming action without affecting extraction or stripping efficiency, greatly expanding the range of solvents that can be used in AASX.
To complement the foam study, films on bubbles blown in solvent were examined by interferometry (film thickness) and infra-red spectroscopy (film composition). A "bound" solvent layer was identified with an initial thickness of ca. 2 - 4 mum, comparable to that determined indirectly (by counting bubbles in an AASX trial and measuring solvent consumption). The film composition appeared to be independent of film thickness as it decreased with time.
As a start to scaling up, the single bubble generation system was adapted by installing up to 8 horizontal capillaries. The bubbles generated were ca. 3.4 mm. Trials showed the multi-bubble set up was a simple replication of the individual bubble case. Preliminary analysis of kinetic data shows a fit to a first-order model.
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Brogan, Alex P. S. « Solvent-free liquid proteins ». Thesis, University of Bristol, 2012. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.573415.

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The work presented in this thesis represents the first investigation into the structure, function, and material properties of solvent-free liquids of globular proteins. Using myoglobin as an archetypal system, it has been shown that solvent-free liquid proteins can be synthesized through the engineering of protein surfaces with an organic corona made from polymer surfactants. These novel materials have been shown to be stoichiometric constructs of protein and surfactant, with respect to charge, that once lyophilized form liquid-like materials with unique thermal properties and very low water contents. The generality of the synthetic procedure was tested with the formation of solvent-free liquid proteins with a variety of surfactants. The result of which was that for myoglobin, there was a surfactant molecular weight limit of c. 700 mg.mL-1 with respect to the constructs that possessed liquid phases. The suggestion of which was that the corona had to extended from the surface of the protein enough to satisfy the interparticle interactions required to yield an accessible liquid state. Spectroscopic measurements were used to assess the secondary structure of proteins in the solvent-free liquid state. UV/Vis spectroscopy showed that the prosthetic heme of myoglobin (and hemoglobin) was retained in a structurally conserved environment, and CD spectroscopy showed the retention of a significant amount of secondary structure. These studies were extended to show that in the absence of water, proteins retained the ability to thermally denature and subsequently refold. This proceeded with extraordinary thermal stability, with solvent-free liquid myoglobin exhibiting a half denaturation temperature of c. 160 QC. With the persistence of secondary structure in solvent-free liquid proteins, the function of myoglobin was also investigated. It has been shown that in the absence of water, oxygen binding was achievable up to 125 QC.
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Sackin, Robert. « Solvent ingress in polymers ». Thesis, University of Surrey, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.326197.

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Bajpayee, Anurag. « Directional solvent extraction desalination ». Thesis, Massachusetts Institute of Technology, 2012. http://hdl.handle.net/1721.1/78539.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Mechanical Engineering, 2012.
"September 2012." Cataloged from PDF version of thesis.
Includes bibliographical references (p. 131-137).
World water supply is struggling to meet demand. Production of fresh water from the oceans could supply this demand almost indefinitely. As global energy consumption continues to increase, water and energy resources are getting closely intertwined, especially with regards to the water consumption and contamination in the unconventional oil and gas industry. Development of effective, affordable desalination and water treatment technologies is thus vital to meeting future demand, maintaining economic development, enabling continued growth of energy resources, and preventing regional and international conflict. We have developed a new low temperature, membrane-free desalination technology using directional solvents capable of extracting pure water from a contaminated solution without themselves dissolving in the recovered water. This method dissolves the water into a directional solvent by increasing its temperature, rejects salts and other contaminants, then recovers pure water by cooling back to ambient temperature, and re-uses the solvent. The directional solvents used here include soybean oil, hexanoic acid, decanoic acid, and octanoic acid with the last two observed to be the most effective. These fatty acids exhibit the required characteristics by having a hydrophilic carboxylic acid end which bonds to water molecules but the hydrophobic chain prevents the dissolution of water soluble salts as well the dissolution of the solvent in water. Directional solvent extraction may be considered a molecular-level desalination approach. Directional Solvent Extraction circumvents the need for membranes, uses simple, inexpensive machinery, and by operating at low temperatures offers the potential for using waste heat. This technique also lends itself well to treatment of feed waters over a wide range of total dissolved solids (TDS) levels and is one of the very few known techniques to extract water from saturated brines. We demonstrate >95% salt rejection for seawater TDS concentrations (35,000 ppm) as well as for oilfield produced water TDS concentrations (>100,000 ppm) and saturated brines (300,000 ppm) through a benchtop batch process, and recovery ratios as high as 85% for feed TDS of 35,000 ppm through a multi-stage batch process. We have also designed, constructed, and demonstrated a semi-continuous process prototype. The energy and economic analysis suggests that this technique could become an effective, affordable method for seawater desalination and for treatment of produced water from unconventional oil and gas extraction.
by Anurag Bajpayee.
Ph.D.
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TRUJILLO, REBOLLO ANDRES. « SOLVENT EXTRACTION OF MOLYBDENUM ». Diss., The University of Arizona, 1987. http://hdl.handle.net/10150/184009.

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The equilibrium and the kinetics of the reaction of Mo (VI) with 8-hydroxyquinoline; 8-hydroxyquinaldine; KELEX 100; LIX63; and LIX65N were studied by solvent extraction. From the equilibrium studies it was concluded that in weakly acidic solution (pH 5 to 6) the overall extraction reaction is (UNFORMATTED TABLE FOLLOWS) MoO₄²⁻ + 2H⁺ + 2HL(o) ↔ (K(ex)) MoO₂L ₂(o) + 2H₂O (TABLE ENDS) where HL is the monoprotic bidentate ligand, "(o)" refers to the organic phase, and K(,ex) is the extraction constant. It was concluded that the complexation reaction requires four protons to convert molybdate into molybdenyl. The extractions constants for LIX63 and 8-hydroxyquinaldine, corrected for the side reaction of the ligand and metal, are 10¹⁶·⁴³ and 10¹⁴·⁴⁰, respectively. In the case of LIX65N, the plot of log(D) vs pH has a maximum at pH 1.0, which was explained qualitatively in terms of protonation of the ligand and molybdic acid at low pH. The extraction constant for the reaction of molybdic acid and the neutral ligand was estimated to be 100,000. The kinetics of extraction Mo (VI) with LIX63, 8-hydroxyquinoline, 8-hydroxyquinaldine, and Kelex 100 were studied in this work. In all cases, except 8-hydroxyquinoline, the rate-determining step of the reaction involves the formation of a 1:1 complex between the neutral ligand and several Mo(VI) species differing in the degree of protonation. The rate-determining step for the reaction of Mo(VI) with 8-hydroxyquinoline involves the formation of a 1:2 complex. The rate constant for the reaction of HMoO₄ with 8-hydroxyquinaldine is four orders of magnitude smaller than the corresponding value reported in the literature for 8-hydroxyquinoline. The slower reaction with 8-hydroxyquinaldine was attributed to the presence of the methyl group next to the nitrogen atom of the ligand which hinders its binding with molybdenum in the rate determining step of the reaction.
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Livres sur le sujet "Solvent-solvent"

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Chadwick, Oliver, H. Ross Anderson, J. Martin Bland et John Ramsey. Solvent Abuse. New York, NY : Springer New York, 1991. http://dx.doi.org/10.1007/978-1-4612-3184-4.

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Barrett, Kevin. Solvent abuse. London : National Society for the Prevention of Cruelty to Children, 1986.

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Connolly, Sean. Solvent abuse. Oxford : Heinemann Library, 2003.

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Birmingham Advisory Committee on Solvent Abuse. Solvent abuse. Birmingham : BACSA, 1987.

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Bureau, National Children's, dir. Solvent misuse. London : National Children's Bureau, 1986.

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Birmingham Advisory Committee on Solvent Abuse., dir. Solvent abuse. Birmingham : Birmingham Advisory Committee on Solvent Abuse, 1989.

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Arlien-Søborg, Peter. Solvent neurotoxicity. Boca Raton, Fla : CRC Press, 1992.

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United States. Environmental Protection Agency. Office of Emergency and Remedial Response. et United States. Environmental Protection Agency. Office of Research and Development., dir. Solvent extraction. Washington, DC : U.S. Environmental Protection Agency, Office of Emergency and Remedial Response, 1994.

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Leahy, R. B. Laboratory comparison of solvent-loaded and solvent-free emulsions. Salem, OR : Oregon Dept. of Transportation, Research Group, 2000.

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Cocchiarella, Linda. Stoddard solvent toxicity. Atlanta, GA : U.S. Dept. of Health & Human Services, Public Health Service, Agency for Toxic Substances and Disease Registry, 1993.

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Chapitres de livres sur le sujet "Solvent-solvent"

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Gooch, Jan W. « Solvent ». Dans Encyclopedic Dictionary of Polymers, 678–82. New York, NY : Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_10886.

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Lynch, Gordon S., David G. Harrison, Hanjoong Jo, Charles Searles, Philippe Connes, Christopher E. Kline, C. Castagna et al. « Solvent ». Dans Encyclopedia of Exercise Medicine in Health and Disease, 800. Berlin, Heidelberg : Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-540-29807-6_3053.

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Gooch, Jan W. « Solvent ». Dans Encyclopedic Dictionary of Polymers, 924. New York, NY : Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_14823.

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Bährle-Rapp, Marina. « solvent ». Dans Springer Lexikon Kosmetik und Körperpflege, 520. Berlin, Heidelberg : Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-71095-0_9815.

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Mohamed, Khayet. « Bore Liquid : Solvent and Non-solvent ». Dans Encyclopedia of Membranes, 1–3. Berlin, Heidelberg : Springer Berlin Heidelberg, 2014. http://dx.doi.org/10.1007/978-3-642-40872-4_1180-4.

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Jones, David T., et David R. Woods. « Solvent Production ». Dans Clostridia, 105–44. Boston, MA : Springer US, 1989. http://dx.doi.org/10.1007/978-1-4757-9718-3_4.

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Medrzycka, Krystyna, et Sebastian Pastewski. « Solvent Sublation ». Dans Chemistry for the Protection of the Environment 2, 67–74. Boston, MA : Springer US, 1996. http://dx.doi.org/10.1007/978-1-4613-0405-0_8.

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Morgan, Michael M., MacDonald J. Christie, Luis De Lecea, Jason C. G. Halford, Josee E. Leysen, Warren H. Meck, Catalin V. Buhusi et al. « Solvent Abuse ». Dans Encyclopedia of Psychopharmacology, 1252. Berlin, Heidelberg : Springer Berlin Heidelberg, 2010. http://dx.doi.org/10.1007/978-3-540-68706-1_3587.

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Gooch, Jan W. « Adhesive, Solvent ». Dans Encyclopedic Dictionary of Polymers, 20. New York, NY : Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_276.

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Gooch, Jan W. « Differentiating Solvent ». Dans Encyclopedic Dictionary of Polymers, 219. New York, NY : Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_3649.

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Actes de conférences sur le sujet "Solvent-solvent"

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Gupta, Subodh Chandra, Simon Gittins, Arun Sood et Khalil Zeidani. « Optimal Amount of Solvent in Solvent Aided Process ». Dans Canadian Unconventional Resources and International Petroleum Conference. Society of Petroleum Engineers, 2010. http://dx.doi.org/10.2118/137543-ms.

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Gupta, Subodh Chandra, et Simon Gittins. « Measurement of Recovered Solvent in Solvent Aided Process ». Dans Canadian Unconventional Resources and International Petroleum Conference. Society of Petroleum Engineers, 2010. http://dx.doi.org/10.2118/136402-ms.

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Ivory, J., T. Frauenfeld et C. Jossy. « Thermal Solvent Reflux and Thermal Solvent Hybrid Experiments ». Dans Canadian International Petroleum Conference. Petroleum Society of Canada, 2007. http://dx.doi.org/10.2118/2007-067.

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Chang, Jeannine, John Joseph Ivory, Ken Forshner et Yu Feng. « Impact Of Solvent Loss During Solvent Injection Processes ». Dans SPE Heavy Oil Conference-Canada. Society of Petroleum Engineers, 2013. http://dx.doi.org/10.2118/165476-ms.

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Rasaiah, Jayendran C., et Jianjun Zhu. « Solvent dynamics and electron transfer reactions ». Dans Ultrafast reaction dynamics and solvent effects. AIP, 1994. http://dx.doi.org/10.1063/1.45397.

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Mialocq, J. C., P. Hébert, G. Baldacchino et T. Gustavsson. « Relaxation dynamics of a polar solvent cage around a nonpolar electronically excited solvent probe. A subpicosecond laser study ». Dans Ultrafast reaction dynamics and solvent effects. AIP, 1994. http://dx.doi.org/10.1063/1.45390.

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Balos, Vasileios, Hossam Elgabarty, Martin Wolf, Thomas Kühne, Roland Netz, Douwe Jan Bonthuis, Naveen Kumar Kaliannan, Philip Loche, Tobias Kampfrath et Mohsen Sajadi. « Ultrafast solvent-to-solvent and solvent-to-solute energy transfer driven by single-cycle THz electric fields ». Dans Terahertz Emitters, Receivers, and Applications XII, sous la direction de Manijeh Razeghi et Alexei N. Baranov. SPIE, 2021. http://dx.doi.org/10.1117/12.2594143.

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Muguet, Francis F., et G. Wilse Robinson. « Energetics and formation of the ‘‘hydrated electron’’ within an itinerant radical model ». Dans Ultrafast reaction dynamics and solvent effects. AIP, 1994. http://dx.doi.org/10.1063/1.45404.

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Grabowska, A. « Proton transfer reactions prepared by the hydrogen bonds in electronically excited polyatomic molecules ». Dans Ultrafast reaction dynamics and solvent effects. AIP, 1994. http://dx.doi.org/10.1063/1.45385.

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Declémy, Alain, et Claude Rullière. « Relaxation dynamics of the solvent cage around an excited molecule in solution ». Dans Ultrafast reaction dynamics and solvent effects. AIP, 1994. http://dx.doi.org/10.1063/1.45386.

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Rapports d'organisations sur le sujet "Solvent-solvent"

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Klatt, L. N. Caustic-Side Solvent Extraction Solvent-Composition Recommendation. Office of Scientific and Technical Information (OSTI), mai 2002. http://dx.doi.org/10.2172/814130.

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Fraga, Carlos, Kai-For Mo, David Abrecht, Amanda Casella, Nicolas Uhnak, Zachary Kennedy et Gregg Lumetta. Solvent Exchange. Office of Scientific and Technical Information (OSTI), septembre 2020. http://dx.doi.org/10.2172/1983975.

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Leonard, R. A. Caustic-side solvent extraction Flowsheet for optimized solvent. Office of Scientific and Technical Information (OSTI), juillet 2002. http://dx.doi.org/10.2172/799858.

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Delmau, Laetitia Helene, et Bruce A. Moyer. Solvent Blending Strategy to Upgrade MCU CSSX Solvent to Equivalent Next-Generation CSSX Solvent. Office of Scientific and Technical Information (OSTI), décembre 2012. http://dx.doi.org/10.2172/1057946.

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Moyer, Bruce, et Nathan Bessen. Density of Next-Generation Caustic-Side Solvent Extraction Solvent. Office of Scientific and Technical Information (OSTI), août 2021. http://dx.doi.org/10.2172/1819565.

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Paffhausen, M. W., D. L. Smith et S. N. Ugaki. Solvent recycle/recovery. Office of Scientific and Technical Information (OSTI), septembre 1990. http://dx.doi.org/10.2172/6153281.

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Crowder, M. L. Solvent Quality Testing. Office of Scientific and Technical Information (OSTI), septembre 2002. http://dx.doi.org/10.2172/802626.

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Leigh R. Martin et Bruce J. Mincher. TALSPEAK Solvent Degradation. Office of Scientific and Technical Information (OSTI), septembre 2009. http://dx.doi.org/10.2172/971366.

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Bonnesen, P. V. Stability of the Caustic-Side Solvent Extraction (CSSX) Process Solvent : Effect of High Nitrite on Solvent Nitration. Office of Scientific and Technical Information (OSTI), juin 2002. http://dx.doi.org/10.2172/814158.

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Duncan, Nathan C., Laetitia Helene Delmau, Dale Ensor, Denise L. Lee, Joseph F. Birdwell Jr, Talon G. Hill, Neil J. Williams et al. Next Generation Solvent Development for Caustic-Side Solvent Extraction of Cesium. Office of Scientific and Technical Information (OSTI), juillet 2013. http://dx.doi.org/10.2172/1087500.

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