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Relevant bibliographies by topics / Phase equilibria

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Academic literature on the topic 'Phase equilibria'

Author: Grafiati

Published: 4 June 2021

Last updated: 11 January 2025

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Journal articles on the topic "Phase equilibria"

1

Walther, J. V. "Phase Equilibria." Science 262, no. 5141 (December 17, 1993): 1911–12. http://dx.doi.org/10.1126/science.262.5141.1911.

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Ashirov, G. "PHASE EQUILIBRIA IN THE Ag8SiTe6–Ag8GeTe6 SYSTEM." Azerbaijan Chemical Journal, no. 1 (March 15, 2022): 89–93. http://dx.doi.org/10.32737/0005-2531-2022-1-89-93.

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Phase equilibria in the Ag8SiTe6–Ag8GeTe6 system were experimentally investigated by means of differential thermal analysis and powder X-ray diffraction techniques. It was established that continuous series of solid solutions with SiGe substitution are formed in the system. T–x-diagram of the title system and concentration dependence of lattice parameters of the obtained solid solutions were plotted

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Mekhdiyeva, I. F. "PHASE EQUILIBRIA IN THE TlTe-Tl9ErTe6 SYSTEM." Azerbaijan Chemical Journal, no. 2 (June 18, 2020): 74–77. http://dx.doi.org/10.32737/0005-2531-2020-2-74-77.

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Amundson, N. R., A. Caboussat, J. W. He, A. V. Martynenko, C. Landry, C. Tong, and J. H. Seinfeld. "A new atmospheric aerosol phase equilibrium model (UHAERO): organic systems." Atmospheric Chemistry and Physics Discussions 7, no. 3 (June 22, 2007): 8709–54. http://dx.doi.org/10.5194/acpd-7-8709-2007.

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Abstract. In atmospheric aerosols, water and volatile inorganic and organic species are distributed between the gas and aerosol phases in accordance with thermodynamic equilibrium. Within an atmospheric particle, liquid and solid phases can exist at equilibrium. Models exist for computation of phase equilibria for inorganic/water mixtures typical of atmospheric aerosols; when organic species are present, the phase equilibrium problem is complicated by organic/water interactions as well as the potentially large number of organic species. We present here an extension of the UHAERO inorganic thermodynamic model (Amundson et al., 2006c) to organic/water systems. Phase diagrams for a number of model organic/water systems characteristic of both primary and secondary organic aerosols are computed. Also calculated are inorganic/organic/water phase diagrams that show the effect of organics on inorganic deliquescence behavior. The effect of the choice of activity coefficient model for organics on the computed phase equilibria is explored.

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Amundson, N. R., A. Caboussat, J. W. He, A. V. Martynenko, C. Landry, C. Tong, and J. H. Seinfeld. "A new atmospheric aerosol phase equilibrium model (UHAERO): organic systems." Atmospheric Chemistry and Physics 7, no. 17 (September 14, 2007): 4675–98. http://dx.doi.org/10.5194/acp-7-4675-2007.

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Abstract. In atmospheric aerosols, water and volatile inorganic and organic species are distributed between the gas and aerosol phases in accordance with thermodynamic equilibrium. Within an atmospheric particle, liquid and solid phases can exist at equilibrium. Models exist for computation of phase equilibria for inorganic/water mixtures typical of atmospheric aerosols; when organic species are present, the phase equilibrium problem is complicated by organic/water interactions as well as the potentially large number of organic species. We present here an extension of the UHAERO inorganic thermodynamic model (Amundson et al., 2006c) to organic/water systems. Phase diagrams for a number of model organic/water systems characteristic of both primary and secondary organic aerosols are computed. Also calculated are inorganic/organic/water phase diagrams that show the effect of organics on inorganic deliquescence behavior. The effect of the choice of activity coefficient model for organics on the computed phase equilibria is explored.

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Tukmakova, Anastasiia, Anna Novotelnova, Sergey Taskaev, Hiroyuki Miki, and Vladimir Khovaylo. "Simulation of Fe-Ti-Sb Thernary Phase Diagram at Temperatures above 900 K." Key Engineering Materials 877 (February 2021): 114–19. http://dx.doi.org/10.4028/www.scientific.net/kem.877.114.

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Heusler alloys have been considered as one of the most promising thermoelectric materials for electrical power generation in a temperature range of 500–800 °C. Establishment of phase diagrams allows one to predict formation, equilibria, and stability of phases in of these ternary alloys. In this work we report on the simulation and investigation of phase diagram and phase equilibria in ternary Ti-Fe-Sb system which is of considerable interest for thermoelectric applications. The simulation was carried out using the CALPHAD method in Pandat software. The existence of the thermoelectric Heusler TiFe1.5Sb phase was revealed in a temperature range from 970 to 1070 K. The equilibria between TiFe1.5Sb and other phases were determined. The entropy of formation was calculated for the phases existing at 970, 1020 and 1070 K using a fitting approach. A narrow equilibrium region containing pure body centered cubic Fe and TiFe1.5Sb was found.

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Ismayilova, E. N., L. F. Mashadiyeva, I. B. Bakhtiyarly, and M. B. Babanly. "PHASE EQUILIBRIA IN THE Cu2Se–SnSE–Sb2Se3 SYSTEM." Azerbaijan Chemical Journal, no. 1 (March 15, 2022): 73–82. http://dx.doi.org/10.32737/0005-2531-2022-1-73-82.

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Phase equilibria in the Cu2Se–SnSe–Sb2Se3 quasi-ternary system has been studied by differential thermal analysis and powder X-ray diffraction. Some polythermal sections, isothermal sections at 300 K of the phase diagram and the projection of the liquidus surface are constructed. The regions of primary crystallization of phases, the nature and temperatures of non- and monovariant equilibria have been determined. The phase diagram of the SnSe–CuSbSe2 quasi-binary section has been refined. It was found that a quaternary compound CuSnSbSe3 is formed in the system by the peritectic reaction. This compound exists in a narrow range ~(650–723 K) temperatures. In addition, in the studied Cu2Se–SnSe–Sb2Se3 system, limited regions of solid solutions based on the SnSe, Sb2Se3, CuSbSe2 and SnSb2Se4 compounds have also been revealed

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Mansimova, Sh H., K. N. Babanly, L. F. Mashadiyeva, R. J. Mirzoyeva, and M. B. Babanly. "PHASE EQUILIBRIA IN THE Ag2Se-PbSe-AgSbSe2 SYSTEM." Chemical Problems 17, no. 1 (2019): 41–49. http://dx.doi.org/10.32737/2221-8688-2019-1-41-49.

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Alakbarzade, G. I. "SOLID-PHASE EQUILIBRIA IN THE TlBiТe2-TlTbTe2 SYSTEM." Chemical Problems 17, no. 4 (2019): 565–70. http://dx.doi.org/10.32737/2221-8688-2019-4-565-570.

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Mashadiyeva, L. F., Z. T. Hasanova, Yu A. Yusibov, and M. B. Babanly. "PHASE EQUILIBRIA IN THE Cu2Se–Cu3AsSe4–As2Se3 SYSTEM." Azerbaijan Chemical Journal, no. 3 (August 21, 2024): 83–93. http://dx.doi.org/10.32737/0005-2531-2024-3-83-93.

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Through experimental study of carefully crystallized via long-term thermal annealing alloys using powder X-ray diffraction and differential thermal analysis methods, as well as considering the evidence from the literature, a comprehensive picture of phase equilibria in the Cu2Se-Cu3AsSe4-As2Se3 system was obtained. The projection of the liquidus surface, the isothermal section at 500 K, and three vertical sections of the phase diagram are presented and discussed. The fields of primary crystallization of phases, types, and coordinates of invariant and monovariant phase equilibria are determined. The side Cu2Se-As2Se3 system was re-investigated and its refined phase diagram was constructed. It is shown that this system is quasi-binary and is characterized by the formation of ternary Cu3AsSe3 and CuAsSe2 compounds

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Dissertations / Theses on the topic "Phase equilibria"

1

Clark, A. Q. "Phase equilibria studies of mixtures." Thesis, University of Exeter, 1986. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.374949.

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Du, Rand Marlie. "High pressure fluid phase equilibria." Thesis, Stellenbosch : Stellenbosch University, 2000. http://hdl.handle.net/10019.1/51789.

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Thesis (MScEng)--University of Stellenbosch, 2000.
ENGLISH ABSTRACT: Supercritical extraction is being investigated as a possible alternative to the processes currently used in the fractionation of paraffinic waxes. By removing the lighter carbon fractions from the wax, the wax hardness will be improved and its melting temperature range reduced, hence improving the performance of the wax product in certain applications. In order to evaluate and operate such an extraction process optimally, it is necessary to have a thermodynamic model that accurately represents the process system. There are, however, currently no predictive models available for these systems. In order to fit present models to the systems, accurate phase equilibrium data of the supercritical solvent - n-alkane systems are needed. Unfortunately, the amount of reliable published data on these systems in the required operating range is very limited. A view cell was designed and developed with which these high pressure equilibria could be studied. The binary phase equilibria of supercritical CO2 with n-CI2, n-CI6, n-C20, n-C24, n-C28 and n-C36 and of supercritical ethane with n-CI6, n-C24 and n-C28 were measured in the temperature range 313 - 367 K. It was found that the systems with these two solvents have very different types of phase behaviour. The n-alkane solubility is much higher in ethane, but supercritical CO2 will provide a much better degree of control over the selectivity achieved in an extraction process. Of the various equations of state investigated, it was found that the Patel Teja equation of state provided the best fit of the CO2 - n-alkane systems and that the Soave-Redlich- Kwong equation fitted the ethane - n-alkane systems the best. The interaction parameters of both these equations of state display a functional relationship with temperature and nalkane acentric factor, making it possible to determine parameter values for application at other operating temperatures and with other n-alkane systems. It was found that the current equations of state were not able to represent the phase equilibria accurately over the entire range of operating conditions. The poor performance of the equations of state can be attributed to inherent flaws in the existing equations of state.
AFRIKAANSE OPSOMMING: Superkritiese ekstraksie word tans ondersoek as 'n moontlike altematief vir die prosesse wat huidiglik gebruik word om paraffiese wasse te fraksioneer. Die Iigter koolstofwasse word verwyder om die washardheid te verhoog en die temperatuurgebied waaroor die was smelt te verklein. Dit verbeter dan die was se kwaliteit en werkverrigting. Modelle wat die superkritiese ekstraksie proses akkuraat kan voorstel word egter benodig om die ekstraksie proses te kan evalueer en optimaal te bedryf. Daar is tans geen modelle beskikbaar wat die proses direk kan voorstel nie. Akkurate fase-ewewigsdata word benodig om bestaande modelle aan te pas vir gebruik in hierdie sisteme. Daar is egter baie min betroubare faseewewigsdata vir die superkritiese oplosmiddel - n-alkaan sisteme beskikbaar in die literatuur. 'n Sig-sel, waarrnee hierdie hoe druk data gemeet kan word, is ontwerp en ontwikkel. Die volgende binere fase ewewigte is in die temperatuur gebied 313 - 367 K gemeet: superkritiese CO2 met n-CI2, n-CI6, n-C20, n-C24, n-C28 en n-C36, en superkritiese Etaan met n-CI6, n-C24 en n-C28. Daar is gevind dat hierdie twee superkritiese oplosmiddelsisteme verskillende tipes fase-ewewigsgedragte openbaar. Die n-alkane het 'n baie boer oplosbaarheid in Etaan, maar deur superkritiese C02 in 'n ekstraksie kolom te gebruik, sal tot beheer oor die selektiwiteit van die ekstraksieproses lei. Uit die verskillende toestandsvergelykings wat ondersoek is, is daar gevind dat die Patel- Teja vergelyking die CO2 sisteme die beste kon beskryf en dat die Soave-Redlich-Kwong vergelyking die beste vergelyking was om die Etaan sisteme mee te modelleer. Beide die toestandsvergelykings se interaksie parameters het 'n funksionele verband met temperatuur en die n-alkaan asentrise faktor getoon. Dit is dus moontlik om waardes vir die parameters vir sisteme by ander temperature en met ander n-alkaan tipes te bepaal. Daar was gevind dat die bestaande toestandsvergelykings nie die die fase-ewewigte oor die hele eksperimenele gebied akkuraat kon voorstel nie. Dit kan toegeskryf word aan foute wat inherent is aan die vergelykings.

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Boothroyd, Simon. "Phase equilibria from molecular simulation." Thesis, Lancaster University, 2018. http://eprints.lancs.ac.uk/126751/.

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Phase equilibria are at the heart of many properties of substances, such as their solubility, manufacturability, and stability. They are of significant industrial and commercial interest, perhaps most importantly to the pharmaceutical industry where drug stability and solubility are two of the largest challenges of drug development. The focus of this thesis then was to develop a molecular level understanding of phase equilibria, and produce tools and models to predict phase stability. An emphasis was given to exploring solid-solid and solid-liquid equilibria and stability. Specifically, the work presented here aimed to elucidate what drives the formation of multicomponent crystals, improve available models for exploring phase equilibria phenomena and explore solubility prediction from first principles as a potentially more powerful alternative to correlation based methods. These three fundamental areas were explored by employing molecular simulation in combination with the machinery of statistical mechanics, utilising advanced sampling methods and free energy calculations. This approach has led to the development of a foundation for understanding multicomponent crystal formation in terms of molecular affinities and packing, the characterisation of a set of soft coarse-grained potentials for use in phase equilibria studies, which overcome the main limitations of the most widely used potential, and finally, the development of a novel method for solubility prediction from first principles. Here, this novel method was successfully applied to an ionic (aqueous sodium chloride) and small molecular (urea in methanol and aqueous urea) system. In the future, these results are expected to lead to a set of guidelines for predicting (and perhaps prohibiting) multicomponent crystal formation, the development of a higher class of coarse-grained transferable force field with utility in studying phase equilibria, and powerful approach for predicting solubility of even large, flexible molecules (such as pharmaceuticals).

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Pinho, Simão. "Phase equilibria in electrolyte systems." Doctoral thesis, Universidade do Porto, Faculdade de Engenharia, 2000. http://hdl.handle.net/10198/1478.

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The main objectives of this work are the study of solid-liquid equilibrium of salts in pure and mixed solvents, and of biomolecules, such as amino acids and peptides, in water. The correlation and prediction of properties for mixtures containing charged electric species, the electrolytes, is of great relevance for the chemical industry. A brief discussion about the whole interest of this work and the need of concentrating efforts to develop accurate models for electrolyte systems is initially focused. The fundamental concepts of electrolyte thermodynamics and industrial examples where electrolytes play an important role are given. The available different models to correlate and/or predict properties and phase equilibria for this kind of mixtures are reviewed and compared. An isothermal analytical method, which has been implemented to measure salt solubilities, is described in detail. The experimental solubilities obtained for NaCl, KCl, NaBr and KBr, in the pure solvents water, methanol, ethanol and in the mixed solvents water/methanol, water/ethanol and methanol/ethanol in the temperature range between 25 oC and 80 oC are given. The new experimental data is used together with additional information published by other authors, concerning solid-liquid equilibrium of salts in pure and mixed solvents and osmotic coefficients in pure solvents, in order to establish an extensive and reliable database. This is adopted for the development of consistent thermodynamic models. Two UNIQUAC based models are suggested: the UNIQUAC + Pitzer-Debye-Hückel model, and the UNIQUAC model with linear temperature dependent solvent/salt parameters. A new developed approach for correlating salt solubilities, based on the symmetric convention of normalization of the activity coefficients and on the mole fraction concentration scale on ionized basis is presented. In this way, it is possible the direct access to the salt solubility product in terms of its calorimetric properties such as the melting temperature, enthalpy of fusion and heat capacity change. The capabilities of these models for the correlation and prediction of solid-liquid equilibrium and other thermodynamic properties are discussed. The results indicate that this procedure and these models are satisfactory for solid-liquid equilibrium calculations. The work on weak electrolytes consists of the development of a new group-contribution method. This includes two terms: the UNIFAC model to account for the short-range interaction forces, and a Debye-Hückel expression for the long-range forces. New UNIFAC groups have been assigned to describe the amino acids and peptides studied, and the chemical equilibrium is taken into account simultaneously with the physical equilibrium. Using this approach, the temperature and pH effects on the solubilities of amino acids in aqueous solutions are taken into consideration. This model predicts very successfully the pH influence on the solubilities of amino acids and therefore may be used for engineering purposes.

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Meyer, Clifford Alexander. "Calculation of chemical and phase equilibria." Master's thesis, University of Cape Town, 1996. http://hdl.handle.net/11427/22557.

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Bibliography: pages 167-169.
The computation of chemical and phase equilibria is an essential aspect of chemical engineering design and development. Important applications range from flash calculations to distillation and pyrometallurgy. Despite the firm theoretical foundations on which the theory of chemical equilibrium is based there are two major difficulties that prevent the equilibrium state from being accurately determined. The first of these hindrances is the inaccuracy or total absence of pertinent thermodynamic data. The second is the complexity of the required calculation. It is the latter consideration which is the sole concern of this dissertation.

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Oliveira, Mariana Belo de. "Phase equilibria modeling for biofuels production." Doctoral thesis, Universidade de Aveiro, 2010. http://hdl.handle.net/10773/3220.

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Doutoramento em Engenharia Química
Em consequência de uma série de problemas ambientais, económicos e políticos relacionados com o uso de combustíveis convencionais, vários países estão agora a focar as suas atenções em combustíveis alternativos. O biodiesel está na linha da frente das alternativas ao petróleo no sector dos transportes, sendo considerado uma opção a curto prazo visto que o seu preço é competitivo e não são necessárias mudanças nos motores para implementar o seu uso. De entres os possíveis processos de produzir biodiesel, a reacção de transesterificação com catálise básica é o método preferido. Depois da reacção são sempre necessários processos de purificação de modo ao biodiesel produzido cumprir os standards definidos para os combustíveis alternativos, reduzindo problemas de motor e consequentemente aumentando a sua aceitação por parte dos consumidores. De entre as especificações encontram-se o conteúdo em água, em álcool e em glicerol. Ser-se capaz de descrever correctamente o equilíbrio de fases de sistemas que são de interesse para os processos de purificação de biodieseis numa gama alargada de condições termodinâmicas é uma condição necessária para uma correcta simulação do processo industrial, de modo a se atingir uma elevada produtividade a baixos custos de operação. O uso de moléculas oxigenadas como combustíveis representa uma alteração significativa em termos da termodinâmica de soluções. Para combustíveis baseados em petróleo as equações de estado cúbicas e os modelos clássicos de coeficientes de actividade mostraram ser apropriados, no entanto para combustíveis novos como o biodiesel, sendo mais complexos do ponto de vista das interacções intermoleculares com formação de dipolos e pontes de hidrogénio, são necessários modelos termodinâmicos mais complexos para descrever essas interacções. Neste trabalho a CPA EoS (Cubic-Plus-Association Equation of State) será desenvolvida de modo a permitir uma descrição adequada dos equilíbrios líquido-vapor e líquido-líquido para uma serie de sistemas binários e multicomponentes contendo água, ácidos gordos, ésteres de ácidos gordos, glicerol e álcoois.
As a consequence of a range of environmental, economical and political problems related to the use of conventional petroleum based fuels, several countries are now focusing their attention on alternative fuels. Biodiesel is at the forefront of the alternatives to petroleum based fuels in the transportation sector, being considered an important short-time option since its price can be competitive with conventional diesel and no motor changes are required. Among the various approaches to produce biodiesel, basic catalyzed transesterification is the preferable method. After the transesterification reaction purification steps are always necessary in order to provide the fuel with the quality levels required by the standards for alternative fuels, reducing engine problems and consequently increasing consumers’ acceptance. Among the specifying minimums are the water, the alcohol and the glycerol contents. Being able to correctly describe the phase equilibria of systems of interest for the biodiesel purification processes in a broad range of thermodynamic conditions is a necessary condition for a correct simulation of the industrial process, in order to achieve high productivity and low operating costs. The use of oxygenated molecules as fuels represents a significant change in terms of solution thermodynamics. While for petroleum-based fuels, cubic equations of state and classic activity coefficient models have proved to be appropriate, new fuels, such as biodiesel, are more complex from the point of view of intermolecular interactions with dipoles and hydrogen bonding being important on these systems. To be able to represent such interactions more complex engineering thermodynamics models are required. In this work the CPA EoS (Cubic – Plus – Association Equation of State) will be developed to provide an adequate description of the vapor-liquid and liquidliquid phase equilibria of several binary and multicomponent systems containing water, fatty acids, fatty acid esters, glycerol and alcohols.

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Apte, Pankaj A. "Phase equilibria and nucleation in condensed phases a statistical mechanical study /." Columbus, Ohio : Ohio State University, 2005. http://rave.ohiolink.edu/etdc/view?acc%5Fnum=osu1135876018.

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Huang, Tsang-Min. "Phase Equilibria of Binary Liquid Crystal Mixtures Involving Induced Ordered Phases." University of Akron / OhioLINK, 2010. http://rave.ohiolink.edu/etdc/view?acc_num=akron1284381816.

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Apte, Pankaj A. "Phase equilibria and nucleation in condensed phases: a statistical mechanical study." The Ohio State University, 2006. http://rave.ohiolink.edu/etdc/view?acc_num=osu1135876018.

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Bonavoglia, Barbara. "Phase equilibria in polymer-supercritical CO₂ systems /." Zürich : ETH, 2005. http://e-collection.ethbib.ethz.ch/show?type=diss&nr=16147.

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Books on the topic "Phase equilibria"

1

B, Stringfellow Gerald, ed. Phase equilibria diagrams. Gaithersburg, Maryland: National Institute of Standards and Technology, Ceramics Division, 1992.

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E, McHale Anna, ed. Phase equilibria diagrams. Gaithersburg, Maryland: National Institute of Standards and Technology, Ceramics Division, 1994.

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S, Roth Robert, ed. Phase equilibria diagrams. Gaithersburg, Maryland: National Institute of Standards and Technology, Ceramics Division, 1995.

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S, Roth Robert, Vanderah Terrell A, American Ceramic Society, and National Institute of Standards and Technology., eds. Phase equilibria diagrams. Westerville, Ohio: American Ceramic Society, 2005.

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P, Cook Lawrence, and McMurdie Howard F, eds. Phase equilibria diagrams. Gaithersburg, Maryland: National Institute of Standards and Technology, Ceramics Division, 1989.

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S, Roth Robert, American Ceramic Society, and National Institute of Standards and Technology, eds. Phase equilibria diagrams. Westerville, Ohio: American Ceramic Society, 2001.

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International, ASM, ed. Journal of phase equilibria. Materials Park, OH: ASM International, 1991.

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B, Stringfellow Gerald, ed. Phase equilibria diagrams: Phase diagrams for ceramists. Westerville: American Ceramic Society, 1992.

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S, Roth Robert, American Ceramic Society, and National Institute of Standards and Technology., eds. Phase equilibria diagrams: Phase diagrams for ceramists. Westerville, Ohio: American Ceramic Society, 1995.

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Chu-kun, Kuo. High temperature phase equilibria and phase diagrams. Oxford [England): Pergamon Press, 1990.

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Book chapters on the topic "Phase equilibria"

1

Raal, J. David, and Andreas L. Mühlbauer. "The Modern Direct Method and Novel Eos Mixing Rules for Hpvle Computation." In Phase Equilibria, 409–36. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-21.

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Raal, J. David, and Andreas L. Mühlbauer. "The Static Method for Hpvle Experimentation." In Phase Equilibria, 165–90. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-9.

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Raal, J. David, and Andreas L. Mühlbauer. "Computation of Low-Pressure Vapor-Liquid Equilibria." In Phase Equilibria, 249–84. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-13.

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Raal, J. David, and Andreas L. Mühlbauer. "Background to High-Pressure Phase Equilibrium Measurement." In Phase Equilibria, 133–46. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-7.

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Raal, J. David, and Andreas L. Mühlbauer. "Liquid-Liquid Equilibrium Measurement." In Phase Equilibria, 97–103. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-4.

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Raal, J. David, and Andreas L. Mühlbauer. "The Direct Method and Equations of State for Hpvle Computation." In Phase Equilibria, 353–78. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-19.

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Raal, J. David, and Andreas L. Mühlbauer. "Dew-Point, Bubble-Point, And Flash Calculations." In Phase Equilibria, 285–94. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-14.

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Raal, J. David, and Andreas L. Mühlbauer. "Prediction of Low-Pressure Vapor-Liquid Equilibrium." In Phase Equilibria, 295–328. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-15.

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Raal, J. David, and Andreas L. Mühlbauer. "Techniques for Hpvle Data Interpretation." In Phase Equilibria, 343–52. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-18.

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Raal, J. David, and Andreas L. Mühlbauer. "Thermodynamic Consistency Testing." In Phase Equilibria, 437–48. Boca Raton: Routledge, 2023. http://dx.doi.org/10.1201/9780203743621-22.

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Conference papers on the topic "Phase equilibria"

1

Goutaudier, C. "Crystal growth in condensed phase and phase diagrams." In XXXVII JEEP – 37th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2011. http://dx.doi.org/10.1051/jeep/201100002.

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2

Bitchikh, K., A. H. Meniai, W. Louaer, and J. P. Grolier. "Experimental and Modelling of liquid –solid equilibria." In XXXV JEEP – 35th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2009. http://dx.doi.org/10.1051/jeep/200900011.

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3

Mansour, S., N. Boutarek, H. Aid, and S. E. Amara. "Phase Equilibrium in the Fe-Cr-Nb Alloys." In XXXV JEEP – 35th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2009. http://dx.doi.org/10.1051/jeep/200900003.

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Linol, J., and G. Coquerel. "Simplification of the landscape under high energy milling of molecular solids exhibiting polymorphism." In XXXV JEEP – 35th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2009. http://dx.doi.org/10.1051/jeep/200900013.

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Couvrat, N., Y. Cartigny, and G. Coquerel. "Influence of solid/vapour equilibria on the stability of organic solids." In XXXV JEEP – 35th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2009. http://dx.doi.org/10.1051/jeep/200900012.

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Martins, D., F. Gouriou, and G. Coquerel. "Tuning of Operating Conditions in View to Access To a Single Polymorph by Spray Drying." In XXXV JEEP – 35th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2009. http://dx.doi.org/10.1051/jeep/200900014.

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7

Ferriol, Michel. "Preface." In XXXVII JEEP – 37th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2011. http://dx.doi.org/10.1051/jeep/201100001.

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8

Keddam, M. "Calcul thermodynamique des phases du système Fe-N." In XXXVII JEEP – 37th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2011. http://dx.doi.org/10.1051/jeep/201100007.

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Idbenali, M., and C. Servant. "Thermodynamic description of the Gallium-Lanthanum binary system." In XXXVII JEEP – 37th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2011. http://dx.doi.org/10.1051/jeep/201100008.

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Ladjali, O., N. Mesrati, L. Hattali, A. B. Vannes, and D. Treheux. "Durcissement structural par laser YAG-Nd+3de l’alliage de Titane " T40 "." In XXXV JEEP – 35th Conference on Phase Equilibria. Les Ulis, France: EDP Sciences, 2009. http://dx.doi.org/10.1051/jeep/200900006.

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Reports on the topic "Phase equilibria"

1

Ho, C. K. Multicomponent three-phase equilibria. Office of Scientific and Technical Information (OSTI), June 1995. http://dx.doi.org/10.2172/87825.

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Tsouris, Costas, and Vinod Shah. Phase Equilibria Modification by Electric Fields. Office of Scientific and Technical Information (OSTI), June 1999. http://dx.doi.org/10.2172/827414.

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Tsouris, Costas. Phase Equilibria Modification by Electric Fields. Office of Scientific and Technical Information (OSTI), December 2000. http://dx.doi.org/10.2172/827419.

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4

Winnie Wong-Ng. Phase Equilibria Relationships of High-Tc Superconductors. Office of Scientific and Technical Information (OSTI), January 2011. http://dx.doi.org/10.2172/1001419.

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Plante, E. R., and J. W. Hastie. Vaporization and phase equilibria of simulated radionuclides. Gaithersburg, MD: National Bureau of Standards, January 1986. http://dx.doi.org/10.6028/nbs.ir.86-3348.

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6

Reeber, R. R., D. Brenner, K. Wang, and John Prater. Thermophysical Properties and Phase Equilibria of Materials Systems. Fort Belvoir, VA: Defense Technical Information Center, June 2002. http://dx.doi.org/10.21236/ada413930.

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7

Athanassios Z. Panagiotopoulos. MOLECULAR SIMULATION OF PHASE EQUILIBRIA FOR COMPLEX FLUIDS. Office of Scientific and Technical Information (OSTI), September 2009. http://dx.doi.org/10.2172/963731.

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8

Traiber, A. J. S., S. M. Allen, P. E. A. Turchi, and R. M. Waterstrat. Electronic structure and phase equilibria in ternary substitutional alloys. Office of Scientific and Technical Information (OSTI), April 1996. http://dx.doi.org/10.2172/383551.

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Akao, J. H. Phase transitions and connectivity in three-dimensional vortex equilibria. Office of Scientific and Technical Information (OSTI), May 1994. http://dx.doi.org/10.2172/10166564.

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Chen, W. W., J. M. Zhang, A. J. Ardell, and B. Dunn. Solid-State Phase Equilibria in the ZnS-CdS System. Fort Belvoir, VA: Defense Technical Information Center, September 1988. http://dx.doi.org/10.21236/ada198982.

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