Academic literature on the topic 'Potassium carbonate systems'

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Journal articles on the topic "Potassium carbonate systems"

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Taniguchi, T., D. Dobson, A. P. Jones, R. Rabe, and H. J. Milledge. "Synthesis of cubic diamond in the graphite-magnesium carbonate and graphite-K2Mg(CO3)2 systems at high pressure of 9–10 GPa region." Journal of Materials Research 11, no. 10 (1996): 2622–32. http://dx.doi.org/10.1557/jmr.1996.0330.

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Cubic diamond was synthesized with two systems, (1) graphite with pure magnesium carbonate (magnesite) and (2) graphite with mixed potassium and magnesium carbonate at pressures and temperatures above 9.5 GPa, 1600 °C and 9 GPa, 1650 °C, respectively. At these conditions (1) the pure magnesite is solid, whereas (2) the mixed carbonate exists as a melt. In this pressure range, graphite seems to be partially transformed into hexagonal diamond. Measured carbon isotope δ13C values for all the materials suggest that the origin of the carbon source to form cubic diamond was the initial graphite powd
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Бетин, А. Н., А. И. Фролов, and В. И. Дорохова. "Potassium Carbonate Increases Cow Productivity." Vestnik APK Verhnevolzh`ia, no. 1(53) (March 30, 2021): 24–27. http://dx.doi.org/10.35694/yarcx.2021.53.1.004.

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Калий является одним из наиболее важных элементов в организме. Он должен поступать в организм ежедневно с кормами, поскольку сохраняется в нём короткое время и является донором катионов. Избыток всосавшегося калия выводится, в основном, через мочу. Он входит в состав буферных систем, поддерживает нормальное осмотическое давление, способствует процессам пищеварения, участвует в процессах синтеза белков и гликогена, тормозит сердечные сокращения. Калий поддерживает солевой баланс организма, состояние которого влияет на синтез белка, рост мышц и укрепление нейронных связей, на энергетическую сист
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Il’in, K. K., D. G. Cherkasov та D. V. Kapustina. "Phase Diagrams of the Ternary Systems Potassium Carbonate + Water + Hydrocarbon at 25°С". Izvestiya of Saratov University. New Series. Series: Chemistry. Biology. Ecology 17, № 2 (2017): 163–65. http://dx.doi.org/10.18500/1816-9775-2017-17-2-163-165.

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Salabat, Alireza, and Mahmod Hashemi. "Liquid–liquid equilibria for aliphatic alcohols + water + potassium carbonate systems; experiment and correlation." Physics and Chemistry of Liquids 45, no. 2 (2007): 231–39. http://dx.doi.org/10.1080/10683160500520502.

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Nicholas, Nathan Johann, Gabriel da Silva, Sandra Kentish, and Geoffrey W. Stevens. "Use of Vanadium(V) Oxide as a Catalyst for CO2Hydration in Potassium Carbonate Systems." Industrial & Engineering Chemistry Research 53, no. 8 (2014): 3029–39. http://dx.doi.org/10.1021/ie403836e.

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Li, Kejiang, Jianliang Zhang, Zhengjian Liu, Xiaojun Ning, and Tianqiu Wang. "Gasification of Graphite and Coke in Carbon–Carbon Dioxide–Sodium or Potassium Carbonate Systems." Industrial & Engineering Chemistry Research 53, no. 14 (2014): 5737–48. http://dx.doi.org/10.1021/ie4039955.

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Frolova, E. A., D. F. Kondakov, L. I. Avdyushkina, A. V. Bykov, A. N. Shkarupin, and V. P. Danilov. "Phase Equilibria in Water-Salt Systems Consisting of Potassium, Sodium, and Ammonium Carbonates and Anti-Icing Properties of Carbonate Compositions." Theoretical Foundations of Chemical Engineering 52, no. 4 (2018): 587–90. http://dx.doi.org/10.1134/s0040579518040103.

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Evdokimov, Andrey N., Alexander V. Kurzin, Andrey A. Sivakov, and Valeriya S. Golikova. "SOLUBILITY IN ALCOHOLS AND ALCOHOLYSIS REACTIONS OF CARBONATES, SULFIDES, CYANIDES, AND PHOSPHATES OF ALKALI METALS." IZVESTIYA VYSSHIKH UCHEBNYKH ZAVEDENIY KHIMIYA KHIMICHESKAYA TEKHNOLOGIYA 61, no. 12 (2018): 14–23. http://dx.doi.org/10.6060/ivkkt.20186112.5735.

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The published data on the solubilities of lithium, sodium, potassium, rubidium and cesium carbonates; sodium bicarbonate; sodium sulphide; potassium and sodium cyanides; orthophosphates, hydro- and dihydroorthophosphates of potassium and sodium, as well as sodium pyrophosphate in methanol, ethanol, 2-propanol, 2-methyl-1-propanol, benzyl alcohol, ethylene glycol, methyl cellosolve and glycerol have been considered and collected. A little bit information for salts has been taken from the most common solubility handbooks, but most of data was selected from scientific articles. There is an acid-b
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Mikhniuk, O. N., S. M. Leschev, and P. A. Kasyanchik. "Distribution constants and group increments of organic substances in the extraction systems of water saline–hexane." Proceedings of the National Academy of Sciences of Belarus, Chemical Series 56, no. 2 (2020): 158–65. http://dx.doi.org/10.29235/1561-8331-2020-56-2-158-165.

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In the extraction systems of hexane–aqueous solutions of potassium carbonate, ammonium sulfate and sodium chloride, the distribution of a number of organic compounds (benzyl alcohol, tetrahydrofuran, phenol, aniline, pyridine, pyridazine, pyrimidine, n-butylamine, diethylamine, triethylamine, benzylamine) was studied. It was shown that sodium chloride, the most frequently used as a salting out agent, is noticeably inferior in salting ability to potassium carbonate, dipotassium phosphate and ammonium sulfate, since it contains singly charged ions with a relatively low charge density. Using the
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Orjuela, Alvaro, Maria Fernanda Gutierrez, Andrea Suaza, and Jose Luis Rivera. "Production of sucroesters using solvent-free reactive systems containing emulsifiers." Ingeniería e Investigación 38, no. 1 (2018): 16–23. http://dx.doi.org/10.15446/ing.investig.v38n1.61432.

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The transesterification reaction of sucrose and fatty acid methyl esters to produce sucroesters was experimentally evaluated using commercial emulsifiers as compatibility agents. Reactions were carried out at temperatures between 100 and 140°C, using emulsifier concentrations in the range of 5 to 15 %wt, and potassium carbonate as catalyst. Fatty acid methyl esters consumption and sucroesters production was monitored by HPLC analysis of samples. Methyl esters conversions around 40 % were obtained with 68 %wt monoester content in sucroesters mixture. Despite the reaction times were reduced by o
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Dissertations / Theses on the topic "Potassium carbonate systems"

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Karthikeyan, Tejas Latha. "Investigation of the absorption solvent for bioenergy carbon capture and storage (BECCS) through pilot plant trials." Thesis, KTH, Kemiteknik, 2020. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-289165.

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Att begränsa globala uppvärmningen till 1,5°C kommer kräva negativa koldioxidutsläpp. En metod för att generera negativa koldioxidutsläpp är så kallad Bio-Energy Carbon Capture and Storage (BECCS). En direkt implementering av BECCS är att fånga in CO2 från rökgas som genereras vid förbränning av biomassa i en så kallad post-combustion capture-konfigurering. Post-combustion BECCS har skapat en stor resonans hos kraftverksoperatörer och pappersproducenter. Stockholm Exergi, som ägs av Fortum och Stockholms Stad, siktar på att fånga in upp till 800 kt CO2 per år från deras biomass-eldade CHP-anlä
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Villar, I. Comajoan Laia. "Simulation of stripper modifications for bioenergy carbon capture by absorption." Thesis, KTH, Kemiteknik, 2021. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-299891.

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Att koldioxidutsläppen neutraliseras är avgörande för att begränsa klimatförändringarna. Bioenergi i kombination med separation och lagring av koldioxid (BECCS) är en Teknik som kan generera negativa utsläpp. Det största hindret för dess storskaliga genomförande är de höga energikraven för processen. Detta projekt syftar till att kvantifiera energistraffen för lean solvent flash och modifikationer för multitrycksstrippning för att förbättra prestandan av koldioxidavskiljning (CC) i en kraftvärmeverksanläggning för förbränning av biomassa.  En jämviktsmodell utvecklades och validerades för att
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Dobson, David Peter. "The system potassium carbonate : magnesium carbonate as an analogue of phase relations and selected physical properties at high pressure." Thesis, University College London (University of London), 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.307649.

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Books on the topic "Potassium carbonate systems"

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1943-, Rousseau Ronald W., Ferrell J. K, and Air and Energy Engineering Research Laboratory, eds. Performance and modeling of a hot potassium carbonate acid gas removal system in treating coal gas: Project summary. U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, 1988.

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Conference papers on the topic "Potassium carbonate systems"

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Jo, Byeongnam, and Debjyoti Banerjee. "Interfacial Thermal Resistance Between a Carbon Nanoparticle and Molten Salt Eutectic: Effect of Material Properties, Particle Shapes and Sizes." In ASME/JSME 2011 8th Thermal Engineering Joint Conference. ASMEDC, 2011. http://dx.doi.org/10.1115/ajtec2011-44373.

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The aim of this study is to estimate the interfacial thermal resistance between a carbon nano-particle and alkali molten salt eutectics using molecular dynamics simulations. Additionally the effect of particle shapes and sizes on the interfacial thermal resistance was investigated using three different shapes of the carbon nanoparticles. Transient heat transfer simulation between a carbon particle and molecules of a molten salt was performed with the lumped capacitance method. A carbonate salt eutectic which consists of lithium carbonate (Li2CO3) and potassium carbonate (K2CO3) in 62:38 molar
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Ren, Nan, Yu-ting Wu, and Chong-fang Ma. "Preparation and Experimental Study of Mixed Carbonates With High Maximum Using Temperature." In ASME 2012 6th International Conference on Energy Sustainability collocated with the ASME 2012 10th International Conference on Fuel Cell Science, Engineering and Technology. American Society of Mechanical Engineers, 2012. http://dx.doi.org/10.1115/es2012-91401.

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In order to meet the demands of future high-temperature solar thermal power generation, 37 kinds of mixed carbonate molten salts were prepared by mixing potassium carbonate, lithium carbonate, sodium carbonate in accordance with different proportions in this paper. Melting point of molten salt, as the most important basic character, is the primary parameter to select molten salt. Melting point and decomposition temperature are measured by Simultaneous Thermal Analyzer. The results show that melting points of major ternary carbonates are close at around 400°C and decomposition temperatures of m
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Raimundo, Rodrigo C., José V. C. Vargas, Wellington Balmant, and Juan C. Ordóñez. "Sustainable Alkaline Membrane Fuel Cell (SAMFC)." In ASME 2018 12th International Conference on Energy Sustainability collocated with the ASME 2018 Power Conference and the ASME 2018 Nuclear Forum. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/es2018-7545.

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This work addresses the development and construction of a sustainable alkaline membrane fuel cell (SAMFC). The SAMFC couples an alkaline membrane fuel cell (AMFC) with a hydrogen generation reactor that uses recycled aluminum from soda cans to split the water molecule through the oxidation of aluminum catalyzed by sodium hydroxide. An innovative cellulosic membrane supports the electrolyte, which avoids the undesirable characteristics of liquid electrolytes, and asbestos or ammonia that are substances that have been used to manufacture alkaline electrolyte membranes, which are knowingly toxic
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Fiaschi, Daniele, Giampaolo Manfrida, Michela Massini, and Giacomo Pellegrini. "Some Innovative Readily Applicable Proposals for Chemical Separation and Sequestration of CO2 Emissions From Power Plants." In ASME 7th Biennial Conference on Engineering Systems Design and Analysis. ASMEDC, 2004. http://dx.doi.org/10.1115/esda2004-58508.

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The goal of the present manuscript is the investigation of two novel systems for partial CO2 capture from the exhausts of fossil fuelled powerplants. These systems should be relatively cheap and easily applicable to existing powerplants with minor modification, in order to make them accessible by a large range of users and favour a significant diffusion of partial CO2 sequestration. Two basic processes were proposed: 1. Absorption with a liquid solution of water and NH3; 2. Absorber/desorber system with a liquid solution of water and phosphates. In the first one, the exhausts react into an abs
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Sibarani, Tiurma Theresa, and Murtaza Ziauddin. "Rock Heterogeneity Effects on Fluid Diversion During Stimulation Treatment." In SPE Annual Technical Conference and Exhibition. SPE, 2021. http://dx.doi.org/10.2118/206095-ms.

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Abstract Rock heterogeneities, such as variations in pore distribution, pore throat diameter, and initial permeability, significantly affect the outcome of carbonate matrix stimulation treatments. A better understanding of the influence of these parameters on stimulation and diversion, especially for the performance of self-diverting acids, is needed for efficient stimulation designs. Carbonate rock samples from six outcrop formations, with permeability ranging from 2 to 150 md, were used in the study. Large blocks were acquired for each outcrop, and several 1.5×6-in. core plugs were drilled f
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Mascara, S., F. Vallorani, R. Jachnik, and D. Formisani. "Successful Shale Drilling Using a New Environmentally Compatible Potassium Carbonate/Polymer/PolyGlycol Mud System: Design and Field Experiences." In European Petroleum Conference. Society of Petroleum Engineers, 1998. http://dx.doi.org/10.2118/50580-ms.

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Siefert, Nicholas, and Shawn Litster. "Exergy and Economic Analysis of Catalytic Coal Gasifiers Coupled With Solid Oxide Fuel Cells." In ASME 2012 10th International Conference on Fuel Cell Science, Engineering and Technology collocated with the ASME 2012 6th International Conference on Energy Sustainability. American Society of Mechanical Engineers, 2012. http://dx.doi.org/10.1115/fuelcell2012-91445.

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The National Energy Technology Laboratory (NETL) as well as Li et al. [1] have shown that integrating a catalytic coal gasifier with a solid oxide fuel cell (SOFC) can achieve high system efficiencies (∼60%) while capturing and sequestering >90% of the carbon dioxide. Integration of a catalytic gasifier with a SOFC is aided by the minimal exergy destruction inside a catalytic, steam-coal gasifier producing a high-methane content syngas, and the decreased exergy destruction in the SOFC due to the ability to operate at lower air stoichiometric flow ratios compared with a SOFC operating only o
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