Academic literature on the topic 'Calcined soda'

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Journal articles on the topic "Calcined soda"

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Li, Bao Jia, and Guo Zhong Li. "Study on Mechanical Properties of Soda Residue / Fly Ash Composite Cementitious Material." Advanced Materials Research 194-196 (February 2011): 1026–29. http://dx.doi.org/10.4028/www.scientific.net/amr.194-196.1026.

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The composite cementitious material was prepared with soda residue and fly ash. The mechanical properties were improved by mixing calcined lime and Portland cement, and the mechanism of admixture was researched. The results showed that the 28d flexural strength reached 3.59MPa and the 28d compressive strength reached 9.71MPa., when the proportion of soda residue and fly ash was 40:60 with 9% Portland cement and 7% calcined lime added.
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Kotwica, Łukasz, Marcin Chorembała, Ewa Kapeluszna, et al. "Influence of Calcined Mine Tailings on the Properties of Alkali Activated Slag Mortars." Key Engineering Materials 761 (January 2018): 83–86. http://dx.doi.org/10.4028/www.scientific.net/kem.761.83.

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Influence of copper mine tailings on properties of soda activated ground granulated blast furnace slag mortars and pastes was investigated. Calcination of copper mine tailings was found to be a method of increasing their pozzolanic activity. Material calcined at 750°C possessed highest pozzolanic activity. So obtained material can be used as a partial substitution of ground granulated slag in soda activated blends. Introduction of calcined copper mine tailings decrease strength up to 28 days, but after 56 days strength results are similar or even higher comparing to control samples. Phase composition of hydrated material is not affected significantly by the presence of calcined copper mine tailings.
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Ersoy, Orkun, Murat Rençberoğlu, Dilek Karapınar Güler, and Ömer Faruk Özkaya. "A Novel Flux That Determines the Physico-Chemical Properties of Calcined Diatomite in Its Industrial Use as a Filler and Filter Aid: Thenardite (Na2SO4)." Crystals 12, no. 4 (2022): 503. http://dx.doi.org/10.3390/cryst12040503.

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Diatomite needs to go through the flux-calcination process in order to increase its functionality in some specific applications such as filter aids. In this study, the effects of the thenardite, which was used for the first time as a flux in the calcination of diatomite, and widely used soda ash on the industrially important physico-chemical properties of diatomite were investigated. Samples taken from two diatomite deposits in the Aegean region of Turkey (Seydiler diatomite from Afyon and Sarayköy diatomite from Denizli) were used in this study. In raw and calcined diatomite samples, geochemical and mineralogical composition and parameters such as colour, grain size, morphology, specific surface area, permeability and wet cake density were characterized. It was found that thenardite was more effective than traditionally used soda ash in improving whiteness (L* = 98.20) and filtrate clarity (wet cake density = 0.378 g/cm3). However, higher permeability (k), i.e., higher filtration rate, was obtained in diatomite calcined with soda ash (k = 0.97 µm2). Fluxes had different effects on different diatomite species. The necessity of choosing flux type depending on the application area and the desired properties from diatomite was demonstrated.
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Chambi, M. M., and Samuel Marcio Toffoli. "Use of Calcined Tannery Sludge Containing Chromium Compounds in Soda-Lime Glass Fabrication." Materials Science Forum 727-728 (August 2012): 1541–46. http://dx.doi.org/10.4028/www.scientific.net/msf.727-728.1541.

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Tanning industries generates large quantities of solid wastes containing chromium compounds with characteristics of high-polluting and hazardous conditions. However, these wastes are a potential source of chromium which could be used by the glass and ceramic enamels industries. In this study the properties of a calcined tannery sludge containing chromium compounds was investigated in order to evaluate the potential of using this powder as a suitable and cheap green colorant for the glass manufacturing. X-ray diffraction (XRD), chemical (XRF) and thermal (DTA/TG) analyses were used to determine the physical and chemical characteristics of tannery sludge. Colorimetric method using diphenylcarbazide were conducted to determinate the Cr (VI) concentration in the samples. Soda-lime glass containing calcined tannery sludge was prepared by melting at 1550°C. The results showed that the calcined tannery sludge has a favorable behavior to be used as an alternative source of chromium for the glass manufacturing.
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Yamagata, Chieko, João B. Andrade, Valter Ussui, Nelson Batista de Lima, and José Octavio Armani Paschoal. "High Purity Zirconia and Silica Powders via Wet Process: Alkali Fusion of Zircon Sand." Materials Science Forum 591-593 (August 2008): 771–76. http://dx.doi.org/10.4028/www.scientific.net/msf.591-593.771.

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Zircon sand was reacted with liquid caustic soda (50% NaOH) in open vessel at 600 oC for 2h. The effect of NaOH/ZrSiO4 reactant ratio on the yield of zirconia recovery was verified. Samples of fusion products water washed were characterized by X-ray diffraction (XRD) to identify the main compounds formed. Silica powders were obtained via acid catalyzed reaction and zirconia powders were resulted from crystallization of zirconium oxychoride. Both zirconia and silica powders were analyzed by XRF (X-ray fluorescence) and BET method. Laser Quasi Elastic Light Scattering (QLS) technique was used for agglomerate size distribution determination. High purity and fine zirconia and silica powders were obtained. The specific surface area of zirconia calcined at 550 oC reached ~ 70m2g-1. Silica powder calcined at 800 oC presented a high specific surface area ~ 500 m2g-1.
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Savinkov, Sergey V., and Vladimir M. Kiselev. "ANALYSIS OF PRICES FOR PRODUCTS OF CHEMICAL COMPLEX IN THE CONTEXT OF SUB-SECTORS OF CHEMICAL INDUSTRY IN THE RUSSIAN AND WORLD MARKETS." EKONOMIKA I UPRAVLENIE: PROBLEMY, RESHENIYA 10/2, no. 130 (2022): 204–16. http://dx.doi.org/10.36871/ek.up.p.r.2022.10.02.017.

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The authors assessed the change in prices on the domestic and world markets for the main commodity items of the chemical industry of the Russian Federation, such as mineral fertilizers, methanol, rubber, production of organic synthesis products, production of plastics in primary forms, plastic products, rubber products, paints, chemical fi bers and threads, products of household chemicals and synthetic detergents there are few means, tires, adhesives and sealants, resins, disinfectants, production products- and medium-tonnage chemical products, caustic and calcined soda. In all positions, except for only a few, the trend of price growth has intensifi ed.
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Paz, Y., and A. Heller. "Photo-oxidatively self-cleaning transparent titanium dioxide films on soda lime glass: The deleterious effect of sodium contamination and its prevention." Journal of Materials Research 12, no. 10 (1997): 2759–66. http://dx.doi.org/10.1557/jmr.1997.0367.

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In the context of photocatalytically self-cleaning windows and windshields, clear, abrasion resistant, thin (60 ± 10 nm) photocatalytic films of TiO2 were formed by a sol-gel process on (a) soda lime glass, (b) the proton-exchanged surface of soda lime glass, and (c) fused silica. The hypothesis that diffusion of sodium oxide from the soda lime glass into the titanium dioxide layer during the calcination step causes the lower photoefficiency in films on glass was tested and proven. At high concentration sodium prevented formation of the photoactive anatase phase and, at low concentration, introduced surface and bulk recombination centers. Sodium transport was efficiently blocked by a thin layer at the interface of proton-exchanged (“hydrogen”) glass and nascent TiO2, formed at 400 °C of a poly(titanyl acetylacetonate) TiO2 precursor. The sodium transport blocking layer did not form and the highly photocatalytic film was not obtained when the TiO2-precursor film was applied to glass that was not proton exchanged. Furthermore, only a much less effective sodium transport blocking layer was formed on glass that was proton-exchanged, but was calcined at 400 °C prior to application of the TiO2 precursor layer, showing that the sodium depleted glass surface, by itself, was a less effective barrier against sodium transport than the interfacial product of hydrogen glass and the TiO2 precursor.
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Yu, Huogen, Jia Guo Yu, Bei Cheng, C. H. Ao, and S. C. Lee. "Effects of Substrates on the Composition and Microstructure of TiO2 Thin Films Prepared by the LPD Method." Key Engineering Materials 280-283 (February 2007): 795–800. http://dx.doi.org/10.4028/www.scientific.net/kem.280-283.795.

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TiO2 thin films were prepared on soda lime glass, fused quartz and stainless steel substrates by liquid phase deposition (LPD) method from a (NH4)2TiF6 aqueous solution upon the addition of boric acid (H3BO3), and then calcined at 500oC for 2 h. The prepared films were characterized with X-ray diffraction (XRD), scanning electron microscopy (SEM) and X-ray photoelectron spectroscopy (XPS). It was found that the substrates obviously influenced the element composition and microstructure of TiO2 thin films. Except Ti, O and a small amount of F and N elements, which came from the precursor solution, some Si (or Fe) element in the thin films deposited on soda lime glass and quartz substrates (or on stainless steel substrate) was confirmed. The Si (or Fe) element in the thin films could be attributed to two sources. One was from the SiF6 2- ions (or FeF6 2- ions) formed by a reaction between the treatment solution and soda lime glass or quartz (or stainless steel) substrates. The other was attributed to the diffusion of Si (or Fe) from the surface of substrates into the TiO2 thin films after calcination at 500oC. The Si (or Fe) element in the TiO2 thin films could behave as a dopant and resulted in the formation of composite SiO2/TiO2 (or Fe2O3/TiO2) thin films on the substrates.
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Wang, Yan Hua, Sheng Ke Yang, Chan Juan Gao, and Miao Miao Zheng. "The Distribution Characteristics Analysis of Pollutant Atrazine in the Petrolic Drilling Fluids." Advanced Materials Research 726-731 (August 2013): 1977–80. http://dx.doi.org/10.4028/www.scientific.net/amr.726-731.1977.

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In view of the present situation that a lot of waste drilling fluids pollute soil and water in the process of petroleum exploration and development, choosing the drilling fluids in 5 well fields which are in the North area of ChangQing oilfield to carry on the pollution characteristic analysis. 35 physicochemical indexs and contamination indexs had been determined in the drilling fluids, its result is: the waste drilling fluids are ropiness colloid, paste, viscosity high. The drilling fluids ingredient is clay, polyacrylamide (PAM), carboxymethylcellulose (CMC). CODCr, mineral oils, NH4+, Cr, Cd, Pb, As, pH, chromaticity and so on exceed standard in the drilling fluids, Zn exceeds standard in some individual well fields, the other over-standard parameterssuperstandard multiple is not big except CODCr, mineral oils which exceed standard siriously. CODCr, mineral oils, NH4+ and so on are from formation petroleum and the additives such as polyacrylamide (PAM), carboxymethylcellulose (CMC).etc, high pH is related to calcined soda or caustic soda, Cr, Cd, Pb, As, Zn and so on are from the sidewall material which is cattied by the circulating mud, which are related to formation lithological composition.
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Xhaferaj, Nertil, Nicolò M. Ippolito, Fabio Maggiore, and Francesco Ferella. "Extraction and Recovery of Metals from Spent HDS Catalysts: Lab- and Pilot-Scale Results of the Overall Process." Metals 12, no. 12 (2022): 2162. http://dx.doi.org/10.3390/met12122162.

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The present study proposes an overall recycling process for spent hydrodesulfurization (HDS) catalysts. These catalysts contain valuable metals like cobalt (Co), molybdenum (Mo), nickel (Ni), and vanadium (V). In particular, one Co-Mo catalyst was treated in order to optimize the roasting step (time, soda ash, and temperature) at a pilot scale and thus maximize the extraction yield of molybdenum (Mo) and vanadium (V). In particular, a dry Co-Mo catalyst was used. After roasting at 700 °C for 2.5 h, the best conditions, the catalysts underwent water leaching, separating Mo and V from Co and the alumina carrier, which remained in the solid residue. The pregnant solution was treated to remove arsenic (As) and phosphorus (P), representing the main impurities for producing steel alloys. V was precipitated as NH4Cl, and further calcined to obtain commercial-grade V2O5, whereas Mo was recovered as molybdic acid by further precipitation at a pH of around one. Thus, molybdic acid was calcined and converted into commercial-grade MoO3 by calcination. The hydrometallurgical section was tested on a lab scale. The total recovery yield was nearly 61% for Mo and 68% for V, respectively, compared with their initial concentration in the spent Co-Mo catalysts.
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Dissertations / Theses on the topic "Calcined soda"

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Cardoso, Gaelle Lise Dias Pinto. "Metanólise de óleo de soja em reator de membrana compósita PVA/casca de ovo calcinada. Estudo do efeito da reticulação." Master's thesis, 2015. http://hdl.handle.net/10362/15742.

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Com a crise energética atual e os efeitos nocivos associados ao consumo de combustíveis fósseis e seus derivados, tornou-se imperativo pesquisar e desenvolver alternativas sustentáveis e economicamente viáveis face a esse recurso. Surgiu então o biodiesel, um combustível derivado de recursos renováveis e potencial substituto do diesel convencional de base petroquímica. A transesterificação de óleos vegetais apresenta ser a principal via na produção de biodiesel. A utilização de catalisadores básicos homogéneos, tal como o hidróxido de sódio, na produção de biodiesel apresenta algumas adversidades, nomeadamente, o aparecimento de reações secundárias de hidrólise dos triglicéridos, na presença de água, que promovem a formação de sabões e emulsões. Mesmo com o uso de reagentes secos, ocorrem reações entre o hidróxido e o álcool, formando-se água. Uma solução para este tipo de problemas é a utilização de catalisadores heterogéneos. Contudo, a produção de biodiesel apresenta custos associados elevados que podem ser diminuídos com a utilização de catalisadores provenientes de resíduos alimentares. Este trabalho consistiu na preparação de membranas catalítica de álcool polivinílico (PVA) incorporadas com um catalisador heterogéneo sólido básico (óxido de cálcio) obtido a partir de resíduos alimentares industriais (casca de ovo de galinha). Procedeu-se à caraterização das membranas por determinação da espessura, ângulos de contato, grau de inchamento e por espectroscopia de infravermelho. As membranas de PVA foram testadas na transesterificação de óleo de soja com metanol em reator de membrana catalítica. Analisou-se o efeito da reticulação química nas propriedades das membranas e na atividade catalítica.
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Book chapters on the topic "Calcined soda"

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Cristea, V. M., and P. S. Agachi. "Control of the Rotary Calciner for Soda Ash Production." In European Symposium on Computer Aided Process Engineering-12, 35th European Symposium of the Working Party on Computer Aided Process Engineering. Elsevier, 2002. http://dx.doi.org/10.1016/s1570-7946(02)80105-5.

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Conference papers on the topic "Calcined soda"

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Atheaux, I., A. Medvedev, and S. Makarychev-Mikhailov. "Analysis of Minerals in Drilling Fluids Using Synergy in X-Ray Fluorescence and Fourier Transform Infrared Spectra Realized with Machine Learning." In GOTECH. SPE, 2024. http://dx.doi.org/10.2118/219204-ms.

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Abstract Analysis of solid contents in drilling muds is part of the API mud testing protocol performed daily by the mud engineer during drilling operations. This is carried out with the laborious manual retort analysis where high-gravity solids (HGS) and low-gravity solids (LGS) are detected. With the vision to improve the process and potential toward online measurement, monitoring of HGS and LGS in water-based mud (WBM) using two fast and reliable analytical techniques, X-ray fluorescence (XRF) spectrometry and Fourier transform infrared (FTIR)-attenuated total reflection (ATR) spectroscopy, have been evaluated. While information on total LGS content in a drilling fluid is useful, understanding the LGS minerology is also undoubtedly valuable, particularly when reactive clays are present and wellbore stability and integrity are at risk. In the present work we describe the dataset of XRF and FTIR-ATR spectra of a series of multicomponent water-based drilling fluids loaded with up to eight dispersed minerals. The minerals were barite (HGS) and LGS as clays (bentonite, illite, and kaolinite), carbonates (calcite and dolomite) and siliceous minerals (quartz and soda feldspar). Machine-learning (ML) analysis techniques such as partial least squares (PLS) and advanced modern PLS methods were applied to XRF and FTIR combined data to analyse these complex multicomponent samples. In this paper, a detailed discussion of the data workflows will cover the spectra preprocessing, ML algorithm selection and results on individual spectra, concatenated data, and data fusion. While quantification of barite (HGS) in drilling fluids with either XRF or FTIR was straightforward (the coefficient of determination, R2, at ~0.99), analysis of some LGS was more challenging. For example, the best soda feldspar and calcite PLS models based on FTIR spectra showed poor performance (R2 ~0.75 and ~0.48, respectively). Interestingly, PLS models based on different combinations of concatenated spectra (joined side-by-side) demonstrated even worse results compared to the single spectra models. Extensions of the PLS method designed to deal with multiblock datasets were then explored, and the sequential and orthogonalized PLS (SO-PLS) was found to be the best, realizing the synergy between spectrum types. SO-PLS models for calcite and soda feldspar gave R2 of 0.97 and 0.77, respectively. Detailed error analysis for all minerals is finally presented in the paper, with prediction errors varied from 1% for barite to 11% for soda feldspar. The two spectrum types, when smartly processed together using data fusion and ML techniques, demonstrate synergy, and provide significantly better mineral quantification accuracy, achieving a comprehensive minerology analysis of solids in drilling fluid.
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Sun, L., C. C. Berndt, R. S. Lima, A. Kucuk, and K. A. Khor. "Effects of Spraying Parameters on Phase Formation and Distribution in Plasma-Sprayed Hydroxyapatite Coatings." In ITSC 2000, edited by Christopher C. Berndt. ASM International, 2000. http://dx.doi.org/10.31399/asm.cp.itsc2000p0803.

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Abstract Calcined spray-dried hydroxyapatite (Ca10(PO4)(OH)6; i.e., HA) powders were atmospherically plasma sprayed (APS) using various process parameters. The resulting phases within the coating surface and the interface between the coating and the substrate were analyzed using X-ray diffraction (XRD) methods. This XRD revealed the presence of both amorphous (i.e., amorphous calcium phosphate: ACP) and crystalline phases. The crystalline phases included both HA and some impurity phases from the decomposition of HA, such as tricalcium phosphate (α-TCP and β-TCP), tetracalcium phosphate (TTCP) and calcium oxide (CaO). The crystallinity of HA decreased with increasing spray power and stand-off distance (SOD). The percentage of all impurity phases increased with the spray power. The percentage of both TCP and TTCP decreased with the SOD while the CaO percentage increased. In addition, the percentage of ACP and CaO were higher in the interface than at the surface of the coating while the percentage of TCP and TTCP exhibited the opposite effect.
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Al-Yami, Abdullah, and Ali Al-Safran. "Activation of Local Bentonite for Oil and Gas Industry Application." In ASME 2022 41st International Conference on Ocean, Offshore and Arctic Engineering. American Society of Mechanical Engineers, 2022. http://dx.doi.org/10.1115/omae2022-81446.

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Abstract Magzoub, et al 20171 have proposed a method of converting calcium bentonite to sodium bentonite. The method will require a reactor for upscaling. The method involves preparation of soda ash solution, heating, mixing for at least 24 hours and finally removing impurities and drying out. Besun et al. 19972 have proposed a method that will require also a reactor facility to upscale. Starch has to be added in water then bentonite is added in a separate water solution. Both were mixed and heated to form a structure of bentonite-starch gel. The formed gel has 20% starch and 80% bentonite. Bentonite is used in different applications such as drilling fluid, leaching earth, and animal feed additive.3 Sodium bentonite is more attractive in applications such as drilling due to its high swelling and good fluid loss control which makes it always in high demand. 4 & 5 The objectives of this study are to investigate and characterize local calcium bentonite in Saudi Arabia and to find optimum method to activate it for application in drilling fluids and cementing. The characterization performed utilized XRF, XRD, and ESEM backscattered electron images along with EDS spectra for samples collected from different depths (5 meter and 7-meter samples). API testing including viscosity and fluid loss measurements were also conducted in the characterization phase. Activation was done utilizing cost effective additives such as soda ash. The activated bentonite was testing using standard testing procedures for drilling fluids and cementing such as rheology, fluid loss control, settling, compressive strength and thickening time tests. The characterization concluded that the samples consisted mainly of Na-montmorillonite with appreciable amounts of impurities of quartz, kaolinite, illite, albite, calcite, and hematite. Compared to API reference sample, the local bentonite samples had less Na-montmorillonite contents, which probably needs some treatments to improve their quality. From this characterization, we can tell that activation of the 7 meter will be easier than the 5-meter bentonite because the Sodium Montmorillonite content is higher. The activation effort was focused on the 7-meter local bentonite sample since it showed better properties in terms of viscosity build up and fluid loss control. A new cost-effective activation method was conducted compared to the previous methods in the literature. Soda ash is an important step to convert or to increase the Na/Ca ratio to ensure higher swelling capacity.
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