Дисертації з теми "Crystallisation processes"
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Ma, Chaoyang. "Particle shape distribution control in crystallisation processes." Thesis, University of Leeds, 2010. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.531612.
Повний текст джерелаSchacht, Ulrich. "Control of nucleation in continuous crystallisation processes." Thesis, University of Strathclyde, 2014. http://oleg.lib.strath.ac.uk:80/R/?func=dbin-jump-full&object_id=24858.
Повний текст джерелаAbebe, Solomon Befekadu. "Monitoring batch crystallisation processes using near infrared spectroscopy." Thesis, University of Leeds, 2007. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.446057.
Повний текст джерелаMabbott, Fraser Adam. "Towards understanding fouling mechanisms in continuous crystallisation processes." Thesis, University of Strathclyde, 2017. http://digitool.lib.strath.ac.uk:80/R/?func=dbin-jump-full&object_id=28675.
Повний текст джерелаLewis, Barrie. "The development of a Semi-Open Refrigeration Cycle for the crystallisation of aqueous salts." Thesis, University of South Wales, 1996. https://pure.southwales.ac.uk/en/studentthesis/the-development-of-a-semiopen-refrigeration-cycle-for-the-crystallisation-of-aqueous-salts(f7306f14-fe23-493f-a428-76b34a79ec80).html.
Повний текст джерелаRockey, Helen Anne. "The environmental control and clean technology of fuel emissions and crystallisation processes." Thesis, Brunel University, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.394707.
Повний текст джерелаMathieson, Gillian Ann. "Olivine-basaltic melt re-equilibration rates and their implications for crystallisation processes." Thesis, University of Sheffield, 1987. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.343508.
Повний текст джерелаParsons, Matthew D. "Optical and mechanical studies of the air/water interface and crystallisation processes." Thesis, University of Southampton, 2018. https://eprints.soton.ac.uk/422298/.
Повний текст джерелаAlhseinat, Emad Yousef Mahmoud. "Characterisation and prediction of crystallisation fouling in reverse osmosis and nanofiltration membrane processes." Thesis, University of Edinburgh, 2013. http://hdl.handle.net/1842/7844.
Повний текст джерелаHickman, Ian. "Chromium segregation and its effect on crystallisation processes in green soda-lime-silica glass." Thesis, University of Sheffield, 2009. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.505561.
Повний текст джерелаZhao, Yanlin. "Methods for electrical impedance spectroscopy and tomography characterising particles in suspensions and crystallisation processes." Thesis, University of Leeds, 2012. http://etheses.whiterose.ac.uk/3409/.
Повний текст джерелаPalmer, Laura. "Investigation of batch and continuous crystallisation processes using non-invasive Raman and acoustic emission spectrometries." Thesis, University of Strathclyde, 2013. http://oleg.lib.strath.ac.uk:80/R/?func=dbin-jump-full&object_id=23215.
Повний текст джерелаAamir, Erum. "Population balance model-based optimal control of batch crystallisation processes for systematic crystal size distribution design." Thesis, Loughborough University, 2010. https://dspace.lboro.ac.uk/2134/6360.
Повний текст джерелаPenchev, Radoslav Yordanov. "Monitoring crystal size and growth processes during batch crystallisation via the use of acoustic attenuation spectroscopy." Thesis, University of Leeds, 2007. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.445842.
Повний текст джерелаAbu, Bakar Mohd R. "Process analytical technology based approaches for the monitoring and control of size and polymorphic form in pharmaceutical crystallisation processes." Thesis, Loughborough University, 2010. https://dspace.lboro.ac.uk/2134/6436.
Повний текст джерелаChabalenge, Billy, Sachin A. Korde, Adrian L. Kelly, Daniel Neagu, and Anant R. Paradkar. "Understanding Matrix Assisted Continuous Cocrystallisation using Data Mining approach in Quality by Design (QbD)." ACS, 2020. http://hdl.handle.net/10454/18005.
Повний текст джерелаThe present study demonstrates the application of decision tree algorithms to the co-crystallization process. Fifty four (54) batches of carbamazepine–salicylic acid co-crystals embedded in poly(ethylene oxide) were manufactured via hot melt extrusion and characterized by powder X-ray diffraction, differnetial scanning calorimetry, and near-infrared spectroscopy. This dataset was then applied in WEKA, which is an open-sourced machine learning software to study the effect of processing temperature, screw speed, screw configuration, and poly(ethylene oxide) concentration on the percentage of co-crystal conversion. The decision trees obtained provided statistically meaningful and easy-to-interpret rules, demonstrating the potential to use the method to make rational decisions during the development of co-crystallization processes.
Bretherton, Tracy Ann. "The design, development and testing of a non-invasive continuous crystalliser system for the study of calcium oxalate crystallisation processes." Doctoral thesis, University of Cape Town, 1996. http://hdl.handle.net/11427/16137.
Повний текст джерелаThe MSMPR was designed according to chemical engineering principles and tests showed that it conforms to the assumptions necessary for conventional MSMPR analysis. Various crystalliser offtakes and six system designs were developed and tested to allow measurements using the thermostatted flow cell. The flow cell allows for continuous measurement of the sample dispersion using a noninvasive monitoring instrument - a Malvern Particle Size Analyser. In this technique, measurement of the steady state crystal size distribution is based on a diffraction pattern produced by the particles in a parallel beam of monochromatic light. Comparative measurements were obtained by sampling directly from the crystalliser and analysing the product in a Coulter Counter. In this technique, the steady state crystal size distribution is measured by the change in resistance as particles, in an electrically conductive liquid, pass through the Coulter aperture. Due to the large volumes required by the crystalliser, it was necessary to pool urines. Aliquots of volume 1. 5 dm3 from the 24 hour urines of each of 8 male controls were pooled. The first series of experiments were performed to investigate the effect on calcium oxalate crystallisation of varying the concentration of sodium oxalate solutions used to initiate crystallisation, and also to investigate the effect of varying the temperature. A further series of experiments was performed to determine the effect of adding inhibitors individually (citrate, magnesium, chondroitin sulphate A) and in combination (citrate and magnesium). The inhibitor experiments were performed using two different approaches. In the first, the pooled urine was pre-treated with the inhibitor prior to being introduced into the crystalliser. In the second set of experiments, the inhibitor was introduced into the crystalliser via a separate, independent feed. It is suggested that these approaches represent crude models respectively of (a) the endogenous presence of inhibitors and (b) the oral administration of such inhibitors. Each individual experiment was performed using three different urine pools. The steady state crystal size distributions obtained from both the Coulter and the Malvern instruments were used to determine nucleation and growth rates in each urine. Scanning electron microscopy was used to obtain qualitative and semi-quantitative data related to crystal morphology, number, size and degree of aggregation. Both nucleation and growth rates increased as the concentrations of the initiating sodium oxalate solutions increased. Nucleation and growth rates also increased with increasing temperatures. In the latter series of experiments, different calcium oxalate crystal phases precipitated at the various temperatures. Citrate inhibited nucleation and growth of calcium oxalate, irrespective of how it was admitted to the crystalliser. Magnesium was found to inhibit growth only and, like citrate, this role was independent of how it was introduced into the crystalliser. Although both inhibited growth, the effect of the citrate was greater. When both components were added in combination, inhibition was observed to be additive. In all cases, inhibitory effects increased with increasing concentration. Chondroitin sulphate A was found to inhibit nucleation; inhibition of growth was minimal at the concentrations tested. Aggregation of calcium oxalate crystals was found to be inhibited by chondroitin sulphate A. The results of the calcium oxalate crystallisation kinetic studies, obtained by using Malvern particle sizing and Coulter Counter techniques independently of each other, showed general agreement. These results, in turn, were in agreement with the published results of others, thereby lending confidence to the findings and highlighting the potential application of the non-invasive continuous crystalliser in urolithiasis research.
Klimm, Kevin. "Differentiation and crystallisation processes in A-type granites an experimental study of the Wangrah Suite, Australia = Differenzierungs- und Kristallisationsprozesse in A-Typ-Graniten /." [S.l. : s.n.], 2004. http://deposit.ddb.de/cgi-bin/dokserv?idn=972117229.
Повний текст джерелаPowell, Keddon A. "Improving continuous crystallisation using process analytical technologies : design of a novel periodic flow process." Thesis, Loughborough University, 2017. https://dspace.lboro.ac.uk/2134/23982.
Повний текст джерелаApshingekar, Prafulla P. "Applications of ultrasound in pharmaceutical processing and analytics." Thesis, University of Bradford, 2014. http://hdl.handle.net/10454/14127.
Повний текст джерелаSelander, André. "Concept development to extract sodium sulfate from an aqueous solution." Thesis, Luleå tekniska universitet, Institutionen för teknikvetenskap och matematik, 2021. http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-85741.
Повний текст джерелаNu när intresset ökar, för att nå en hållbar infrastruktur, så experimenterat SCA med möjligheten att producera förnybara kolväten från svartlut som kan extraheras från en sulfatprocess. Vid extrahering av svartluten tas dock mycket natriumbaserade föreningar bort från återvinningsprocessen och när kolväten produceras i SCA:s bioraffinaderi fastnar dessa föreningar i en vattenlösning. Den lösningen tas emot vid 50°C och de natriumbaserade föreningarna är huvudsakligen natriumsulfat och natriumkarbonat, där lösningen också innehåller organiska föreningar och ett lösningsmedel som används i bioraffinaderiet. Denna avhandling fokuserade på att bygga ett koncept för att extrahera natriumsulfat från vattenlösningen. Avhandlingen omfattade också om ytterligare förberedande arbete måste göras av lösningen innan man extraherar natriumsulfat. Slutligen skapades ett flödesschema som kartlägger den energi som behövs för processen. Metoden som bestämde sig för att användas var kristallisering genom kylning av lösningen. Genom att kyla lösningen minskar lösligheten av natriumsulfater vilket leder till att natriumsulfat faller ut ur lösningen som kristaller. Det bestämdes att lösningsmedlet som lösningen innehåller skulle extraheras om lösningsmedlets koktemperatur är under 100°C. Vidare, genom att kyla lösningen under omrörning till 15°C med en uppehållstid på 3 timmar, kan oönskade ämnen extraheras. Genom att senare kyla lösningen under omrörning till 5°C med en uppehållstid på 1 timme gav natriumsulfatdekahydrat (Na2SO4·10H2O) med små mängder organiska föreningar. Genom att avlägsna vattnet nådde den torra produkten en renhet av 94 vikt% natriumsulfat med ett utbyte av 12% (massa torr produkt/massa vattenlösning). Detta resultat nådde de specifika mål som sattes i början av denna avhandling, vilket var att nå en renhet av 90 vikt% natriumsulfat med ett utbyte på 5%. Energiintensiteten för att förånga lösningsmedlet förväntas vara hög. Det beror mycket på vilket lösningsmedel som används. Denna process kan dock använda den lägsta ångkvaliteten som finns tillgänglig från massafabriken. Det förväntas att kylningen kommer att kräva stora mängder kylvatten och höga investeringskostnader för värmeväxlaren. Ändå är detta en viktig del av processen för att minska behovet av kylare som drivs av elektricitet.
Abdul, Abas Riad. "Experimental Studies of Thermal Diffusivities concerning some Industrially Important Systems." Doctoral thesis, Stockholm : School of Industrial Engineering and Management, Royal Institute of Technology, 2006. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-3864.
Повний текст джерелаKlimm, Kevin [Verfasser]. "Differentiation and crystallisation processes in A-type granites : an experimental study of the Wangrah Suite, Australia = Differenzierungs- und Kristallisationsprozesse in A-Typ-Graniten / von Kevin Klimm." 2004. http://d-nb.info/972117229/34.
Повний текст джерелаArlow, Antoinette. "Crystallisation aspects of the wet-process phosphoric acid industry." Diss., 2004. http://hdl.handle.net/2263/23966.
Повний текст джерела- Agitation increases x-compound precipitation and can be used commercially to increase the precipitation rate to a point where sludge can be removed before transportation.
- Adding x-compound seeding crystals or magnesium ions also increases precipitation.
- Adding gypsum, sodium, hexafluorosilicates or fluorosilic acid reduces the precipitation, with sodium ions producing the lowest yield. This reduction is however not sufficient to be used commercially.
Dissertation (MSc(Chemical Engineering))--University of Pretoria, 2005.
Chemical Engineering
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