Добірка наукової літератури з теми "Fluidised bed drying"
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Статті в журналах з теми "Fluidised bed drying"
López Fontal, Elkin Mauricio. "Coffe drying on fluidised bed." Ingeniería e Investigación 26, no. 1 (January 1, 2006): 22–26. http://dx.doi.org/10.15446/ing.investig.v26n1.14684.
Повний текст джерелаSoponronnarit, Somchart, Thanit Swasdisevi, Somboon Wetchacama, and Wivat Wutiwiwatchai. "Fluidised bed drying of soybeans." Journal of Stored Products Research 37, no. 2 (April 2001): 133–51. http://dx.doi.org/10.1016/s0022-474x(00)00015-1.
Повний текст джерелаGazor, H. R., and A. Mohsenimanesh. "Modelling the drying kinetics of canola in fluidised bed dryer." Czech Journal of Food Sciences 28, No. 6 (December 13, 2010): 531–37. http://dx.doi.org/10.17221/256/2009-cjfs.
Повний текст джерелаTaechapairoj, Chaiyong, Isares Dhuchakallaya, Somchart Soponronnarit, Somboon Wetchacama, and Somkiat Prachayawarakorn. "Superheated steam fluidised bed paddy drying." Journal of Food Engineering 58, no. 1 (June 2003): 67–73. http://dx.doi.org/10.1016/s0260-8774(02)00335-7.
Повний текст джерелаAnantharaman, N., S. Sundaram, and S. H. Ibrahim. "Fluidised bed drying of agro products." Bioprocess Engineering 23, no. 4 (October 20, 2000): 411–15. http://dx.doi.org/10.1007/s004499900184.
Повний текст джерелаLópez Fontal, Elkin Mauricio. "Fuzzy logic systems applied to fluidise bed coffee drying." Ingeniería e Investigación 25, no. 3 (September 1, 2005): 84–91. http://dx.doi.org/10.15446/ing.investig.v25n3.14671.
Повний текст джерелаThomas, P. P., and Y. B. G. Varma. "Fluidised bed drying of granular food materials." Powder Technology 69, no. 3 (March 1992): 213–22. http://dx.doi.org/10.1016/0032-5910(92)80012-l.
Повний текст джерелаValle Vargas, Marcelo Fernando, Ricardo Durán Baron, Jader Alean, and Héctor J. Ciro Velasquez. "Drying kinetics of organic parchment coffee beans (Coffea arabica L.) using microwave fluidised bed: Semi-theoretical modeling." Revista Ingenierías Universidad de Medellín 20, no. 39 (October 23, 2020): 167–83. http://dx.doi.org/10.22395/rium.v20n39a10.
Повний текст джерелаCiesielski, K., and I. Zbicinski. "HYBRID NEURAL MODELLING OF FLUIDISED BED DRYING PROCESS." Drying Technology 19, no. 8 (August 31, 2001): 1725–38. http://dx.doi.org/10.1081/drt-100107269.
Повний текст джерелаSkoneczna-Łuczków, Joanna, and Włodzimierz Ciesielczyk. "Exergetic Analysis For A Complete Node Of Fluidised-Bed Drying Of Poppy Seeds." Chemical and Process Engineering 36, no. 4 (December 1, 2015): 437–47. http://dx.doi.org/10.1515/cpe-2015-0031.
Повний текст джерелаДисертації з теми "Fluidised bed drying"
Ireland, Emma. "The impact of high frequency flow pulsation on fluidised bed drying." Thesis, University of Sheffield, 2016. http://etheses.whiterose.ac.uk/16550/.
Повний текст джерелаRaghavan, Rambali Sundara. "Optimisation of fluidised bed drying using electrical capacitance tomography sensor modelling and measurement." Thesis, University of Manchester, 2008. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.493952.
Повний текст джерелаPicado, Apolinar. "An Analytical Solution Applied to Heat and Mass Transfer in a Vibrated Fluidised Bed Dryer." Licentiate thesis, KTH, Teknisk strömningslära, 2011. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-34241.
Повний текст джерелаQC 20110614
Laboulfie, Fabien. "Dépôt en couche mince d'un multi-matériau à la surface de particules solides : application à l'enrobage de particules alimentaires." Phd thesis, Toulouse, INPT, 2013. http://oatao.univ-toulouse.fr/18015/1/laboulfie.pdf.
Повний текст джерелаGoksu, Emel Iraz. "Fluidized Bed, Microwave And Microwave Assisted Fluidized Bed Drying Of Macaroni Beads." Master's thesis, METU, 2003. http://etd.lib.metu.edu.tr/upload/1098789/index.pdf.
Повний текст джерела0.08 mm diameter) were dried from about 20% to 12% moisture content in a fluidized bed of 7.6 cm diameter, in a domestic microwave oven with a power of 609 W and in the fluidized bed placed in the microwave oven conditions. In the experiments with the fluidized bed three air temperatures
50, 60 and 70°
C at an air velocity of 2.3 m/s and in those with the microwave oven two power levels
50% and 100% were used. The drying curves indicated that the drying rate increased with the air temperature and microwave power in each drying method. Microwave assisted fluidized bed drying reduced the drying time by about 50% and 11% on the average compared with the fluidized bed and microwave drying, respectively. Therefore, it was concluded that the drying time was reduced more by the effect of microwave energy than the fluidization. The effective diffusivities in the fluidized bed and microwave assisted fluidized bed drying were found to be in the order of 4.125x10-11 and 8.772x10-11 m2/s on the average, respectively. The effective diffusivities for the fluidized bed drying were fitted to an Arrhenius type of equation and the magnitude of the activation energy was found to be in the order of 12595 kJ/kg mol.
Roe, Eric A. "Vibrofluidized bed drying of citrus processing residue for byproduct recovery." [Tampa, Fla.] : University of South Florida, 2003. http://purl.fcla.edu/fcla/etd/SFE0000628.
Повний текст джерелаHajidavalloo, Ebrahim. "Hydrodynamic and thermal analysis of a fluidized bed drying system." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0024/NQ31525.pdf.
Повний текст джерелаРожновський, Максим Олександрович. "Удосконалення роботи сушарки киплячого шару у виробництві таблетованого ампіциліну". Master's thesis, КПІ ім. Ігоря Сікорського, 2020. https://ela.kpi.ua/handle/123456789/39550.
Повний текст джерелаExplanatory note to the diploma project "Improvement of the fluidized bed dryer in the production of ampicillin tablets" contains 92 pages, 39 references, 21 figures, 23 tables. In the master's dissertation the dryer with a fluidized bed and the improved part of the apparatus of the lattice of the dryer of the fluidized bed are considered. The lattice of the fluidized bed dryer belongs to the field of dryers used in food production lines and the pharmaceutical industry. The production of solid drugs (DR) is the most common and well-known technology in pharmacy, in which the first place in terms of the number of products are tablets. The basic requirement for finished products of any drug production is to ensure quality, safety and efficiency. Ensuring this requirement is due to the use of equipment with high functional compliance with current production technology. The proposed lattice of the fluidized bed dryer provides high-quality drying of the material and increases the efficiency of this dryer. To confirm the efficiency and reliability of the structure, thermal, hydraulic, structural and strength calculations of structural elements were performed. A patent search was carried out, due to which a comparative analysis of the main indicators of the dryer design with the current analogues was performed. The project also addresses issues related to the installation and operation of the heat exchanger. Calculations and drawings are made according to current standards, using modem system and information technologies.
Сухецький, Андрій Геннадійович. "Модернізація решітки сушарки псевдозрідженого шару для дослідження процесу псевдозрідження". Master's thesis, КПІ ім. Ігоря Сікорського, 2019. https://ela.kpi.ua/handle/123456789/34117.
Повний текст джерелаThe explanatory note to the diploma project "Modernization of the fluidized bed dryer grid for the study of fluidization process" contains 96 pages, 37 literary sources, 23 drawings, 21 tables. The master's thesis deals with the fluidized bed dryer and the improved part of the apparatus of the fluidized bed dryer grid. The fluidized bed dryer grate belongs to the field of drying apparatus used in food production lines and the pharmaceutical industry. What is new is that the grate through which the air passes has sloping openings, which are arranged in an Archimedes spiral to create vortex flows during material drying. The proposed fluidized bed dryer grille provides high-quality drying of the material and increases the efficiency of the dryer. Thermal, hydraulic, structural and durable calculations of structural elements were carried out to confirm the construction's reliability and reliability, computer analysis and the necessary «Ansys» calculations were performed to verify the machine's performance. A patent search was carried out, whereby a comparative analysis of the main parameters of the design of the dryer with its existing analogues was performed. The project also addresses the issues of installation and operation of the heat exchanger. Calculations and drawings are made according to current standards, using modem system and information technologies.
ALMEIDA, Marcello Maia de. "Secagem de fatias e pedaços cúbicos de goiaba (Pisidium guajava L)." Universidade Federal de Campina Grande, 2004. http://dspace.sti.ufcg.edu.br:8080/jspui/handle/riufcg/1858.
Повний текст джерелаMade available in DSpace on 2018-10-01T13:55:41Z (GMT). No. of bitstreams: 1 MARCELLO MAIA DE ALMEIDA - TESE PPGEP 2004..pdf: 16341545 bytes, checksum: 6b12541c4495c47b84602868e8133365 (MD5) Previous issue date: 2004-12-06
Neste trabalho estudou-se inicialmente a secagem de fatias de goiabas cortadas no sentido polar da fruta, os resultados obtidos mostraram que o produto apresentou alterações desfavoráveis a comercialização, apresentando alteração significativa na cor, escurecimento, como também, na textura das fatias. Numa segunda etapa utilizou-se os processos combinados de leito fixo/leito de jorro e de leito fixo/leito fluidizado para a secagem de pedaços cúbicos de goiaba obtidos do mesocarpo da fruta. Inicialmente, fez-se um estudo fluidodinâmico dos pedaços cúbicos de goiaba em leito de jorro e leito fluidizado o qual mostrou a viabilidade do uso dessas técnicas, embora as propriedades físicas do material após pré-secagem em leito fixo tenham afetado sensivelmente a fluidodinâmica dos leitos, os quais sofreram modificações estruturais. No estudo fluidodinâmico em leito de jorro foram determinadas a velocidade mínima de jorro e a altura máxima capaz de manter o jorro estável. Os resultados obtidos experimentalmente foram comparados com correlações da literatura e mostraram boa concordância. Em leito fluidizado determinou-se a velocidade de mínima fluidização experimental os resultados obtidos apresentaram boa com os determinados através de correlações empíricas. Posteriormente, realizou-se um estudo das propriedades físicas, propriedades térmicas e um estudo do equilíbrio higroscópico dos pedaços cúbicos da fruta. Os resultados encontrados da massa específica e do diâmetro mostraram que estes se enquadram na categoria D, segundo a classificação de Geldart, o que favorece a um jorro e fluidização incipiente. Em relação ao estudo do encolhimento dos cubos observou-se um comportamento linear com o volume par todos os níveis de umidade do produto durante a secagem. Contudo, para umidade de 1,5 em base seca, durante a secagem em leito de jorro, duas regiões bem distintas foram caracterizadas pela mudança na inclinação da curva. Em relação às propriedades térmicas estas apresentaram a mesma tendência, ou seja, aumentando com a elevação da umidade passando por um máximo correspondente ao máximo encontrado na massa específica. No estudo do equilíbrio higroscópico, observou-se que as isotermas, dentro da faixa de temperatura estudada, foram ajustadas ao modelo de Henderson apresentando um ajuste satisfatório, não se observando efeito da temperatura. No estudo da cinética de secagem utilizou-se o modelo difusional para esferas, truncado em quatro termos levando-se em conta o efeito do encolhimento, os resultados obtidos para leito fixo/leito de jorro ajustou bem os dados experimentais. Por outro lado, este modelo não prediz satisfatoriamente o comportamento da secagem em leito fixo/leito fluidizado haja vista o fator encolhimento não ter sido utilizado no modelo. O coeficiente de difusão efetivo para níveis de umidades mais elevados apresentaram a mesma ordem de grandeza para ambos os processos independente da altura do leito. A hipótese de controle difusional externo desprezível foi confirmada a partir do número de Biot de massa que foi muito elevado. O desempenho dos secadores foi realizado a partir da determinação das perdas de vitamina C e da eficiência de energética do processo. Verificou-se que a degradação do ácido ascórbico é mais acentuada em leito de fluidizado. Com relação a eficiência energética valores mais elevados foram encontrados em níveis de umidade mais acentuadas. De maneira geral, podemos afirmar que o sistema combinado de secagem de pedaços cúbicos de goiaba aponta de forma promissora para a produção de um novo produto obtido a partir de uma tecnologia simples, obtendo-se produtos com características adequadas à comercialização.
Initially, the objective of this work was to study the drying of whole guava slices cut in the fruit polar direction. The results pointed out that this process introduced adverse aspects for commercialization, such as significant alteration in color, darkness, and slices texture. Looking for a better product quality, studies on combined process fixed bed/spouted bed and fixed bed/fluidized bed for guava cubic pieces drying were performed in a second step. The guava slices were obtained by cutting the fruit pith in approximately 1cm cubic form. A fluid-dynamic study in spouted bed and fluidized bed showed the feasibility of this technique, although the physical properties of guava cubic pieces after pre-drying in fixed bed affected the fluid-dynamics behavior causing structural alteration. The minimum spouting velocity, the maximum spoutable height and the minimum fluidization velocity as well, were determined and the obtained results showed good agreement with literature correlations. In order to characterize the fruit cubic pieces, the physical properties, thermal properties and hygroscopic equilibrium were determined as a function of the moisture content. The results of density and diameter pointed out that the particles were classified as type D according Geldart. In such situation, one may expect a stable spouting with incipient fluidization. In relation to the study of the shrinking and deformation it was observed a linear volume contraction with the moisture reduction at all levels of product moisture content during drying, together with a rapid rounding of the cube vertices. Spite the linear behavior, two distinct regions, limited by 1,5 (db) moisture content, had been observed during the spouted bed drying, characterized by the change in the curve slope. The thermal properties, thermal conductivity, thermal diffusivity and specific heat, were measured as a function of moisture content. All three presented the same trend: it was observed a region of increasing value of the property with the moisture content with a maximum in the region of maximum density. The Henderson model was adjusted to the hygroscopic equilibrium isotherms; the results showed a good fitting and little effect of temperature was observed within the studied temperature range. A diffusional model for spheres was proposed to describe the drying kinetics. The Fick's solution, truncated in four terms of the series and including the shrinking effect, was used in the modeling. The fixed bed/spouted bed experimental data showed a good fitting whereas this model does not satisfactorily predict the drying behavior in the fixed bed/fluidized bed system. The failure in this case is probably due to the shrinking factor was not considered in the model for fixed/fluidized bed. The effective diffusion coefficient for high levels of moisture presented the same order of magnitude for both processes, independent of the bed height. The internal diffusional control hypothesis for the mass transfer was then confirmed by the high mass Biot number, calculated for both processes. The driers performance was evaluated by means of analysis of the vitamin C loss and process energetic efficiency. It was verified that the acid ascorbic degradation is more significant in the fluidized bed, probably due to the instable behavior of this configuration. With regard to the energy efficiency higher values were found for the highest moisture content levels. In general, it is concluded that the combined system fixed/spouted or fixed/fluidized bed drying of guava pieces is an expecting suitable process to obtain a new product by a simple technology, getting products with adequate characteristics to the commercialization.
Книги з теми "Fluidised bed drying"
Temple, S. J. Control of fluidized bed tea drying. Wageningen: Wageningen Universiteit, 2000.
Знайти повний текст джерелаC, Payne R., and Commission of the European Communities. Directorate-General for Science, Research and Development., eds. Production of hot gas for drying processes using fluidised bed combustion of coal. Luxembourg: Commission of the European Communities, 1985.
Знайти повний текст джерелаModelling and Experimental Study of Granular Material Drying in a Vibrated Fluidized Bed. Argentina: The Argentine Association of Chemical Engineers, 2006.
Знайти повний текст джерелаЧастини книг з теми "Fluidised bed drying"
Bück, Andreas, Robert Dürr, and Nicole Vorhauer. "Feedback Control of Fluidised Bed Drying." In Intelligent Control in Drying, 403–23. Boca Raton : Taylor & Francis, a CRC title, part of the Taylor & Francis imprint, a member of the Taylor & Francis Group, the academic division of T&F Informa, plc, 2018. | Series: Advances in drying science & technology: CRC Press, 2018. http://dx.doi.org/10.1201/9780429443183-20.
Повний текст джерелаShilton, N. C., and K. Niranjan. "Puff Drying of Foods in a Fluidised Bed." In Developments in Food Engineering, 337–39. Boston, MA: Springer US, 1994. http://dx.doi.org/10.1007/978-1-4615-2674-2_105.
Повний текст джерелаBahu, R. E. "Fluidized bed dryers." In Industrial Drying of Foods, 65–89. Boston, MA: Springer US, 1997. http://dx.doi.org/10.1007/978-1-4613-1123-2_4.
Повний текст джерелаSuzuki, Kanichi, Masaaki Ikeda, Muneharu Esaka, and Kiyoshi Kubota. "Characteristics of Vibro-Fluidized Bed Freeze Drying." In Drying ’85, 254–59. Berlin, Heidelberg: Springer Berlin Heidelberg, 1985. http://dx.doi.org/10.1007/978-3-662-21830-3_32.
Повний текст джерелаMoriyama, Takashi, Hiroshi Itaya, and Akihiko Nakamura. "A New Fluidized Bed Dryer for Amorphous Slag." In Drying ’85, 390–95. Berlin, Heidelberg: Springer Berlin Heidelberg, 1985. http://dx.doi.org/10.1007/978-3-662-21830-3_52.
Повний текст джерелаPatil, R. T., and Dattatreya M. Kadam. "Hot Air Drying Design: Fluidized Bed Drying." In Handbook of Food Process Design, 542–77. Oxford, UK: Wiley-Blackwell, 2012. http://dx.doi.org/10.1002/9781444398274.ch20.
Повний текст джерелаPeglow, Mirko, Sergiy Antonyuk, Michael Jacob, Stefan Palzer, Stefan Heinrich, and Evangelos Tsotsas. "Particle Formulation in Spray Fluidized Beds." In Modern Drying Technology, 295–378. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2014. http://dx.doi.org/10.1002/9783527631728.ch20.
Повний текст джерелаPeglow, Mirko, Sergiy Antonyuk, Michael Jacob, Stefan Palzer, Stefan Heinrich, and Evangelos Tsotsas. "Particle Formulation in Spray Fluidized Beds." In Modern Drying Technology, 295–378. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2011. http://dx.doi.org/10.1002/9783527631667.ch7.
Повний текст джерелаTsotsas, Evangelos, Stefan Heinrich, Michael Jacob, Mirko Peglow, and Lothar Mörl. "Intensification of Fluidized-Bed Processes for Drying and Formulation." In Modern Drying Technology, 85–130. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2014. http://dx.doi.org/10.1002/9783527631728.ch32.
Повний текст джерелаTsotsas, Evangelos, Stefan Heinrich, Michael Jacob, Mirko Peglow, and Lothar Mörl. "Intensification of Fluidized-Bed Processes for Drying and Formulation." In Modern Drying Technology, 85–130. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2014. http://dx.doi.org/10.1002/9783527631704.ch04.
Повний текст джерелаТези доповідей конференцій з теми "Fluidised bed drying"
SRINIVASAKANNAN, C., and N. BALASUBRAMANIAM. "BATCH FLUIDISED BED DRYING: ANALYSIS ON KINETIC MODELS." In The Proceedings of the 5th Asia-Pacific Drying Conference. World Scientific Publishing Company, 2007. http://dx.doi.org/10.1142/9789812771957_0092.
Повний текст джерелаZammouri, Amel, N. Boudhrioua Mihoubi, and N. Kechaou. "Comparison between bubbling and turbulent regime for the simulation of batch pharmaceutical powders fluidized bed drying." In 21st International Drying Symposium. Valencia: Universitat Politècnica València, 2018. http://dx.doi.org/10.4995/ids2018.2018.7703.
Повний текст джерелаMEOR TALIB, MEOR ZAINAL, SUHAILA BINTI ABDULLAH, WAN RAMLI WAN DAUD, and SITI MASRINDA TASIRIN. "ON-LINE WEB-BASED DESIGN SIMULATOR OF A PLUG FLOW FLUIDISED BED CROSS-FLOW DRYER." In The Proceedings of the 5th Asia-Pacific Drying Conference. World Scientific Publishing Company, 2007. http://dx.doi.org/10.1142/9789812771957_0091.
Повний текст джерелаChen, Guanyi, Gang Li, Michel P. Glazer, Chunlei Zhang, and J. Andries. "Operation of a Circulating Fluidised Bed Biomass Gasifier." In ASME Turbo Expo 2004: Power for Land, Sea, and Air. ASMEDC, 2004. http://dx.doi.org/10.1115/gt2004-53659.
Повний текст джерелаWang, Haigang, Wuqiang Yang, Ian Proctor, Julian Taylor, Alex Marr, and Trevor Page. "Online monitoring and flow regime identification of fluidised bed drying and granulation processes." In 2009 IEEE International Workshop on Imaging Systems and Techniques (IST). IEEE, 2009. http://dx.doi.org/10.1109/ist.2009.5071643.
Повний текст джерелаA˚mand, Lars-Erik, Bo Leckner, Solvie Herstad Sva¨rd, Marianne Gyllenhammar, David Eskilsson, and Claes Tullin. "Co-Combustion of Pulp- and Paper Sludge With Wood: Emissions of Nitrogen, Sulphur and Chlorine Compounds." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-097.
Повний текст джерелаWard, John, Roy Garwood, Randall Bowen, Maurice Fisher, and David Gent. "Design and Development of an Improved Air Distributor for a Large Coal-Fired Fluidised Bed Combustor." In ASME 2008 International Mechanical Engineering Congress and Exposition. ASMEDC, 2008. http://dx.doi.org/10.1115/imece2008-67224.
Повний текст джерелаWard, John, Muhammad Akram, and Roy Garwood. "Fluidised Bed Combustion of Blends of Coal and Pressed Sugar Beet Pulp." In ASME/JSME 2011 8th Thermal Engineering Joint Conference. ASMEDC, 2011. http://dx.doi.org/10.1115/ajtec2011-44093.
Повний текст джерелаKaur, Amanat, Yvan Gariépy, Valérie Orsat, and Vijaya Raghavan. "Microwave assisted fluidized bed drying of celery." In 21st International Drying Symposium. Valencia: Universitat Politècnica València, 2018. http://dx.doi.org/10.4995/ids2018.2018.7368.
Повний текст джерелаYüksel, Hira, Tuğçe Türkoğlu, Hale Baykal, Gülşah Çalışkan Koç, and Safiye Nur Dirim. "The intermittent drying of wheat by microwave and fluidized bed drying." In 21st International Drying Symposium. Valencia: Universitat Politècnica València, 2018. http://dx.doi.org/10.4995/ids2018.2018.7467.
Повний текст джерелаЗвіти організацій з теми "Fluidised bed drying"
Boysen, J. E., C. Y. Cha, F. A. Barbour, T. F. Turner, T. W. Kang, M. H. Berggren, R. F. Hogsett, and M. C. Jha. Development of an advanced process for drying fine coal in an inclined fluidized bed. Office of Scientific and Technical Information (OSTI), February 1990. http://dx.doi.org/10.2172/6273657.
Повний текст джерелаBoysen, J., T. Kang, C. Cha, M. Berggren, and M. Jha. Development of an advanced process for drying fine coal in an inclined fluidized bed. Office of Scientific and Technical Information (OSTI), October 1989. http://dx.doi.org/10.2172/5586826.
Повний текст джерелаBoysen, J. E., C. Y. Cha, M. H. Berggren, and M. C. Jha. Development of an advanced process for drying fine coal in an inclined fluidized bed: Technical progress report for the second quarter, January 19--March 31, 1989. Office of Scientific and Technical Information (OSTI), May 1989. http://dx.doi.org/10.2172/6089545.
Повний текст джерела