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Littérature scientifique sur le sujet « Scale-up industriale »

Auteur : Grafiati

Publié le 9 mars 2023

Mis à jour le 10 mars 2023

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Articles de revues sur le sujet "Scale-up industriale"

Sutherland, I. A., L. Brown, A. S. Graham, G. G. Guillon, D. Hawes, L. Janaway, R. Whiteside et P. Wood. « Industrial Scale-Up of Countercurrent Chromatography : Predictive Scale-Up ». Journal of Chromatographic Science 39, n^o 1 (1 janvier 2001) : 21–28. http://dx.doi.org/10.1093/chromsci/39.1.21.

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López, C. M. « ESCALAMIENTO PILOTO DE LA SÍNTESIS DE ZEOLITA NaA A PARTIR DE GELES ALUMINOSILICATOS OBTENIDOS CON MATERIALES INDUSTRIALES VENEZOLANOS NO TRATADOS ». Revista Mexicana de Ingeniería Química 17, n^o 1 (26 mars 2018) : 75–86. http://dx.doi.org/10.24275/uam/izt/dcbi/revmexingquim/2018v17n1/lopezc.

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Sadighi, Sepehr, Seyed Reza Seif Mohaddecy et Mehdi Rashidzadeh. « Modeling, Evaluating and Scaling up a Commercial Multilayer Claus Converter Based on Bench Scale Experiments ». Bulletin of Chemical Reaction Engineering & ; Catalysis 15, n^o 2 (25 mai 2020) : 465–75. http://dx.doi.org/10.9767/bcrec.15.2.7521.465-475.

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Industrial scale reactors work adiabatically and measuring their performance in an isothermal bench scale reactor is faced with uncertainties. In this research, based on kinetic models previously developed for alumina and titania commercial Claus catalysts, a multilayer bench scale model is constructed, and it is applied to simulate the behavior of an industrial scale Claus converter. It is shown that performing the bench scale isothermal experiments at the temperature of 307 ºC can reliably exhibit the activity of catalytic layers of an industrial Claus converter operating at the weighted average bed temperature (WABT) of 289 ºC. Additionally, an adiabatic model is developed for a target industrial scale Claus reactor, and it is confirmed that this model can accurately predict the temperature, and molar percentages of H2S and CS2. Based on simulation results, 20% of excess amount of Claus catalysts should be loaded to compensate their deactivation during the process cycle life. Copyright © 2020 BCREC Group. All rights reserved

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Jackson, A. T. « Some problems of industrial scale-up ». Journal of Biological Education 19, n^o 1 (mars 1985) : 48–52. http://dx.doi.org/10.1080/00219266.1985.9654686.

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Geipel, Christian, Karl Hauptmeier, Kai Herbrig, Frank Mittmann, Markus Münch, Martin Pötschke, Ludwig Reichel et al. « Stack Development and Industrial Scale-Up ». ECS Transactions 91, n^o 1 (10 juillet 2019) : 123–32. http://dx.doi.org/10.1149/09101.0123ecst.

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Sutherland, I. A., A. J. Booth, L. Brown, B. Kemp, H. Kidwell, D. Games, A. S. Graham et al. « INDUSTRIAL SCALE-UP OF COUNTERCURRENT CHROMATOGRAPHY ». Journal of Liquid Chromatography & ; Related Technologies 24, n^o 11-12 (30 juin 2001) : 1533–53. http://dx.doi.org/10.1081/jlc-100104362.

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Meulenberg, Rogier. « Scale up of industrial enzyme production ». New Biotechnology 29 (septembre 2012) : S75. http://dx.doi.org/10.1016/j.nbt.2012.08.209.

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Rodriguez, F., M. Ramirez, R. Ruiz et F. Concha. « Scale-up procedure for industrial cage mills ». International Journal of Mineral Processing 97, n^o 1-4 (novembre 2010) : 39–43. http://dx.doi.org/10.1016/j.minpro.2010.07.010.

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Mascarenhas, João, M. Alexandra Barreiros et Maria João Brites. « Scale up of microwave annealed FA0.83Cs0.17PbI1.8Br1.2 perovskite towards an industrial scale ». Materials Letters : X 5 (mars 2020) : 100029. http://dx.doi.org/10.1016/j.mlblux.2019.100029.

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Hoeks, Frans W. J. M. M., Lotte A. Boon, Fabian Studer, Menno O. Wolff, Freija van der Schot, Peter Vrabél, Rob G. J. M. van der Lans et al. « Scale-up of stirring as foam disruption (SAFD) to industrial scale ». Journal of Industrial Microbiology & ; Biotechnology 30, n^o 2 (février 2003) : 118–28. http://dx.doi.org/10.1007/s10295-003-0023-7.

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Thèses sur le sujet "Scale-up industriale"

Santagiuliana, Michele <1992&gt. « Trasferimento e scale-up di processo produttivo per la sintesi di molecole di interesse farmaceutico ». Master's Degree Thesis, Università Ca' Foscari Venezia, 2019. http://hdl.handle.net/10579/16034.

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La presente tesi è stata sviluppata nel corso dello stage svolto presso FIS – Fabbrica Italiana Sintetici, uno dei principali produttori italiani di principi attivi e intermedi per l’industria farmaceutica. L’attività, svolta presso i laboratori del reparto R&D, ha riguardato lo studio del processo produttivo per la sintesi di un principio attivo commissionata da una casa farmaceutica. Sono stati affrontati tutti gli aspetti coinvolti nelle fasi di trasferimento e scale-up di processo, quali: studi di stabilità, compatibilità dei materiali, studi di solubilità, valutazione dei reflui, valutazione di fluido dinamica, valutazione di sicurezza di processo. Per ragioni di riservatezza, tutti i dati sensibili contenuti in questa tesi verranno oscurati in fase di pubblicazione.

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Cristallini, Pietro Paolo. « Atom transfer radical polymerization di monomeri polari : studio delle condizioni utili per uno scale-up industriale ». Master's thesis, Alma Mater Studiorum - Università di Bologna, 2017. http://amslaurea.unibo.it/13377/.

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In questo progetto è stata studiata la sintesi di copolimeri a blocchi poli(N-vinil caprolattame)-b-poli(vinil acetato) (PNVCL-b-PVAc) mediante Atom Transfer Radical Polymerization (ATRP). In visione di una futura produzione di questi materiali a livello industriale, è stato ritenuto interessante studiare questo processo utilizzando un solvente con alto valore di flash point, in particolare il polipropilen glicole Mn=1000g/mol (PPG-1000) (flash point 229°C). Inoltre, si è scelto di lavorare a temperature comprese tra 50 e 80°C, in modo da poter asportare il calore di reazione utilizzando semplicemente acqua non sottoraffreddata e ottenendo così una diminuzione dei costi di produzione. Sono quindi stati effettuati degli studi cinetici relativi alla sintesi dei due omopolimeri PNVCL e PVAc al fine di ottimizzare le condizione di sintesi ed ottenere un controllo sull’intero processo. In this work the synthesis of poly(N-vinyl caprolactam)-b-poly(vinyl acetate) (PNVCL-b-PVAc) block copolymers by Atom Transfer Radical Polymerization (ATRP) was studied. The process was carried out in presence of an high flash point solvent [polypropylene glycol Mn=1000g/mol (PPG-1000) (fp=229°C)] in order to attend to the environmental requirements of an industrial production and at temperature between 50 and 80°C with the aim to avoid the use of undercooled water for the heat removal, and hence reduce the production costs. Thus kinetic studies on the synthesis of PNVCL and PVAc homopolymers were performed in order to optimize the systems and obtain the control on the overall process.

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CAPITANI, CHIARA. « Synthesis of semiconductor colloidal nanocrystals with large Stokes-shift for luminescent solar concentrators ». Doctoral thesis, Università degli Studi di Milano-Bicocca, 2022. http://hdl.handle.net/10281/366195.

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I concentratori solari luminescenti (LSCs) sono delle guide d’onda composti da una matrice polimerica drogata o ricoperta con fluorofori. La luce solare diretta e/o diffusa che penetra nella matrice è assorbita dai fluorofori e poi riemessa dagli stessi con energia minore. La luce emessa, grazie alla riflessione totale interna, propaga fino a raggiungere i bordi della guida d’onda dove è convertita in elettricità da celle fotovoltaiche poste sul perimetro della matrice. L’efficienza del dispositivo è ridotta da numerosi processi di perdita, sia dovuti alla riflessione della matrice e al cono di fuga, sia quelli che dipendono dalle caratteristiche dei fluorofori, come il coefficiente di assorbimento, il quantum yield (QY) di fotoluminescenza (PL) e il riassorbimento. Per minimizzare tali perdite, una buona alternativa ai tradizionali fluorofori sono i quantum dots (QDs) colloidali che presentano solitamente un elevato QY, un alto coefficiente di assorbimento e una lunghezza d’onda di emissione controllabile cambiando le dimensioni dei nanocristalli tramite modifiche dei parametri di sintesi. Inoltre, ingegnerizzando opportunamente i QDs, è possibile realizzare particelle con elevato Stokes-shift tra gli spettri di assorbimento ed emissione, in modo da ridurre quanto più possibile il riassorbimento. Il progetto si è quindi focalizzato sullo sviluppo della sintesi di QDs, al fine di ottimizzare il QY di fotoluminescenza, la compatibilizzazione con la matrice polimerica e la fotostabilità, limitando comunque il riassorbimento. Inoltre. la procedura di sintesi deve essere facilmente trasportabile su volumi industriali, per soddisfare il fabbisogno di produzioni di elevati metri quadrati di LSCs. Durante i tre anni di progetto di dottorato in Alto Apprendistato ho potuto sviluppare una procedura di sintesi che consiste in quattro step: • crescita di nanocristalli di CuInS2 core; • formazione del quaternario tramite aggiunta di zinco (ZnCuInS2); passaggio cruciale per aumentare il QY e controllare la lunghezza d’onda di emissione; • crescita di una shell di solfuro di zinco (ZnCuINS2/ZnS) per passivare la superficie dei nanocristalli, aumentare il QY e la fotostabilità; • trattamento post sintesi di scambio di leganti parziale per migliorare la solubilità nella matrice polimerica. I nanocristalli così prodotti mostrano un QY del 60% ed un’ottima solubilità nella matrice polimerica. Infatti, è stato prodotto un LSC di grande dimensione (30 cm x 30 cm x 0.7 cm) la cui optical power efficiency, OPE = 6.8%. Inizialmente ho sviluppato la procedura di sintesi in un pallone di vetro da 25 mL, producendo 250 mg a sintesi. Grazie all’attrezzatura fornita da Glass to Power S.p.A ho potuto studiare lo scale-up della sintesi. Dapprima ho effettuato studi preliminare, per approfondire alcune possibili problematiche dovute all’aumento dei volumi, su palloni di maggiori dimensioni, 500 mL e 2 L. Analizzate e risolte le tematiche di riscaldamento e stop della sintesi ho effettuato sintesi in un reattore preindustriale producendo 300 g di nanocristalli di ZnCuINS2/ZnS. Oltre ad incrementare la produzione di sintesi da 250 mg a 300 g mi sono occupata dell’ottimizzazione della procedura di sintesi. Ho testato diverse strategie per incrementare il QY senza danneggiare la solubilità nel polimero. Grazie ad una variazione di reagente nel secondo step e ad un incremento dei layer della shell ho ottenuto nanocristalli con 80% di QY. Il prossimo step sarà effettuare lo scale-up di questa nuova procedura e produrre LSC di grandi dimensioni. Grazie alle collaborazioni con altri studenti di dottorato ho sintetizzato nanocristalli di calcogenuro drogati oro e opportunamente decorati con molecole coniugate per sistemi di up-conversion. Grazie all’introduzione dell’oro in questi sistemi si è ottenuta un’efficienza di up-conversion del 12%.
Luminescent solar concentrators (LSCs) are waveguides composed of a polymeric matrix doped or coated with fluorophores. The direct and/or diffuse sunlight that penetrates the matrix is absorbed by the fluorophores and then re-emitted by them with less energy. The light emitted, thanks to the total internal reflection, propagates until it reaches the edges of the wave guide where it is converted into electricity by photovoltaic cells placed on the perimeter of the matrix. The efficiency of the device is reduced by numerous loss processes, due to the reflection of the matrix and the escape cone, and/or due to the characteristics of the fluorophores, such as the absorption coefficient, the quantum yield (QY) of photoluminescence (PL) and the reabsorption. To minimize losses due to fluorophores, a good alternative are colloidal quantum dots (QDs) that usually have a high QY, a high absorption coefficient and a controllable emission wavelength by changing the size of the nanocrystals. Furthermore, by properly engineering the QDs, it is possible to realize particles with high Stokes-shift between the absorption and emission spectra, in order to reduce the reabsorption as much as possible. The project is focused on the development of the synthesis of QDs, in order to optimize the QY of photoluminescence, compatibility with the polymer matrix and photostability, while limiting the reabsorption. Besides. the synthesis procedure must be easily transferable on industrial volumes, to meet the production needs of high square meters of LSCs. During the three years of the doctoral project in High Apprenticeship I was able to develop a synthesis procedure consisting of four steps: • growth of CuInS2 core nanocrystals; • quaternary formation with zinc addition (ZnCuInS2); crucial step to increase the QY and control the emission wavelength; • growth of a zinc sulphide shell (ZnCuInS2/ZnS) to passivate the surface of nanocrystals, increase QY and photostability; • post-synthesis treatment of the partial exchange of ligands to improve solubility in the polymer matrix. The nanocrystals thus produced show 60% QY and excellent solubility in the polymer matrix. In fact, a large size LSC (30 cm x 30 cm x 0.7 cm) was produced, whose optical power efficiency, OPE = 6.8%. Initially, I developed the synthesis procedure in a 25 ml glass flask, producing 250 mg for batch. Thanks to the equipment provided by Glass to Power s.p.A I was able to study the increase in the scale of the synthesis. Firstly, in order to investigate some possible problems due to the increase in volumes, I have carried out preliminary studies on larger balloons, 500 mL and 2 L. After analysis of heating and quenching of synthesis, I have performed the synthesis in a preindustrial reactor producing 300 g of nanocrystals of ZnCuInS2/ZnS. In addition I also optimized the synthesis procedure. I tested several strategies to increase QY without damaging solubility in the polymer. Thanks to a variation of the reagent in the second step and an increase of the shell layers, I obtained nanocrystals with 80% of QY. The next step will be to scale up this new procedure and produce large LSCs. I collaborated with other PhD students, in particular, I synthesized with a heat-up method CdSe nanocrystals doped with Au7 clusters and decorated with conjugated dyes as efficient triplet sensitizers or up-conversion applications (gold doping improves up-conversion efficiency). The beneficial effects of the doping strategy result in a maximum UC efficiency of 12%, which is an unprecedented result for up-conversion based on decorated NCs as triplet sensitizers.

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Taraborelli, Simone. « Studio del reforming combinato del biogas su nanoparticelle bimetalliche supportate ». Master's thesis, Alma Mater Studiorum - Università di Bologna, 2020. http://amslaurea.unibo.it/21674/.

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The study of the combined reforming (CR) process to produce synthesis gas (CO + H2) feeding Clean Biogas (CB, biogas in which the main pollutants have been removed) has been performed on Ni-based bimetallic catalysts promoted by small amounts of Rh or Cu, prepared by incipient wetness impregnation or coprecipitation of different precursors on mixed oxides Mg/Al/O obtained by calcination of hydrotalcite-type (Ht) coprecipitates. It has been observed as the formation of bimetallic particles promoted the catalytic activity and limited the deactivation phenomena, allowing to operate at lower temperature and feeding lower amounts of steam. By this way, it was possible to define the best promoter, to tune its amount and the formation of the bimetallic nanoparticles. Finally, it has been simulated the scale-up of the CR process to industrial level, evaluating the feasibility and economic degree by comparison with the industrially exploited Autothermal reforming (ATR) process, evidencing the possible scalability and the advantages at environmental and energetic level in comparison to the current reforming processes.

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Castagnini, Simone. « Dal piccolo al grande : scale up e industrializzazione del processo di produzione di un nuovo piretroide sintetico ». Master's thesis, Alma Mater Studiorum - Università di Bologna, 2022.

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Il presente lavoro di tesi ha avuto l’obiettivo di realizzare la fase di Conceptual Design e di avviare la fase di Basic Design preliminari allo sviluppo di un processo industriale per la produzione di un nuovo piretroide dotato di spiccato potere insetticida. Il lavoro svolto si inquadra innanzitutto nell’ambito del Conceptual Design, ovvero nella definizione delle caratteristiche del processo, delle specifiche di prodotto, della sequenza delle operazioni fondamentali, dei dati chimico- fisici delle sostanze coinvolte e, infine, degli aspetti termici e di sicurezza da tenere in considerazione. In particolare, ai fini dello sviluppo del processo, si sono svolte diverse prove sperimentali in laboratorio, utilizzando volumi di reazione via via crescenti. A valle delle prove sperimentali, si è progettato preliminarmente un possibile impianto industriale per la sintesi del piretroide. La tesi è strutturata in 7 capitoli. Dopo il capitolo 1, avente carattere introduttivo, il capitolo 2 descrive le caratteristiche generali dei piretroidi. La descrizione dettagliata del nuovo piretroide e della sua sintesi viene presentata nel capitolo 3, nel quale è anche descritta una possibile via di sintesi dei precursori del piretroide. Nel capitolo 4 è descritto il processo proposto per la sintesi del piretroide in scala di laboratorio e sono esposte dettagliatamente le prove sperimentali, che sono state svolte in reattori del volume di 1 litro, 4 litri e 25 litri. Il capitolo 5 è dedicato alla fase preliminare di Basic Design del processo, ovvero all’implementazione del processo su scala industriale, definendo un possibile impianto industriale per la produzione del piretroide. Nel capitolo 6 si analizza il recupero della piridina dalle acque di scarico ottenute a valle della reazione di sintesi del piretroide, descrivendo 2 metodi sperimentali adatti a questo scopo e approfondendo quello più efficace. Le conclusioni finali della tesi sono riportate nel capitolo 7.

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Chiossi, Francesco. « Sviluppo di un processo in continuo per la sintesi di un intermedio farmaceutico ». Master's thesis, Alma Mater Studiorum - Università di Bologna, 2022. http://amslaurea.unibo.it/25476/.

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In this work process for the coupling reaction between a secondary chiral alcohol and a heterocyclic amine is studied. The chiral configuration must be inverted. The mesylate derivative of the alcohol is known to be unstable, so a continuous process with no isolation is developed for alcohol activation and amine coupling. This approach led to poor results in terms of yield and chiral purity. As an alternative approach, the Mitsunobu reaction is used. The application of flow chemistry to this reaction is promising since it uses highly energetic compounds and has a fast kinetic. Despite these premises, this approach led to worst results in yield and selectivity when using the substrate of interest. The reaction kinetic basically addresses selectivity towards by-products that in this case are reduced by mass transfer limitation. Mass transfer is the rate determining step.

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Crimaldi, Antonio. « Nuovi processi catalitici per la produzione di syngas ». Master's thesis, Alma Mater Studiorum - Università di Bologna, 2019. http://amslaurea.unibo.it/19204/.

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The study of the combined Steam/Dry Reforming (S/DR) process for the production of syngas (CO + H2) from clean biogas was carried out using Ni/Ir bimetallic catalysts on Mg and Al mixed-oxides, obtained by calcination of hydrotalcite-type precursors (Ht) prepared by co-precipitation. The presence of small amounts of Ir promoted the catalytic activity and limited the deactivation phenomena through the formation of a bimetallic alloy, which does the catalyst very active even at lowest temperature and in lack of steam. By integrating a High Temperature–WGS unit (HTS) after the S/DR reactor it was possible to increase the H2 yield of the process. The performance of the Zn/Al/Cu-based catalyst was improved using a templating agent during the synthesis of the catalyst, which increased the catalyst’s structural properties and activity especially at lowest temperatures and at highest contact times. Finally, starting from the laboratory data, it was possible to simulate the S/DR process on industrial scale, evaluating its scalability and environmental impact. The results showed that, using the S/DR technology instead of the current processes, it was possible to reduce the energy costs and the atmospheric emissions of the plant.

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De, Ford D. « Scale-up of bioreactors : The concept of bioreactor number and its relation to the physiology of industrial micro-organisms at different scales ». Thesis, Teesside University, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.380694.

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Fernandes, Tânia Filipa Correia. « Scale up do processo de produção da bolacha Newkcal para a escala industrial - adaptação de uma linha de produção ». Master's thesis, ISA, 2014. http://hdl.handle.net/10400.5/6775.

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Mestrado em Engenharia Alimentar - Processamento de Alimentos - Instituto Superior de Agronomia
This thesis portrays the scale up process of the semi-sweet biscuit production Newkcal from the pilot to industrial scale, highlighting occurred troubles, respective possible causes and the solutions adopted to solve them. These solutions resulted in modifications of the recipe and the biscuit manufacturing process, such as: reducing the total weight of Newkcal dough; opting for a three stage formulation of the dough; production of two different Newkcal formats with different production line speeds; changing the position of the cutting/engraving molds of the dough. The parameters and standards were stipulated for each stage of the manufacturing process. The final product specifications were reset by adjusting the specifications pre-defined while the biscuit production was at a pilot scale: the length and thickness of the biscuit decreased slightly and the width and moisture were increased. The Newkcal biscuit is considered an improvement of the recipe and production process of a previous one: Fruit & Fit. The characteristics of both biscuits were compared and it was verified that Newkcal biscuit has a more compact and less porous structure and is softer than the Fruit & Fit biscuit.

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Reichert, Ute. « Prozessdesign, Prozessoptimierung und scale up am Beispiel des industriell relevanten Enzyms Formiatdehydrogenase aus E. coli ». [S.l. : s.n.], 2002. http://deposit.ddb.de/cgi-bin/dokserv?idn=96841365X.

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Livres sur le sujet "Scale-up industriale"

Mathematical modeling and scale-up of liquid chromatography. Berlin : Springer, 1995.

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1946-, Seaver Sally S., dir. Commercial production of monoclonal antibodies : A guide for scale-up. New York : M. Dekker, 1987.

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Lars, Hagel, dir. Handbook of process chromatography : A guide to optimization, scale up, and validation. San Diego : Academic Press, 1997.

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Minato, Ray. Reactor scale-up of copper-chlorine cycle of hydrogen production from proof-of-principle to large engineering scale. Norwich, N.Y.] : Knovel, 2012.

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1943-, Fink David J., Curran Linda M. 1950-, Allen Billy R. 1948-, National Science Foundation (U.S.) et Battelle Memorial Institute, dir. Research needs in non-conventional bioprocess : Proceedings of the Workshop on Bioprocess Scale-Up, held at Battelle's Columbus Laboratories, December 12-13, 1983. Columbus, Ohio : Battelle Press, 1985.

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India, Reserve Bank of. Report of the study group to examine the issues relating to the setting up of soft loan assistance fund for rehabilitation of sick small scale industrial units. Bombay : Reserve Bank of India, Rural Planning and Credit Dept., 1985.

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Industrial Process Scale-up. Elsevier, 2013. http://dx.doi.org/10.1016/c2012-0-07045-7.

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Industrial Process Scale-Up. Elsevier, 2019. http://dx.doi.org/10.1016/c2018-0-00308-4.

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Tarleton, Stephen, et Richard Wakeman. Solid/Liquid Separation : Scale-Up of Industrial Equipment. Elsevier Science & Technology Books, 2011.

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Solid/Liquid Separation : Scale-up of Industrial Equipment. Elsevier Science, 2005.

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Chapitres de livres sur le sujet "Scale-up industriale"

Castex, Mathieu, Henri Durand et Bernadette Okeke. « Issues with Industrial Probiotic Scale-up ». Dans Aquaculture Nutrition, 347–59. Chichester, UK : John Wiley & Sons, Ltd, 2014. http://dx.doi.org/10.1002/9781118897263.ch13.

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Yang, Xiaoming. « Scale-Up of Microbial Fermentation Process ». Dans Manual of Industrial Microbiology and Biotechnology, 669–75. Washington, DC, USA : ASM Press, 2014. http://dx.doi.org/10.1128/9781555816827.ch47.

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Blacker, A. John, et Peter Thompson. « Scale-Up Studies in Asymmetric Transfer Hydrogenation ». Dans Asymmetric Catalysis on Industrial Scale, 265–90. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2010. http://dx.doi.org/10.1002/9783527630639.ch16.

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Xia, Jianye, Guan Wang, Jihan Lin, Yonghong Wang, Ju Chu, Yingping Zhuang et Siliang Zhang. « Advances and Practices of Bioprocess Scale-up ». Dans Bioreactor Engineering Research and Industrial Applications II, 137–51. Berlin, Heidelberg : Springer Berlin Heidelberg, 2015. http://dx.doi.org/10.1007/10_2014_293.

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Ray, Lopamudra, et Vishakha Raina. « Scale-Up of Engineering Strain for Industrial Applications ». Dans Microbial Engineering for Therapeutics, 311–26. Singapore : Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-3979-2_14.

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Cowan, G. H. « Some Factors Involved in Scale-Up of Industrial Biotechnological Adsorption Processes ». Dans Adsorption : Science and Technology, 505–16. Dordrecht : Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-2263-1_26.

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Maranghi, Simone, Maria Laura Parisi, Riccardo Basosi et Adalgisa Sinicropi. « LCA as a Support Tool for the Evaluation of Industrial Scale-Up ». Dans Life Cycle Assessment in the Chemical Product Chain, 125–43. Cham : Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-34424-5_6.

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Czermak, P., et W. J. Bauer. « Process Optimization of an Enzyme Membrane Reactor with Soluble Enzymes up to Industrial Scale ». Dans Effective Industrial Membrane Processes : Benefits and Opportunities, 241–53. Dordrecht : Springer Netherlands, 1991. http://dx.doi.org/10.1007/978-94-011-3682-2_18.

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Del Valle, E. M., R. Gutierrez et M. A. Galán. « Bioprocess Scale-up : SMB as a Promising Technique for Industrial Separations Using IMAC ». Dans Chemical Engineering, 85–102. Chichester, UK : John Wiley & Sons, Ltd, 2005. http://dx.doi.org/10.1002/0470025018.ch4.

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Rani, Radha, Neha Raina, Azmi Khan, Manupriya Choudhary et Madhu Gupta. « Liposomal-Based Pharmaceutical Formulations – Current Landscape, Limitations and Technologies for Industrial Scale-Up ». Dans Micro- and Nanotechnologies-Based Product Development, 209–24. Boca Raton : CRC Press, 2021. http://dx.doi.org/10.1201/9781003043164-13.

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Actes de conférences sur le sujet "Scale-up industriale"

Kowalczyk, Alexandra, Sebastian Schwede, Mandy Gerber et Roland Span. « Scale Up of Laboratory Scale to Industrial Scale Biogas Plants ». Dans World Renewable Energy Congress – Sweden, 8–13 May, 2011, Linköping, Sweden. Linköping University Electronic Press, 2011. http://dx.doi.org/10.3384/ecp1105748.

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Manske, Eberhard, Thomas Fröhlich, Roland Füssl, Rostyslav Mastylo, Ulrike Blumröder, Paul Köchert, Oliver Birli et al. « Scale spanning subnanometer metrology up to ten decades ». Dans Optical Measurement Systems for Industrial Inspection XI, sous la direction de Peter Lehmann, Wolfgang Osten et Armando Albertazzi Gonçalves. SPIE, 2019. http://dx.doi.org/10.1117/12.2526076.

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Mah, Jeffrey C., Philip Bates et Bobbye Baylis. « Vibration Welding Scale Up - A Comparison of Laboratory and Industrial Components ». Dans SAE 2002 World Congress & Exhibition. 400 Commonwealth Drive, Warrendale, PA, United States : SAE International, 2002. http://dx.doi.org/10.4271/2002-01-0718.

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Hoyt, J. W. « Scale-Up From Laboratory Pipe-Flow Data to Large Flows ». Dans ASME/JSME 2003 4th Joint Fluids Summer Engineering Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/fedsm2003-45656.

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By scale-up, one means the prediction of pressure drop in large industrial or commercial pipelines, or other flow situations, based on results from laboratory-scale small pipe facilities. Scale-up for the use of non-Newtonian fluids or drag-reducing solutions in long-distance oil pipelines, central-station heating or cooling schemes, or application to ship design, are important current interests. A simple analytical approach has been developed which provides excellent scaling over a wide range of pipe sizes for both water-based and oil-based polymer solutions. Examples are given which show close comparisons of scaling from small pipes to actual test data from much larger diameter industrial-scale facilities.

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Griffin, D. « A Proven, Industrial Magnetron Sputtering System With Excellent Expansion And Scale-Up Capabilities ». Dans 31st Annual Technical Symposium, sous la direction de Carl M. Lampert. SPIE, 1987. http://dx.doi.org/10.1117/12.941863.

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PINTO, A. A. L., B. A. C. ROQUE, P. P. F. BRASILEIRO, R. D. RUFINO, J. M. LUNA et e. L. A. SARUBBO. « SCALE–UP DE PRODUÇÃO DE BIOSSURFACTANTE POR CANDIDA SPHAERICA UTILIZANDO RESIDUOS INDUSTRIAS ». Dans XX Congresso Brasileiro de Engenharia Química. São Paulo : Editora Edgard Blücher, 2015. http://dx.doi.org/10.5151/chemeng-cobeq2014-1958-16676-171329.

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Breuer, Roman, et Said Al-Asmi. « Nimr Water Treatment Project -- Up Scaling A Reed Bed Trail To Industrial Scale Produced Water Treatment ». Dans SPE International Conference on Health, Safety and Environment in Oil and Gas Exploration and Production. Society of Petroleum Engineers, 2010. http://dx.doi.org/10.2523/126265-ms.

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Sachs, Marius, Jochen Schmidt, Wolfgang Peukert et Karl-Ernst Wirth. « Design and scale-up of a semi-industrial downer-reactor for the rounding of irregular polymer particles ». Dans PROCEEDINGS OF PPS-31 : The 31st International Conference of the Polymer Processing Society – Conference Papers. AIP Publishing LLC, 2016. http://dx.doi.org/10.1063/1.4942289.

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Han Feng, Li Wenhong et Li Dong. « Comprehensive utilization of dioscorea zingiberensis and industrial scale-up : New approach to pollution prevention in diosgenin industry ». Dans 2011 International Symposium on Water Resource and Environmental Protection (ISWREP). IEEE, 2011. http://dx.doi.org/10.1109/iswrep.2011.5893331.

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Punvichai, Teerasak. « Scale up biodiesel production from palm fatty acid distillate at palm oil refining plant ». Dans 2022 AOCS Annual Meeting & Expo. American Oil Chemists' Society (AOCS), 2022. http://dx.doi.org/10.21748/jhdk5629.

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A study on scale up biodiesel production from palm fatty acid distillate at palm oil refining plant, namely palm oil derived using palm fatty acid distillate (PFAD), collected from the Oleen Palm Oil industrial refining plant. This PFAD showed free fatty acid content and a saponification value of 88.4 % and 204 mg KOH/g respectively. An acid catalyst was successfully used to produce biodiesel in the esterification reaction, and a 97.11% conversion to biodiesel based on the European Standard EN 14214:2003 was achieved under the conditions (PFAD to methanol molar ratio 1:3.71 with 1.834 % H2SO4 catalyzed at 121 ÂºC for 15 minute). Overall, this novel process achieved highly enhanced FAME (95.82% to 97.31%) with a significantly increased reaction time (10 to 30 minutes) and catalyst requirements (1.834 % H2SO4). In conclusion, the acid catalyst with high temperature and pressure showed potential to enhance the esterification reaction rate of PFAD with low biodiesel production costs, high FAME yields and short reaction times.

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Rapports d'organisations sur le sujet "Scale-up industriale"

Powell, Adam Clayton. Industrial Scale-Up of Low-Cost Zero-Emissions Magnesium by INFINIUM Electrolysis. Office of Scientific and Technical Information (OSTI), mars 2018. http://dx.doi.org/10.2172/1431302.

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