Littérature scientifique sur le sujet « Bioreactors design »
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Articles de revues sur le sujet "Bioreactors design"
Malhotra, Neeraj. « Bioreactors Design, Types, Influencing Factors and Potential Application in Dentistry. A Literature Review ». Current Stem Cell Research & ; Therapy 14, no 4 (23 mai 2019) : 351–66. http://dx.doi.org/10.2174/1574888x14666190111105504.
Texte intégralKırdök, Onur, Berker Çetintaş, Asena Atay, İrem Kale, Tutku Didem Akyol Altun et Elif Esin Hameş. « A Modular Chain Bioreactor Design for Fungal Productions ». Biomimetics 7, no 4 (27 octobre 2022) : 179. http://dx.doi.org/10.3390/biomimetics7040179.
Texte intégralChristianson, Laura E., Richard A. Cooke, Christopher H. Hay, Matthew J. Helmers, Gary W. Feyereisen, Andry Z. Ranaivoson, John T. McMaine et al. « Effectiveness of Denitrifying Bioreactors on Water Pollutant Reduction from Agricultural Areas ». Transactions of the ASABE 64, no 2 (2021) : 641–58. http://dx.doi.org/10.13031/trans.14011.
Texte intégralCatapano, Gerardo, Juliane K. Unger, Elisabetta M. Zanetti, Gionata Fragomeni et Jörg C. Gerlach. « Kinetic Analysis of Lidocaine Elimination by Pig Liver Cells Cultured in 3D Multi-Compartment Hollow Fiber Membrane Network Perfusion Bioreactors ». Bioengineering 8, no 8 (23 juillet 2021) : 104. http://dx.doi.org/10.3390/bioengineering8080104.
Texte intégralGrün, Christoph, Brigitte Altmann et Eric Gottwald. « Advanced 3D Cell Culture Techniques in Micro-Bioreactors, Part I : A Systematic Analysis of the Literature Published between 2000 and 2020 ». Processes 8, no 12 (15 décembre 2020) : 1656. http://dx.doi.org/10.3390/pr8121656.
Texte intégralVanags, J., et A. Suleiko. « Oxygen Mass Transfer Coefficient Application in Characterisation of Bioreactors and Fermentation Processes ». Latvian Journal of Physics and Technical Sciences 59, no 5 (1 octobre 2022) : 21–32. http://dx.doi.org/10.2478/lpts-2022-0038.
Texte intégralHartfiel, Lindsey M., Michelle L. Soupir et Kurt A. Rosentrater. « Techno-Economic Analysis of Constant-Flow Woodchip Bioreactors ». Transactions of the ASABE 64, no 5 (2021) : 1545–54. http://dx.doi.org/10.13031/trans.14300.
Texte intégralSirirak, Khanoksinee, Sorawit Powtongsook, Sudarat Suanjit et Somtawin Jaritkhuan. « Effectiveness of various bioreactors for thraustochytrid culture and production (Aurantiochytruim limacinum BUCHAXM 122) ». PeerJ 9 (27 mai 2021) : e11405. http://dx.doi.org/10.7717/peerj.11405.
Texte intégralCatapano, Gerardo, Gionata Fragomeni, Giuseppe Falvo D’Urso Labate, Luigi De Napoli, Vincenza Barbato, Maddalena Di Nardo, Valentina Costanzo, Teresa Capriglione, Roberto Gualtieri et Riccardo Talevi. « Do Bioreactor Designs with More Efficient Oxygen Supply to Ovarian Cortical Tissue Fragments Enhance Follicle Viability and Growth In Vitro ? » Processes 7, no 7 (15 juillet 2019) : 450. http://dx.doi.org/10.3390/pr7070450.
Texte intégralZaburko, J., G. Łagód, M. K. Widomski, J. Szulżyk-Cieplak, B. Szeląg et R. Babko. « Modeling and optimizations of mixing and aeration processes in bioreactors with activated sludge ». Journal of Physics : Conference Series 2130, no 1 (1 décembre 2021) : 012027. http://dx.doi.org/10.1088/1742-6596/2130/1/012027.
Texte intégralThèses sur le sujet "Bioreactors design"
Ntwampe, Seteno Karabo Obed. « Multicapillary membrane bioreactor design ». Thesis, Cape Peninsula University of Technology, 2005. http://hdl.handle.net/20.500.11838/897.
Texte intégralThe white rot fungus, Phanerochaete chrysosporium, produces enzymes, which are capable of degrading chemical pollutants. It was detennined that this fungus has multiple growth phases. The study provided infonnation that can be used to classify growth kinetic parameters, substrate mass transfer and liquid medium momentum transfer effects in continuous secondary metabolite production studies. P. chrysosporium strain BKMF 1767 (ATCC 24725) was grown at 37 QC in single fibre capillary membrane bioreactors (SFCMBR) made of glass. The SFCMBR systems with working volumes of 20.4 ml and active membrane length of 160 mm were positioned vertically. Dry biofilm density was determined by using a helium pycnometer. Biofilm differentiation was detennined by taking samples for image analysis, using a Scanning Electron Microscope at various phases of the biofilm growth. Substrate consumption was detennined by using relevant test kits to quantify the amount, which was consumed at different times, using a varying amount of spore concentrations. Growth kinetic constants were detennined by using the substrate consumption and the dry biofilm density model. Oxygen mass transfer parameters were determined by using the Clark type oxygen microsensors. Pressure transducers were used to measure the pressure, which was needed to model the liquid medium momentum transfer in the lumen of the polysulphone membranes. An attempt was made to measure the glucose mass transfer across the biofilm, which was made by using a hydrogen peroxide microsensor, but without success.
Miller, Stanley David 1960. « Mass separation techniques for the design of fixed film bioreactors ». Thesis, The University of Arizona, 1988. http://hdl.handle.net/10150/276846.
Texte intégralCAPUANA, Elisa. « Design of perfusion bioreactors and PLLA-based scaffolds for in vitro tissue engineering ». Doctoral thesis, Università degli Studi di Palermo, 2022. https://hdl.handle.net/10447/562180.
Texte intégralTissue engineering (TE) represents a novel approach that uses cells integrated with matrices to achieve the formation of new tissues. In this strategy, three essential components constitute the so-called triad of Tissue Engineering: regulatory signals, cells, and three-dimensional (3D) biodegradable porous scaffolds. They are combined to develop an organized 3D functional tissue that mimics the extracellular matrix (ECM) of tissue to be regenerated. The tissue-specific functions of native tissues are linked to complex environments that can be replicated outside the body by using special devices called bioreactors. These systems provide an environment where specific parameters can be controlled to match desired biological conditions. In this thesis, all these components are accounted for developing in vitro models for various applications in the field of Tissue Engineering. Specifically, poly-(L-lactic acid) (PLLA)-based scaffold, scaffold fabrication via phase separation, static cell cultures, and dynamic cell cultures using perfusion bioreactors are analyzed and discussed. Two main sections compose this thesis: several experimental setups using PLLA-based scaffolds for various in vitro systems; and the design and modeling of a custom perfusion bioreactor using computational fluid dynamics (CFD) and mathematical equations. A rigorous theoretical framework is developed to study the properties of PLLA biomaterial, the use of perfusion bioreactor for regenerative medicine, and models developed for investigating cells growth on 3D matrices cultured within a dynamic system. In the experiments, the morphology of different PLLA scaffolds produced through different protocols of the thermally induced phase separation technique (TIPS) is analyzed according to the targeted properties of TE scaffolds, i.e., porosity, pore interconnectivity, and pore size. Cell cultures are performed in these constructs to create a 3D environment so that seeded cells can grow both in static 3D culture and the perfusion bioreactor. Cell proliferation and adhesion are observed up to 7 days of in vitro culture, demonstrating that scaffold morphology can induce cell growth under both static and dynamic conditions. For the second part, a combined modeling and experimental approach is followed. The custom-made perfusion apparatus is an existing airlift bioreactor that provides a low-shear environment with good mixing, resolving mass transport limitations and providing physical stimuli beneficial for overall cells proliferation and differentiation. The hydrodynamics (gas holdup, superficial liquid velocity, and shear rate) and mass transfer (kLa and the volumetric mass transfer coefficient) are modeled and determined by CFD to examine the influence of Abstract iii these features on cell and tissue growth. The simulation results indicate that the hydrodynamics matched the mathematical data and experimental validation. Then, osteoblast cells are cultured on a support in the bioreactor perfused with culture medium at 10mL/min for up to 6 days. An evaluation combining proliferation results and statistical analysis allows the quantification of cell growth as a function of the space inside the system. Given the hierarchical nature of the bioreactor-scaffold system, its multi-scale nature will be considered, ranging from the extracellular matrix scale to the bioreactor scale. The flow-dependent properties of an engineered matrix cultured within a perfusion bioreactor are studied theoretically and evaluated experimentally, emphasizing the influence of inter-scale dependencies. Perfusion bioreactors are in vitro systems beneficial for drug screening because they mimic the in vivo environment. For this purpose, an optimized design of the airlift bioreactor that can induce a double-flow on a hollow scaffold is theoretically and experimentally validated. Specifically, the system is tested for carriers diffusion and air-liquid-interface (ALI) model to reproduce the nasal mucosa environment. The rationale is to combine an internal and an external flow of independent fluids for either diffusing the carriers throughout the engineered matrix for drug prescreening or redirecting the culture medium to feed the cells seeded into the channel of the hollow scaffold. In conclusion, this thesis project focuses on the major aspects of tissue engineering and regenerative medicine, varying from in vitro tests for growing cells on scaffolds toward models to study the multi-scale nature of a tissue-like system or recreate the physiology of a native tissue.
Phelan, Michael. « THE DESIGN, CONSTRUCTION, AND VALIDATION OF NOVEL ROTATING WALL VESSEL BIOREACTORS ». Master's thesis, Temple University Libraries, 2018. http://cdm16002.contentdm.oclc.org/cdm/ref/collection/p245801coll10/id/488702.
Texte intégralM.S.
The rotating wall vessel (RWV) bioreactor is a well-established cell culture device for the simulation of microgravity for suspension cells and the generation of spheroids and organoids. The key to the success of these systems is the generation of a delicately maintained fluid dynamics system which induces a solid body rotation capable of suspending cells and other particles in a gentle, low-shear environment. Despite the unique capabilities of these systems, the inherently delicate nature of their fluid dynamics makes the RWV prone to multiple failure modes. One of the most frequently occurring, difficult to avoid, and deleterious modes of failure is the formation of bubbles. The appearance of even a small bubble in an RWV disrupts the crucial laminar flow shells present in the RWV, inducing a high-shear environment incapable of maintaining microgravity or producing true spheroids. The difficulty of eliminating bubbles from the RWV substantially increases the learning curve and subsequent barrier-to-entry for the use of this technology. The objective of this study is to create a novel RWV design capable of eliminating the bubble formation failure mode and to demonstrate the design’s efficacy. The tested hypothesis is: “The addition of a channel capable of segregating bubbles from the fluid body of the RWV will protect its crucial fluid dynamics system while enabling the growth of consistently sized and properly formed cell spheroids, improving ease of use of the RWV and decreasing experimental failure.”
Temple University--Theses
Williams, Chrysanthi. « Perfusion bioreactor for tissue-engineered blood vessels ». Diss., Available online, Georgia Institute of Technology, 2004:, 2003. http://etd.gatech.edu/theses/available/etd-06072004-131410/unrestricted/williams%5Fchrysantyhi%5F200405%5Fphd.pdf.
Texte intégralHanna, Molin. « Optimal steady-state design of bioreactors in series with Monod growth kinetics ». Thesis, Uppsala universitet, Avdelningen för systemteknik, 2018. http://urn.kb.se/resolve?urn=urn:nbn:se:uu:diva-338760.
Texte intégralBioreaktorer används för att utföra olika biologiska processer och används vanligen inom biogasproduktion eller för rening av avloppsvatten. Två vanliga hydrauliska modeller som används vid modellering av bioreaktorer är helomblandad bioreaktor (på engelska continuous stirred tank reactor, CSTR) eller pluggflödesreaktor (på engelska plug-flow reactor, PFR). I den här rapporten presenteras ett system av differentialekvationer som används för att beskriva koncentrationerna av substrat, biomassa och inert biomassa i både CSTR och PFR. Ekvationssystemet används för analys och design av en serie CSTRs vid steady-state. Tillväxten av biomassa beskrivs av Monod-kinetik. Avdödning av biomassa är inkluderat i studien. Från ekvationssystemet formulerades två optimeringsproblem som löstes för N CSTRs i serie och för CSTR+PFR. Det första optimerinsproblemet var att minimera substrathalten i utflödet givet en total volym. I det andra minimerades den totala volymen som krävs för att nå en viss substrathalt i utflödet. Resultaten visade att ekvationssystemet kan användas för att hitta den optimala volymsfördelningen som löser optimeringsproblemen. Den optimala volymen för N CSTRs i serie minskade när antalet CSTRs ökade. När N ökade konvergerade resultaten mot de för en CSTR sammankopplad med en PFR. En analys av hur avdödningshastigheten påverkade resultaten visade att en ökad avdödningshastighet gav mindre skillnad mellan de två olika konfigurationerna när den totala volymen hölls konstant. När den totala volymen istället minimerades ledde en ökad avdödningshastighet till att de två konfigurationerna divergerade från varandra. Modellen som presenteras i studien kan användas för att fördela en total reaktorvolym i mindre zoner på ett optimalt sätt och på så vis öka substratomvandlingen, något som kan vara av intresse i exempelvis befintliga avloppsreningsverk där utrymmet är begränsat. En relativt bra approximation till den optimala designen av N CSTRs i serie är att optimera volymerna för en CSTR+PFR, använda volymen för CSTR som första volym i konfigurationen med N CSTR i serie, och sedan fördela den kvarvarande volymen lika mellan de övriga zonerna.
Betts, Jonathan Ian. « The design and characterisation of miniature bioreactors for microbial fermentation process development ». Thesis, University College London (University of London), 2006. http://discovery.ucl.ac.uk/1445372/.
Texte intégralMorello, Luca. « Sustainable landfilling : hybrid bioreactors and final storage quality ». Doctoral thesis, Università degli studi di Padova, 2017. http://hdl.handle.net/11577/3424792.
Texte intégralIl moderno sistema di deposito finale dei rifiuti in discarica costituisce un passaggio inevitabile nella gestione dei rifiuti solidi. Il suo scopo è chiudere il “ciclo della materia” riportando gli elementi allo stato di immobilità in cui erano prima di essere estratti. Contemporaneamente, l’applicazione del principio di sostenibilità alle discariche prescrive di garantire la salvaguardia ambientale e della salute, assicurando che il rifiuto smaltito diventi chimicamente e bio-chimicamente stabile entro un tempo “ragionevole”. Una “Discarica Sostenibile” deve combinare questi due principi, bilanciando i contributi per ottenere una “chiusura sostenibile del ciclo della materia”. Il potenziamento dei processi biochimici in discarica, con lo scopo di raggiungere più velocemente condizioni che garantiscano la salvaguardia ambientale e terminare la fase di post-chiusura, è uno degli argomenti più dibattuti nella letteratura scientifica inerente alla gestione dei rifiuti. Lo scopo generale del progetto di dottorato è stato contribuire a questo dibattito, mediante lo svolgimento di test in scala di laboratorio utili a simulare l’andamento dei processi in discarica e analizzando lo stato biochimico finale dei rifiuti trattati. La prima parte del lavoro consiste in una panoramica sui processi biochimici in discarica e sulla metodica dei test biochimici in scala di laboratorio. L’approccio usato dallo studente in questa tesi è principalmente sperimentale, basato sulla progettazione, l’esecuzione e la rielaborazione dei dati di svariate simulazioni di discarica in laboratorio. La discussione dei risultati ottenuti è stata propedeutica alla valutazione delle performance dei modelli concettuali testati così come al confronto con altri risultati ottenuti grazie a una approfondita ricerca bibliografica. Il lavoro originale svolto dallo studente può essere diviso in tre progetti principali. Il reattore ibrido Semi-aerobico, Anaerobico, Aerato (S.An.A ®) è una concetto innovativo testato in scala di laboratorio con promettenti risultati per quanto concerne la stimolazione della produzione di metano e la riduzione delle emissioni di lungo termine. Gli effetti del ricircolo del concentrato di percolato da osmosi inversa all’interno del corpo rifiuti di una discarica sono stati analizzati per verificare se possano esistere potenziali accumuli di contaminanti che rendano insostenibile tale pratica. La procedura di Final Storage Quality (FSQ) per determinare la chiusura della fase di aftercare di una discarica è stata testata su un rifiuto sovra-stabilizzato di sui sono state calcolate emissioni totali e la speciazione chimica degli elementi principali.
Hamnström, Johanna. « Design of a Smartphone App for Control of Bioreactors Used for Cell Cultivation ». Thesis, Uppsala universitet, Institutionen för informationsteknologi, 2012. http://urn.kb.se/resolve?urn=urn:nbn:se:uu:diva-173123.
Texte intégralGill, N. K. « Design and characterisation of parallel miniature bioreactors for bioprocess optimisation and scale-up ». Thesis, University College London (University of London), 2008. http://discovery.ucl.ac.uk/1445974/.
Texte intégralLivres sur le sujet "Bioreactors design"
Reinhart, Debra R. Landfill bioreactor design and operation. Boca Raton, Fla : Lewis Publishers, 1998.
Trouver le texte intégral1949-, Tramper J., dir. Basic bioreactor design. New York : M. Dekker, 1991.
Trouver le texte intégral1949-, Tramper J., dir. Basic bioreactor design. New York : M. Dekker, 1991.
Trouver le texte intégralBioreactor design fundamentals. Boston : Butterworth-Heinemann, 1991.
Trouver le texte intégralS, Cabral Joaquim, Mota Manuel et Tramper J. 1949-, dir. Multiphase bioreactor design. London : Taylor & Francis, 2001.
Trouver le texte intégral(Project), BIOTOL, Open Universiteit (Heerlen Netherlands) et Thames Polytechnic, dir. Bioreactor design and product yield. Oxford : Butterworth-Heinemann, 1992.
Trouver le texte intégral1962-, Mitchell David A., Krieger Nadia et Berovic M, dir. Solid-state fermentation bioreactors : Fundamentals of design and operation. Berlin : Springer, 2006.
Trouver le texte intégralYang, Zhao. Design and Testing of Digital Microfluidic Biochips. New York, NY : Springer New York, 2013.
Trouver le texte intégralVieth, W. R. Membrane systems : Analysis and design : applications in biotechnology, biomedicine, and polymer science. Munich : Hanser Publishers, 1988.
Trouver le texte intégralVieth, W. R. Membrane systems : Analysis and design : applications in biotechnology, biomedicine, and polymer science. New York : J. Wiley, 1994.
Trouver le texte intégralChapitres de livres sur le sujet "Bioreactors design"
Zeilinger, Katrin, et Jörg C. Gerlach. « Artificial Liver Bioreactor Design ». Dans Bioreactors, 147–74. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch5.
Texte intégralMandenius, Carl-Fredrik. « Challenges for Bioreactor Design and Operation ». Dans Bioreactors, 1–34. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch1.
Texte intégralRathore, Anurag S., Lalita Kanwar Shekhawat et Varun Loomba. « Computational Fluid Dynamics for Bioreactor Design ». Dans Bioreactors, 295–322. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch10.
Texte intégralMandenius, Carl-Fredrik, et Robert Gustavsson. « Soft Sensor Design for Bioreactor Monitoring and Control ». Dans Bioreactors, 391–420. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch14.
Texte intégralOosterhuis, Nico M. G., et Stefan Junne. « Design, Applications, and Development of Single-Use Bioreactors ». Dans Bioreactors, 261–94. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch9.
Texte intégralMandenius, Carl-Fredrik. « Design-of-Experiments for Development and Optimization of Bioreactor Media ». Dans Bioreactors, 421–52. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch15.
Texte intégralLattermann, Clemens, et Jochen Büchs. « Design and Operation of Microbioreactor Systems for Screening and Process Development ». Dans Bioreactors, 35–76. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch2.
Texte intégralFerrer, Pau, et Francisco Valero. « Coping with Physiological Stress During Recombinant Protein Production by Bioreactor Design and Operation ». Dans Bioreactors, 227–60. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527683369.ch8.
Texte intégralHiggins, James, Al Mattes, William Stiebel et Brent Wootton. « The Design of EEB Systems ». Dans Eco-Engineered Bioreactors, 215–38. Boca Raton : Taylor & Francis, CRC Press, 2018. : CRC Press, 2017. http://dx.doi.org/10.1201/9781315166810-8.
Texte intégralVilladsen, John. « Design of Ideal Bioreactors ». Dans Fundamental Bioengineering, 319–56. Weinheim, Germany : Wiley-VCH Verlag GmbH & Co. KGaA, 2015. http://dx.doi.org/10.1002/9783527697441.ch10.
Texte intégralActes de conférences sur le sujet "Bioreactors design"
Neitzel, G. Paul, Robert M. Nerem, Athanassios Sambanis, Marc K. Smith, Timothy M. Wick, Jason B. Brown, Christopher Hunter et al. « Effect of Fluid-Mechanical and Chemical Environments on Cell Function and Tissue Growth : Experimental and Modeling Studies ». Dans ASME 1998 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 1998. http://dx.doi.org/10.1115/imece1998-0794.
Texte intégralCruel, Magali, Morad Bensidhoum, Laure Sudre, Guillaume Puel, Virginie Dumas et Thierry Hoc. « Study of the Effect of Mechanical Loading on Cell Cultures in Bone Tissue Engineering ». Dans ASME 2012 11th Biennial Conference on Engineering Systems Design and Analysis. American Society of Mechanical Engineers, 2012. http://dx.doi.org/10.1115/esda2012-82989.
Texte intégralKadic, Enes, et Theodore J. Heindel. « Hydrodynamic Considerations in Bioreactor Selection and Design ». Dans ASME 2010 3rd Joint US-European Fluids Engineering Summer Meeting collocated with 8th International Conference on Nanochannels, Microchannels, and Minichannels. ASMEDC, 2010. http://dx.doi.org/10.1115/fedsm-icnmm2010-30367.
Texte intégralBertrand, Robert S., Emmanuel Revellame, Lisa Stephanie Dizon, Kristel Gatdula et Remil Aguda. « Measurement of Volumetric Mass Transfer Coefficient in Lab-scale Stirred Tank Reactors : Is There a Point of Diminishing Returns for Impeller Speed and Gas Flowrate ? » Dans 2022 AOCS Annual Meeting & Expo. American Oil Chemists' Society (AOCS), 2022. http://dx.doi.org/10.21748/zrrh2541.
Texte intégralPatenaude, Jeffrey A., Aaron Desjarlais, Jessica Kornfeld, Michael Lee, Matthew McGrath, Jeffrey Perry et Jeffrey W. Ruberti. « Design of Optically Accessible, Ultra Low-Volume, Tissue Loading Bioreactor ». Dans ASME 2009 Summer Bioengineering Conference. American Society of Mechanical Engineers, 2009. http://dx.doi.org/10.1115/sbc2009-206675.
Texte intégralHijazi, Rayane, Jihane Rahbani Mounsef et Hadi Y. Kanaan. « Design Considerations for Photo-Bioreactors : A Review ». Dans 2020 5th International Conference on Renewable Energies for Developing Countries (REDEC). IEEE, 2020. http://dx.doi.org/10.1109/redec49234.2020.9163888.
Texte intégralFerrar, Joseph, Philip Maun, Kenneth Wunch, Joseph Moore, Jana Rajan, Jon Raymond, Ethan Solomon et Matheus Paschoalino. « High Pressure, High Temperature Bioreactors as a Biocide Selection Tool for Hydraulically Fractured Reservoirs ». Dans SPE Hydraulic Fracturing Technology Conference and Exhibition. SPE, 2021. http://dx.doi.org/10.2118/204198-ms.
Texte intégralChristianson, Laura, Alok Bhandari et Matt Helmers. « Potential Design Methodology for Agricultural Drainage Denitrification Bioreactors ». Dans World Environmental and Water Resources Congress 2011. Reston, VA : American Society of Civil Engineers, 2011. http://dx.doi.org/10.1061/41173(414)285.
Texte intégralMagarotto, E., T. Ahmed-Ali et M. Haddad. « A new sampled-data observer design for bioreactors ». Dans 2022 8th International Conference on Control, Decision and Information Technologies (CoDIT). IEEE, 2022. http://dx.doi.org/10.1109/codit55151.2022.9804131.
Texte intégralTandon, N., A. Marsano, C. Cannizzaro, J. Voldman et G. Vunjak-Novakovic. « Design of electrical stimulation bioreactors for cardiac tissue engineering ». Dans 2008 30th Annual International Conference of the IEEE Engineering in Medicine and Biology Society. IEEE, 2008. http://dx.doi.org/10.1109/iembs.2008.4649983.
Texte intégralRapports d'organisations sur le sujet "Bioreactors design"
Kendall, Edward. Bioreactors : Design, Background, and Applications. Office of Scientific and Technical Information (OSTI), septembre 2022. http://dx.doi.org/10.2172/1887112.
Texte intégralShuler, Michael L. Development of Cell Models as a Basis for Bioreactor Design for Genetically Modified Bacteria. Fort Belvoir, VA : Defense Technical Information Center, octobre 1986. http://dx.doi.org/10.21236/ada174571.
Texte intégralKnotek-Smith, Heather, et Catherine Thomas. Microbial dynamics of a fluidized bed bioreactor treating perchlorate in groundwater. Engineer Research and Development Center (U.S.), septembre 2022. http://dx.doi.org/10.21079/11681/45403.
Texte intégralHusson, Scott M., Viatcheslav Freger et Moshe Herzberg. Antimicrobial and fouling-resistant membranes for treatment of agricultural and municipal wastewater. United States Department of Agriculture, janvier 2013. http://dx.doi.org/10.32747/2013.7598151.bard.
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